expansion from 0.6 mtpa non recovery coke ......2006 shall be provided. copies of consent to...
TRANSCRIPT
EIA/EMP REPORT for
EXPANSION FROM 0.6 MTPA NON RECOVERY COKE OVEN & 40 MW POWER PLANT TO 1.0 MTPA INTEGRATED STEEL PLANT, 1.2
MTPA NON RECOVERY COKE OVEN & 205 MW POWER PLANT of
BENGAL ENERGY LIMITED DAUKA, TENTULMURI,PASCHIM MEDINIPUR, WEST BENGAL
Accredited Consulting Organization GLOBAL TECH ENVIRO EXPERTS PVT.
LTD.
C-23, BJB NAGAR, BHUBANESWAR-
751014, ODISHA, PH. NO.-0674-2433487
EMAIL- [email protected]
NABET ACCREDITATED
CATEGORY “A” CONSULTANT
SL. NO.- 77
Accredited Laboratory KALYANI LABORATORIES PVT. LTD.
PLOT NO. 78/944, BALIANTA, PAHAL,
BHUBANESWAR, ODISHA
MoEF&CC ACCREDITATION NO. 125
FOR THE PERIOD OF 06.08.2014 TO
05.08.2019
NABL ACCREDITATION NO. TC-7043
FOR THE PERIOD OF
16.03.2017 TO 15.03.2020
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, WB
TC - 1 Global Tech Enviro Experts Pvt. Ltd.
Compliance to the prescribed Terms of Reference vide Ltr no J-11011/28/2008-IA.II(I) dt:
21.06.17
Sl.No ToR Conditions Action Taken in EIA & EMP Report
Specific ToR CHAPT
ERS BRIEF DESCRIPTION
1 Public Hearing shall be conducted by SPCB
CH7
PH was conducted by SPCB on
15.05.2018 at Project Site, Dauka,
Dist-Paschim Medinipur, West
Bengal. The details are given in Pg
214-224.
2
The issues raised during PH and commitment
of the project proponent on the same along
with time bound action plan to implement the
commitment and financial allocation thereto
should be clearly provided
Ch7
The issues raised during PH and
commitment of PP along with
budgetary expenditure of Rs 1810
lakhs, expenditure budget head,
time schedule has been given in
para 7.8 in Pg 224-226
3
Project proponent should carry out social
impact assessment of the project as per the
OM J-11013/25/2014-IA-I dt 11.08.2014
issued by the ministry regarding the
guidelines on environment sustainability and
enterprise social commitment (ESC) related
issues. The SIA study so carried out should
form part of EIA/EMP report
CH7 Social Impact assessment study
has been conducted as per the OM
issued by Ministry and the detailed
SIA has been attached as Annexure
VI
4
Detailed specification of Air Pollution Control
Equipment shall be provided in EIA/EMP. Post
Project monitoring shall be clearly specified
along with the no. of locations, stations,
frequency of monitoring, parameters to be
monitored, fund provision etc
CH6
The detail action plan along with
monitoring schedule & frequency is
illustrated in table 6.1 from page
187.
5
Permission for drawl of Surface water as
proposed shall be provided alongwith
EIA/EMP.
CH 2
Permission exists for drawl of
14,400 M3/day water from
Kangsabati River. The permission
letter is attached as Annexure III
6
Green belt in 33% of the project area shall be
planned with local and broad-leaved species
and details of species, number, location,fund
provision etc shall be provided in the EIA/EMP.
CH4
11,216 nos. of trees have already
been planted in about 56.0 ha of
land which is about 34 % of the
total area. The detail plan is given
in para 4.8 Pg 177-178
7
The Project proponent shall identify railaway
siding points to be used most frequently by it
for transportation of materials and goods.
CH 2
The company has developed its
own railway siding at Benapur
station on Kharagpur-Balasore-
Bhadrak Section of SE railway. The
permission letter is attached as
Annexure II
8
The plant shall be planned to Zero Liquid
Discharge (ZLD)
CH 2
The waste water generated from
various operations shall be trated
and reused. No effluent shall be
discharged outside. The company
has envisaged Zero Liquid
Discharge.
9
The plan for concreted floor with covered
storage of raw materials and coal shall be
provided in the EIA/EMP
Ch 2
All the raw materials will be stored
under shed and over concrete floor.
The details is given in Pg 56
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, WB
TC - 2 Global Tech Enviro Experts Pvt. Ltd.
10
The project proponent shall plan for solar light
system for all common areas, street lights,
villages, parking around the project area and
maintain the same regularly. CH 2
Power saving measures to be
undertaken for the plant includes
plan for LED lights in residential
area and solar syatems in
peripheral areas. Details provided
in Pg 64 11
The Project proponent plan for LED lights in
their offices and residential areas.
12
The proponent shall submit plan for solid
waste management as per the provisions of
SWM Rules, 2016 for thei residential colony as
a part of the EIA/EMP report.
CH 2
The detailed solid waste
Management Plan has been given
in table 2.4, under para 2.6.6 Pg 64
Standard ToR CHAPT
ERS BRIEF DESCRIPTION
1 Executive Summary
The Executive Summary includes
the desired configuration, technical
details, present environmental
status, Impact, Environmental
Management Plan along with
budgetary provisions. The details
are enclosed in page 7-15.
2 Introduction
i. Details of the EIA consultant including NABET
Accreditation CH 1
The consultant for this project is
M/s Global Tech Enviro Experts Pvt
Ltd., Bhubaneswar. They are
NABET accreditated “ A” Category
Consultant. Details of the
consultant has been given in
Chapter - 2 at page no 21.
ii. Information about the project proponent CH 1
Mr. Rajeev maheswari is the owner
of this project. He has about 25
years of experience in Steel
production. Detailed information is
provided in Para 1.2 of Chapter - I
page no17.
iii. Importance and benefits of the project CH 1
The project is located at Dauka,
PS- Tentulmuri, Dist-Paschim
Medinipur, West Bengal Given in
Para 1.3.3 of Chapter - 1 page no
18-19.
3 Project Description
i. Cost of project and time of completion. CH 2
The approximate cost of the project
is 4943 crores. The tentative
completion time is 3 years. The
details are provided Para 2.6.8 &
2.6.9 of Chapter - 2 page no 71-72
ii Products with capacities for the proposed
project CH 2
The proposed project is an
expansion project from 0.6 MTPA
Coke Oven and 40 MW power to
1.2 MTPA Coke oven, 205 MW
power and 1.0 MTPA Integrated
Steel Plant. The details of the
configuration is provided in Para
2.4 in table no 2.2 of chapter - 2
page no 29
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, WB
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iii.
If Expansion project, details of existing
products with capacities and whether
adequate land is available for expansion,
reference of earlier EC if any.
The proposed project is expansion
of existing facilities. The total land
available for the project is 161.87
ha. Plant facilities cover 131.1 ha
and balance 30.77 ha is vacant
area for future expansion.
iv List of raw materials required and their source
along with mode of transportation . CH 2
The major raw Materials are Iron
Ore, Coal, Pig Iron The details of
their procurement, their source and
mode of transportation is explained
in Para 2.6.3 in chapter - 2 page
no 56 & 58
v Other chemicals and materials required with
quantities and storage capacities CH 2
vi Details of emission, effluents, hazardous
waste generation and their management. CH 7
The existing plant had 2 no. of
stacks attached to Coke oven,
RMHP. The proposed expansion will
have additional 12 no. of stacks
attached to DRI Kiln, IF, EAF
Sinter, additional Coke Oven & CPP.
The detail is given in table 4.5.
6387 m3/day of waste water is
generated which is treated in ETP
and reused in the process. Detailed
water balance diagram & Schematic
diagram of ETP is provided para
2.10 in chapter-2. There is no
hazardous waste generated from
the process. However, small
amount of hazardous wastes like
Spent Oil, ETP Sludge & Oil filters
will be generated. The detail
management plan is given in para
4.9 page 167.
vii
Requirement of water, power, with source of
supply, status of approval, water balance
diagram, man-power requirement(regular and
contract)
CH 2
13,165 m3/day of fresh water will
be drawn from Kangsabat river.
153 MW of power will be required.
Total manpower requirement is
1355 both regular & contract
Permission letter with water
balance diagram is given in para
2.6.4 to 2.6.5 page no 59-62. The
permission letters are annexed as
Annexure III.
viii
Process description along with major
equipments and machineries, process flow
sheet (quantitative) from raw material to
products to be provided.
CH 2
Process description along with
major equipments and machineries,
process flow sheet (quantitative)
from raw material to products has
been given in para 2.5.2 of
Chapter - 2 page31-46
ix Hazard identification and details of proposed
safety system CH 7
Hazard identification & Risk
Analysis with safety system
proposed for th project has been
illustrated in para 7.4 in chapter -
7, 193-195
x Expansion/modernisation proposals:
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, WB
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a. Copy of all the environmental
Clearance(s) including Amendments thereto
obtained for the project from MoEF / SEIAA
shall be attached as an Annexure. A certified
copy of the latest Monitoring Report of the
regional Office of the Ministry of Environment
and forests as per circular dated 30th may,
2012 on the status of compliance of conditions
stipulated in all the existing environmental
clearances including Amendments shall be
provided. In addition, status of compliance of
consent to operate for the ongoing existing
operation of the project from SPCB shall be
attached with the EIA- EMP report.
EC was granted on 02.01.2009
vide letter no J-11011/28/2008-IA-
II(I)
Certified RO monitoring report
shows minor compliances was
detected. The PAs have already
complied to the conditions
identified by RO. PAs have already
complied to the conditions
identified by RO. The details are
attached as Annexure I
CTO exists for the existing plant
and is valid till 31.03.2022 vide
letter No. 5899-2359/WPB(HRO)-
K/2009.
b. In case the existing project has not
obtained environmental clearance, reasons for
not taking EC under the provisions of the EIA
Notification 1994 and/ or EIA Notification
2006 shall be provided. Copies of consent to
establish/ No objection Certificate and consent
to operate (in case of units operating prior to
EIA Notification 2006, CTE and CTO of fy
2005-2006 ) obtained from the SPCB shall be
submitted. Further, compliance report to the
further, compliance report to the conditions of
consents from the SPCB shall be submitted.
Not Applicable
4 Site details
i
Location of the project site covering village,
Taluka/ Tehsil, District and state, justification
for selecting the site, whether other sites were
considered.
CH 2
The project is located at Dauka
village of Pachim Medinipur District
of West Bengal. Location of the
project with all details has been
given in para 2.3 of Chapter - 2 &
in Chapter - 5 .No alternate site
was considered as the project is
the to be proposed in existing land.
ii
A topo sheet of the Study area of radius of 10
km and site location on1:50:000/1:25:000
scale on an A3/A2 sheet.(including all eco
sensitive areas and environmentally sensitive
places).
CH 2
The project comes under Survey of
India Toposheet no F45J6. Site
location is given in para 2.3.2 in
chapter - 2 , fig 2.1 Page 26
iii Co –ordinates (lat-long) of all 4 corner of the
site.
CH 2
The project site extends from 22
15’ 22.96’’ N to 22 15’ 27.68’’ N
and 87 22’ 53.37’’ E to 87 23’
34.69’’ N with AMSL 32m .Table of
boundary coordinates along with
google map is in ch- 2, Fig 2.2,
page no 28, .
iv Google map- Earth downloaded of the project
site
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, WB
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v
Layout maps indicating existing unit as well as
proposed unit indicating storage area, plant
area, green belt area, utilities etc. If located
within an industrial area / Estate /Complex,
lay out of industrial area indicating location of
unit within the industrial area
CH 2
Lay out map showing existing unit
in blue color & proposed units in
pink color with all the facilities is
given in Fig - 2.5 of ch - 2. page 55
vi
Photographs of the proposed and existing (if
applicable) plant site. If existing, show
photographs of plantation/ green belt, in
particular.
CH 3
Photographs of existing facilities in
14.97 ha & Green Belt plantation
in 53.41 ha with its direction is
provided in para 3.2 under site
description in ch- 3 page no 73-76.
vii
Land use break-up of total land of the project
site( identified and acquired), Gov./ pvt.-
Agricultural, forest, wasteland, water bodies,
settlements, etc shall be included.(not
required for industrial area)
CH 2
Total land required for the project
is 131.1 ha. Total of 161.87 ha has
been acquired by the proponent.
Land schedule with land use
breakup is given in para 2.6.1 table
2.1 in chapter - 2 page no 52-53.
viii
A list of major industries with name and type
within study area (10km radius) shall be
incorporated. Land use details of the study
area
CH 3
The project is surrounded by 2
nos. of Steel Industries within 10
km radius. The list of industries is
given in table no - 3.2 in ch - 3
page no 79.
ix Geological features and Geo hydrological
status of the study area shall be included. CH 3
The area is dominated by
Metamorphic rocks. The main rivers
are Subarnarekha and Kangsabati.
The geological & geohydrological
features is provided in para 3.5.4 &
3.5.6 of ch- 3 in page no 97-100.
x
Details of the drainage of the project up to 5
km radius of study area. If the site is within
1km radius of any major river, peak and lean
season river discharge as well as flood
occurrence frequency based on peak rainfall
data of the past 30 years. Details of the flood
level of the project site and maximum flood
level of the river shall all so be provided.
(Mega green field projects)
CH 3
The nearest river is Kangsabati,
about 16.7 km away from the site.
The HFL is at a distance of 16.5 km
from the site. 10 km radius
Drainage, with description of the
area has been provided in chapter
3 in para 3.5.6.
xi
Status of acquisition of land. If acquisition is
not complete, stage of acquisition process and
expected time of complete possessions of the
land.
CH 2
The company owns 161.87 ha of
land for its existing and expansion
facilities. The details of land
breakup is in para 2.6.1 table 2.1
in chapter - 2 page no 52-53..
xii R & R details in respect of land in line with
state Govt policy. CH 3
There was no settlement in
acquired industrial land or the land
tobe acquired. Hence R&R does not
arise.
5 Forest & wild life Related issues(If applicable): The existing land on which
modification and expansion is
proposed has been allotted in
Raturia Industrial Area. No forest
land is involved in the project.
i
Permission and approval for the use of forest
land (forestry clearance), if any, and
recommendations of the State Forest
department.(If applicable)
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, WB
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ii
Land use map based on high resolution
satellite imagery (GPS) of the proposed site
delineating the forestland (in case of projects
involving forest land more than 40 ha).
iii
Status of application submitted for obtaining
the stage 1forestry clearance along with latest
status shall be submitted.
iv
The projects to be located within 10 km of the
National parks, Sanctuaries, biosphere
Reserves, Migratory Corridors of wild Animals,
the project proponent shall submit the map
duly authenticated by chief wildlife Warden
showing these features vis-a-vis the project
location and the recommendations or
comments of the chief wildlife Warden-
thereon.
v
Wildlife Conservation plan duly authenticated
by the chief Wildlife Warden of the state
Government for conservation of schedule1
fauna, if any exists in the study area.
vi
Copy of application submitted for clearance
under the wildlife (protection) Act, 1972, to
Standing Committee of the national Board for
Wildlife.
6 Environmental Status
i
Determination of atmospheric inversion level
at the project site-Specific micro-metrological
data using temperature, relative humidity,
hourly wind Speed and direction and rainfall
CH 3
Atmospheric inversion level at 7.00
am is 40m-80m & at 2.00 pm is
1000m-1150m. Inversion level
using site specific temp., humidity,
wind speed & direction is given in
Ch - 3 from page no 96 under
section 3.5.3
ii
AAQ data (except monsoon) at 8 locations for
PM 10. PM 2.5, SO2, Nox, CO and other
parameters relevant to the project shall be
collected. The monitoring stations shall be
based CPCB guidelines and take into account
the pre-dominate wind direction, population
Zone and sensitive receptors including
reserved forests
CH 3
8 locations were identified as per
windrose diagram and CPCB
guidelines namely Keshuriya,
bargopal, Daharpur, Nutandih, Silti,
Belti, Shalka, Mirjapur. Major
parameters like PM10, PM2.5, SO2,
NOx ,CO monitored and the details
are illustrated in Table 3.10 from
page no 91.
iii
Raw data of all AAQ measured for 12 weeks of
all stations as per frequency given in the
NAQQM Notification of Nov. 2009 along with -
min., max., average and 98% values for each
of the AAQ Parameters from data of all AAQ
Stations should be provided as an annexure to
the EIA Report.
12 weeks Raw data of 8 AAQ
locations as per NAAQM standard is
Attached as Annexure IV. The
summarized values including max.,
min. and 98th percentile is given in
table 3.10
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, WB
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iv
Surface water quality of nearby River (60 m
upstream and downstream) and other surface
drains at eight location as per CPCB/ MoEF&
CC guidelines.
CH 3
8 locations were identified in the
buffer area including 2 loactions in
60m upstream and downstream of
Kangsabati river as per CPCB
guidelines. The locations are U/s &
D/s of River Kangsabati, Dauka
pond, Rampura Pond, Bagberia
pond, Banspukuria Pond, &
Kalighai river. The details are Given
in Table 3.12B from page no 109-
110 in ch - 3.
v
Whether the site falls near to polluted stretch
of river identified by the CPCB/MoEF & CC.If
yes give details
CH 3
No, The site does not fall near to
any polluted stretch of river
identified by CPCB / MoEF & CC.
vi Ground water monitoring at minimum at 8
locations shall be included CH 3
Eight locations in Daharpur,
Nutandih, Silti, Keshuriya,
Bargopal, Belti, Shalkha, Mirjapur
were identified and the montoring
results are Given in Table 3.12 A
from page no 104 in ch - 3.
vii Noise levels monitoring at minimum at 8
locations within the study area. CH 3
8 Noise monitoring locations were
identified within 3 km radius from
the project site. The monitoring
values were found to be within
limits and the details are Given in
para 3.5.8 in table 3.14 page no
121 in Ch - 3.
viii Soil characteristic as per CPCB guidelines. CH 3
Soil characteristics were monitored
as per CPCB guidelines in 8
locations within the buffer area.
Given in para 3.5.7 in table 3.13
page no 116 in Ch - 3.
ix
Traffic study of the area ,type of vehicles,
frequency of vehicles for transportation of
materials, additional traffic due to proposed
project , parking arrangement etc
CH 3
Traffic study including the type of
vehicles and their frequency was
carried out in NH 16 location for 4
days. The proposed project will
impose additionl 2500 PCU/hr on
existing road. The existing road can
withstand the additional load
without traffic congestion. The
details are given in para 3.6 in
page no 121-124 in Ch - 3.
x
Detailed description of flora and fauna
(terrestrial and aquatic) existing in the study
area shall be given with special reference to
rare, endemic and endangered species. If
Schedule-1 fauna are found within the study
area, a Wildlife Conservation plan shall be
prepared and furnished.
CH 3
The detailed description of flora &
Fauna with all the rare, endemic
and endangered species is attached
as Annexure V
As per the study report no
Schedule -1 fauna was found within
the study area.
xi Socio-economic status of the study area. CH 3
Given in para 3.8 in Ch - 3.
Detailed SIA study is attached as
annexure VI
7 Impact Assessment and environment Management Plan
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i
Assessment of ground level concentration of
pollutants from the stack emission based on
site-specific meteorological features. In case
the project is located on a hilly terrain, the
AQIP Modelling shall be done using inputs of
the specific terrain characteristics for
determining the potential impacts of the
project on the AAQ. Cumulative impact of all
sources of emissions (including
transportation) on the AAQ of the area shall
be well assessed. Details of the model used
and the input data used for modelling shall
also be provided. The air quality contours
shall be plotted on a location map showing the
location of project site, habitation nearby,
sensitive receptors, if any.
CH 4
AAQ modeling & Traffic modeling
has been carried out using the site
specific Micro Meterological data
and the predicted GLC due to the
same is stated under para 4.3.3
from page no 151-153 & 155-158.
in ch - 4
ii
Water quality modelling - in case , if the
effluent is proposed to be discharged in to the
local drain, then water quality Modeling study
should be conducted for the drain water
taking into consideration the upstream and
downstream quality of water of the drain.
CH 4
Waste water generated from
process shall be treated in the
proposed ETP & STP and will be
reused in the process. No Effluent
will be discharged to local drains or
outside the plant premises. SO,
water quality modeling is not
envisaged .The detail is given in
Page 154
iii
Impact of the transport of the raw materials
and end products on the surrounding
environment shall be assessed and provided.
In this regard, Options for transport of raw
materials and finished products and wastes
(large quantities) by rail or rail-cum road
transport or conveyor-cum-rail transport shall
be examined.
CH 4
The impact of the transportation of
raw materials and products has
been assessed through Traffic
modeillng for present & proposed
scenario. EURO IV/V vehicles
conforming to emission norms will
be used for transportation. The
details are provided in chapter - 4
in page no 155-159 & 163-165.
iv
A note on treatment of waste water from
different plant operations, extent recycled and
reused for different purpose shall be included.
Complete scheme of effluent treatment.
Characteristics of untreated and treated
effluent to meet the prescribed standards of
discharge under E (p) Rules.
CH 4
The details of waste water
management & disposal is covered
under para 4.4.2 & page 172-174.
Schematic Diagram of ETP & STP
has also been provided. No effluent
will be discharged outside. Waste
water will be recycled and reused in
process.
v Details of stack emission and action plan for
control of emission to meet standards. CH 4
The stack emissions are given in
table 4.5 which are used as model
input for deriving the isopleth using
ISCST 3 MODEL . Necessary
pollution control equipment has
been provided in the same table.
vi Measures for fugitive emission control CH 4
Primary & Secondary Fugitive
emission source & control
measures is given in para 4.9 page
no 146-147 ch - 4.3.3
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vii
Details of hazardous waste generation and
their storage, utilization and disposal. Copies
of MOU regarding utilization of solid and
hazardous wastes shall also be included. EMP
shall include the concept of waste-
minimization, recycle/reuse/recover
techniques, Energy conservation, and natural
resource conservation.
CH 4
Hazardous waste are used oil,
cotton easte, empty barrels and oil
filters. Hazardous wastes shall be
given to authorized recyclers. Solid
wastes inventory with their
generation, storage & management
practices is given under para 4.3.3
at page no 166. MoUs for Fly ash,
Bottom Ash and DRI fly ash are
attached as Annexure VII
viii
Proper utilization of fly ash shall be ensured as
per Fly Ash Notification, 2009. A detailed plan
of action shall be provided.
CH 4
Fly Ash generation, storage &
management practices is given
under para 4.3.3 at page no 167.
MoUs for Fly ash, Bottom Ash are
attached as Annexure VII
ix
Action plan for the green belt development
plan in 33% area i.e land with not less than
1,500 trees per ha. Giving details of species,
width of plantation, planning schedule etc.
shall be included. The green belt shall be
around the project boundary and a scheme for
greening of the roads used for the project
shall also be incorporated.
CH 4
11,216 nos. of trees have already
been planted in about 56.0 ha of
land which is about 34 % of the
total area. The detail plan is given
in para 4.8 Pg 177-178
x
Action plan for rainwater harvesting measures
at plant site shall be submitted to harvest
rainwater from the roof tops and storm water
drains to recharge the ground water and also
to use for the various activities at the project
site to conserve fresh water and reduce the
water requirement from other sources.
CH 4
It ha been estimated that about
3,81,102 m3 of water can be
harvested and used in plant. The
details is provided under para 4.5
from page no 175-176
xi
Total capital cost and recurring cost/annum
for environmental pollution control measures
shall be included.
CH 6
The budgetary provisions for EMP is
155.1 cr with recurring cost of
18.33 cr. The details is given in
table 6.2 with SEGREGATED OPEX
& CAPEX. Page 188
xii Action plan for post-project environmental
monitoring shall be submitted. CH 6
The detail action plan along with
monitoring schedule & frequency is
illustrated in table 6.1 from page
187.
xiii
Onsite and offsite Disaster (natural and Man-
made) Preparedness and Emergency
Management plan including risk Assessment
and damage control. Disaster management
plan should be linked with district Disaster
Management plan.
CH 7
The onsite & Offsite disaster
management plan & Emergency
plan is given in section 7.6 with the
hirachy of commands & emergency
command structures covered
between 197-204
8 Occupational health
i
Details of existing occupational & safety
hazards. What are the exposure levels of
hazards and whether they are within
permissible exposure level (PEL). If these are
not within PEL, what measures the company
has adopted to keep them within PEL so that
the workers can be preserved.
CH 7
The details of identification
Occupational Health Hazards &
respective mitigation measures
with PPE is been detailed in 7.12.1
from page no 207-209
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ii
Details of exposure specific health status
evaluation of worker. If the workers health is
being evaluated by pre designed format, chest
x-rays, audiometry, vision testing (far & near
vision, color vision and any other ocular
defect) ECG, during pre placement and
periodical examinations give the details of the
same. Details regarding last month analyzed
data of above mentioned parameters as per
age,sex duration of exposure and department
wise.
CH 7
From the periodic monitoring and
annual health check up of the
employee base of M/s BEL Ltd, no
trend of disease vectors were
identified correlating to the type of
job, or period of job for individuals.
Therefore, it may be inferred that
the temporary ailments if identified
within the employee are not related
to working conditions.
iii
Annual report of health status of workers with
special reference to occupational health and
safety
Health checkup has been carried
out & Analysis has been done for
TC, DC, ESR, HB, FBS, LFT, KFT,
Urine Analysis, CXR,PFT,& ECG.
Attached as Annexure VIII
iv
Plan and fund allocation to ensure the
occupational health & safety of all contract
and casual workers
CH 6
1.5sr has been allocated for
Occupational Health and Safety.
The detail cost is given in Pg 212
9 Corporate Environment Policy
i
Does the company have a well laid down
environment policy approved by its Board of
directors? If so, it may be detailed in the EIA
report
CH 7
The environment policy including
safety measures and standard
operating procedures is exhibited in
page no 234-236. ii
Does the environment policy prescribe for
standard operating process/ procedures to
bring into focus any infringement / deviation /
violation of the environmental or forest
norms/conditions? If so, it may be detailed in
the EIA
iii
What is the hierarchical system or
administrative order of the company to deal
with the environmental issues and for
ensuring compliances with the environmental
clearance conditions? Details of the system
may be given
CH 7
The hierarchy for administrative
control and reporting system is
given in page no 236-238
iv
Does the company have system of reporting
of non compliances/ violations of
environmental norms to the board of directors
of the company and / or shareholders or
stakeholders at large? This reporting
mechanism shall be detailed in the EIA report.
CH 7
The company has a system for
reporting of Non compliances &
their remedies to head of the
Organization and stake holders.
239-240
10
Details regarding infrastructure facilities such
as sanitation, fuel, restroom etc. to be
provided to the labour force during
construction as well as to the casual workers
including truck drivers during operation.
CH 4
During construction period the
existing infrastructural facilities will
be extended to labor force. The
details with respect to sanitation &
Hygine is detailed under para 4.3.1
at page no 143
11 Enterprise Social Commitment(ESC)
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i
Adequate funds(at least 2.5% of the project
cost) shall be earmarked towards the
Enterprise Social Commitment based on public
Hearing Issues and item-wise details along
with time bound action plan shall be included.
Socio- economic development activities need
to be elaborated upon.
CH 7
As per the issues raised during PH
and the gas analysed in SIA study
the company will spend 18.10 crore
under CER activities. The details of
distribution of budget is given
under para 7.8 page 225-226.
12
Any litigation pending against the project and/
or any direction/ order passed by any Court of
law against the project, If so, details thereof
shall also be included. Has the unit received
any notice under the section 5 of environment
(protection) Act, 1986 or relevant Section of
Air and water Acts? If so, Details thereof and
compliance/ ATR to the notice(s) and present
status of the case.
CH 1 There is no litigation pending
against the company. Page 20
ADDITIONAL TORS FOR INTEGRATED STEEL PLANT
1
Iron ore/coal linkage documents along with
the status of environmental clearance of iron
ore and coal mines
CH 2
M/s BEL obtains Coal from
Singapore either through Vizag port
and Iron Ore from Barbil. The
linkage document is attached as
Annexure IX
2
Quantum of production of coal and iron ore
from coal and iron ore mines and the projects
they cater to. Mode of transportation to the
plant and its impact
The major raw Materials are Iron
Ore, Coal, Pig Iron The details of
their procurement, their source and
mode of transportation is explained
in Para 2.6.3 in chapter - 2 page
no 56 & 58
3
For Large ISPs,a 3D view i.e DEM (Digital
Elevation Model) for the area in10 km radius
from the proposal site. MRL details of project
site and RL of nearby source of water shall be
indicated.
CH 3
The DEM map depicts high
elevation 61.1 m in NW region. The
DEM is given in Fig 3.6, CH 3
4
Recent land-use map based on satellite
imagery. High-resolution satellite image data
having 1m-5m spatial resolution like
quickbird, ikonos, IRS P-6 pan sharpened
etc.for the 10 km radius area from proposed
site. The same shall be used for land
used/land cover mapping of the area.
CH 3
High resolution multi spectral
satellite Image namely LISS III has
been considered for preparation of
Land use map of the total which is
provided in fig 3.4 & page 77-78.
5
PM(PM10 AND PM2.5) present in the ambient
air must be analyzed for source analysis
natural dust/RSPM generated from plant
operations (trace elements) of PM10 to be
carried over.
CH 4
The elemental analysis of PM10 &
PM 2.5 has been carried out and
the result is illustrated in Table
3.10A from page no 94
6
All stock piles will have to be on top of a
stable liner to avoid leaching of materials to
ground water .
CH 2
Stock piles will be stored on
impervious layer under covered
sheds.
7
Plan for implementation of the
recommendation made for steel plants in the
CREP guidelines.
CH 6
The CREP guideline compliance has
been given in page 188-189 in
table 6.3.
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8 Plan for slag utilization. CH 4
Blast furnace slag will be handed
over to ASO Cement. as per their
agreement. EAF & IF slag will be
used for construction after iron
recovery. Details is given under
para 4.3 at page no 166.
9 Plan for utilization of energy in off gases (coke
oven ,blast furnace). CH 2
90 MW power will be generated
from DRI & MBF gas and A part of
the gas after cleaning will be used
in MBF tuyeres to heat blast air. 80
MW will be generated from Coke
Oven
10 System of coke quenching adopted with
justification. CH 2
Dry Quenching will be adopted for
the proposed project. Details given
in Pg 34
11 Trace metals Mercury, Arsenic and Fluoride
emissions in the raw material. CH 2
Under para 2.6.3 the chemical
analysis of coal is given in page no
57.
12 Trace metals in waste material especially slag. CH 2
The occurrence of trace metals with
their form in BF slag is illustrated
under para 2.6.6 at page no 65.
13 Trace metals in water CH 3 The trace metal in Kangsabati River
water is given in Pg 103
14 Details of proposed layout clearly demarcating
various units CH 2
Lay out map showing existing unit
in blue color & proposed units in
pink color with all the facilities is
given in Fig - 2.5 of ch - 2. page 55
15
Complete process flow diagram describing
each unit, its process and operations along
with material balance CH 2
Process description along with
major equipments and machineries,
process flow sheet (quantitative)
from raw material to products has
been given in para 2.5.2 of
Chapter - 2 page31-46 16
Details on design and manufacturing for all
the units
17
Details on environmentally sound technologies
for recycling of Hazardous materials as per
CPCB guidelines may be mentioned in case of
handling scrap and other recycled materials.
CH 4
Hazardous waste are used oil,
cotton easte, empty barrels and oil
filters. Hazardous wastes shall be
given to authorized recyclers.
Details given under para 4.3.3 at
page no 166.
18 Details on requirement of energy and water
along with its source and authorization. CH 2
13,165 m3/day of fresh water will
be drawn from Kangsabat river.
153 MW of power will be required.
Total manpower requirement is
1355 both regular & contract
Permission letter with water
balance diagram is given in para
2.6.4 to 2.6.5 page no 59-62. The
permission letters are annexed as
Annexure III.
19 Details on toxic metal content in waste
material and its composition and end use. CH 2
The occurrence of trace metals with
their form in BF slag is illustrated
under para 2.6.6 at page no 65. 20 Details on toxic content (TCLP), composition
and end use of slag
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TABLE OF CONTENTS
EXECUTIVE SUMMARY ........................................................................................ 7
CHAPTER-1 ....................................................................................................... 16
INTRODUCTION................................................................................................ 16
1.0 GENERAL ................................................................................................ 16
1.1 PURPOSE OF THE REPORT ......................................................................... 16
1.2 IDENTIFICATION OF THE PROJECT & PROJECT PROPONENT: .......................... 17
1.3 BRIEF DESCRIPTION OF NATURE, SIZE, LOCATION OF THE PROJECT AND ITS
IMPORTANCE TO THE COUNTRY, REGION ............................................................. 18
1.3.1 NATURE & SIZE OF PROJECT ............................................................. 18
1.3.2 LOCATION OF THE PROJECT SITE: ..................................................... 18
1.3.3 IMPORTANCE OF THE PROJECT TO THE COUNTRY AND REGION ............... 18
1.3.4 NATIONAL STEEL POLICY: ................................................................... 19
1.3.5 GLOBAL STEEL SCENARIO ................................................................... 19
1.3.6 DOMESTIC SCENARIO: ........................................................................ 19
1.4 LITIGATION/COURT CASE AGAINST THE COMPANY .................................... 20
1.5 SCOPE OF THE PRESENT STUDY DETAILS OF REGULATORY SCOPING CARRIED
OUT (AS PER TERMS OF REFERENCE) .................................................................. 20
1.6 AUTHORIZATION ..................................................................................... 21
1.7 ACKNOWLEDGEMENT: .............................................................................. 21
CONCLUSION: ................................................................................................. 21
CHAPTER-2 ....................................................................................................... 23
PROJECT DESCRIPTION .................................................................................... 23
2.0 CONDENSED DESCRIPTION OF THOSE ASPECTS OF THE PROJECT LIKELY TO
CAUSE ENVIRONMENTAL EFFECTS. ..................................................................... 23
2.1 TYPE OF PROJECT ..................................................................................... 23
2.2 NEED OF THE PROJECT .............................................................................. 23
2.3 LOCATION OF THE PROJECT(MAPS SHOWING GENERAL LOCATION, SPECIFIC LOCATION,
PROJECT BOUNDARY & PROJECT SITE LAYOUT) ................................................................ 24
2.3.1 GENERAL LOCATION ................................................................................. 24
2.3.2 SPECIFIC LOCATION ................................................................................. 25
2.3.3 PROJECT BOUNDARY & PROJECT SITE LAYOUT ............................................. 27
2.4 SIZE OR MAGNITUDE OF OPERATION (INCLUDING ASSOCIATED ACTIVITIES
REQUIRED BY OR FOR THE PROJECT) .................................................................. 27
Project configuration & product mix ................................................................. 27 Table 2.2 Project Configuration Before And After Expansion ........................................ 28
2.5 TECHNOLOGY AND PROCESS DESCRIPTION: ............................................. 28
2.5.1 TECHNOLOGY .......................................................................................... 28
2.5.2 PROCESS DESCRIPTION ........................................................................ 29
DRY QUENCHING FLOW SHEET ........................................................................... 32 Fig 2.1 Process & material flow sheet of M/s BEL .......... Error! Bookmark not defined.
2.5.3 MATERIAL BALANCE: ...................................................................... 46 Table 2.4 Sources and type of Pollution from the Proposed Project & mitigation measure .. 48
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2.6 PROJECT DESCRIPTION, INCLUDING DRAWINGS SHOWING PROJECT LAYOUT,
COMPONENTS OF PROJECT ETC. SCHEMATIC REPRESENTATIONS OF THE FEASIBILITY
DRAWINGS WHICH GIVES INFORMATION IMPORTANT FOR EIA PURPOSE. ................ 49
2.6.1 LAND DETAILS ..................................................................................... 49 Table 2.1 Land schedule of project site core zone ...................................................... 49 Table 2.1A Land utilisation of project site core zone ................................................... 49
2.6.2 PROJECT LAYOUT ............................................................................... 50 Table 2.3 Water Requirement .................................................................................... 54 Fig 2.2 Water Balance Diagram ................................................................................ 55 Table 2.4 Solid Waste Generation ........................................................................... 59 Table 2.5 Summary Of Manpower Requirement ......................................................... 60 Table 2.6 Category-wise break-down of manpower ...................................................... 61 Table 2.7 Total capital cost of Project ......................................................................... 61
2.7 DESCRIPTION OF MITIGATION MEASURES INCORPORATED INTO THE PROJECT TO
MEET ENVIRONMENTAL STANDARDS, ENVIRONMENTAL OPERATING CONDITIONS OR
OTHER EIA REQUIREMENTS (AS PER REQUIRED SCOPE) ........................................ 63
2.8 ASSESSMENT OF NEW & UNTESTED TECHNOLOGY FOR THE RISK OF
TECHNOLOGICAL FAILURE. ................................................................................ 64
CONCLUSION ................................................................................................... 64
CHAPTER-3 ....................................................................................................... 65
DESCRIPTION OF EXISTING ENVIRONMENT .................................................... 65
3.0 INTRODUCTION ....................................................................................... 65
3.1 STUDY AREA, PERIOD & COMPONENTS ........................................................ 65
3.1.1 STUDY AREA ...................................................................................... 65
3.1.2 STUDY PERIOD................................................................................... 65
3.1.3 COMPONENTS .................................................................................... 66
SITE CONNECTIVITY ...................................................................................... 66 Fig 3.1 Location of Site ............................................................................................. 66
3.2 PHOTOGRAPHS OF PROJECT SITE ............................................................... 67
3.3 TOPOGRAPHY .......................................................................................... 67
3.3.1 LAND USE PATTERN OF BUFFER ZONE ...................................................... 67 Fig 3.4 Landuse & Land Cover MapLAND USE PATTERN OF 10KM BUFFER ZONE OF
PROJECT SITE ......................................................................................................... 67 3.4 ESTABLISHMENT OF BASELINE FOR VALUED ENVIRONMENTAL COMPONENTS AS
IDENTIFIED IN THE SCOPE WITH METHODOLOGY ADOPTED. BASE MAP OF ALL
ENVIRONMENTAL COMPONENTS. ........................................................................ 69
3.5 BASELINE STATUS OF STUDY AREA ............................................................ 70 Table-3.2: Temperature Profile of the study area ......................................................... 70 Table-3.3: Maximum and Minimum Humidity of the Study Area ..................................... 70 Table-3.4: Rainfall Pattern in the Region ..................................................................... 71
3.5.2 METEOROLOGICAL CONDITIONS DURING STUDY PERIOD. ...................... 71 Table-3.5: Summarized Meteorological Data at site. ..................................................... 72 Table-No. 3.6: Overall Wind Frequency Distribution ..................................................... 72
3.5.3 AMBIENT AIR QUALITY ..................................................................... 74 Table 3.7 Monitored parameters and frequency of sampling .......................................... 74 Table 3.8 Techniques used for ambient air quality analysis ........................................ 75 Table-3.9: National Ambient Air Quality Standards as per MoEF Notification under
Schedule-VII, Rule- 3(3B). dt 18.11.09 ...................................................................... 75 Table- 3.10 A: Details of Ambient Air Quality Monitoring Locations ............................. 76 Table 3.10 B Summary of Ambient Air Quality Result .................................................. 77 Table 3.10A: Chemical characterization of RSPM (PM10) ............................................. 80
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MIXING HEIGHT ............................................................................................ 81
ToR-4(ix) Geological features and Geo-Hydrological status of the Study Area shall
Be Included 83
3.5.4 GEOLOGY OF THE STUDY AREA ......................................................... 83 Fig 3.13 Map Showing the geological features of the study area ........................................
3.5.5 GEOMORPHOLOGYOF THE STUDY AREA .............................................. 83 Fig 3.14Geomorphological Map of the area ......................................................................
3.5.6 WATER ENVIRONMENT: ....................................................................... 84 Fig 3.15 Ground water Prospect Map of the area ........................................................... Fig 3.16 Drainage Map of the study area ..................................................................... Table- 3.12: Surface and Groundwater Sampling Locations ......................................... 85 Table 3.12 A Ground Water analysis result .................................................................. 87 Table 3.12 B Surface Water analysis result ................................................................. 91
3.5.7 SOIL CHARACTERISTICS ..................................................................... 95 Fig 3.17 Soil Map of The area ..................................................................................... Table- 3.13: Details of Soil Quality Monitoring Locations ............................................... 96 Table 3.13 A Soil Analysis Results .............................................................................. 98
3.5.8 NOISE ENVIRONMENT: ...................................................................... 100
DISCUSSION ..................................................................................................... 103
THE NOISE READING TAKEN WERE WITHIN THE LIMITS AS THERE IS NO SUCH NOISE GENERATING
SOURCE EXCEPT VEHICULAR MOVEMENT. DURING FESIVALS THE NOISE LEVEL INCREASES. ........... 103
3.6 TRAFFIC STUDIES: ................................................................................. 103
3.7 ECOLOGICAL ENVIRONMENT OF THE 10KM. RADIUS OF THE STUDY AREA: .... 106
3.7.1 Ecological Overview .......................................................................... 106
3.7.2 Objective: ....................................................................................... 107
3.7.3 Floral Characteristics ......................................................................... 108
Plankton Analysis ........................................................................................ 108 Table 3.16 Quantitative Assessment of Natural Plant species & Calculation of Biodiversity
Index of Natural Plant Species in the study area ......................................................... 111 3.8 SOCIO-ECONOMIC ENVIRONMENT ........................................................... 113
3.8.1 OBJECTIVE: ..................................................................................... 113
3.8.2 DEMOGRAPHIC PATTERN ................................................................... 114
3.8.6 GAP ANALYSIS ................................................................................. 114
3.9 CONCLUSION: .......................................................................................... 115
CHAPTER-4 ..................................................................................................... 116
ANTICIPATED ENVIRONMENTAL IMPACT & MITIGATION MEASURE ............... 116
4.1 DETAILS OF INVESTIGATED ENVIRONMENTAL IMPACTS DUE TO PROJECT
LOCATION, POSSIBLE ACCIDENTS, DESIGN, CONSTRUCTION, OPERATION,
DECOMMISSIONING OR REHABILITATION OF A COMPLETED PROJECT .................. 116
4.1.1 Objectives of Impact Prediction .......................................................... 116
4.1.2 Impact Prediction & Assessment ......................................................... 117
4.1.3 Pollution Potential ............................................................................. 117
4.2 METHODS USED FOR THE STUDY OF ENVIRONMENTAL IMPACTS .................. 117 Table 4.1: Parameter Impact Value of Environment Components ............................... 120 Table 4.2 Impact Identification Matrix for M/s Bengal Energy Ltd............................. 121
4.3 IMPACT PREDICTION & MEASURES FOR MINIMISING AND/OR OFFSETTING
ADVERSE IMPACT IDENTIFIED. ........................................................................ 123
4.3.1 IMPACTS DURING CONSTRUCTION PHASE: ......................................... 123 Table 4.4: Action Plan for Excavation and Muck Disposal during Construction .............. 126
4.3.3 IMPACTS DURING OPERATIONAL PHASE ............................................ 127
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Table 4.5: Details of predicted stack emission from proposed expansion Project ........... 130 Table 4.6 Assessment of GLC of pollutants without APC equipments .............................. 133 Isopleth of NOx ........................................................................................................... Table 4.7 The GLC values after implementation of APC systems are ............................ 137 Table 4.3 Solid Wastes utilization & disposal measures ............................................... 138 Table 4.9 Hazardous Waste Management ................................................................... 139
4.4 EMP AT DESIGN STAGE ........................................................................... 139
4.4.1 ENVIRONMENTAL MANAGEMENT PLANT (EMP) AT CONSTRUCTION STAGE:
140
4.4.2 ENVIRONMENTAL MANAGEMENT PLANT (EMP) AT OPERATIONAL PHASE . 141 E S Ps ................................................................................................................... 141
4.5 RAIN WATER HARVESTING ...................................................................... 147
4.6 MAINTENANCE OF POLLUTION CONTROL EQUIPMENTS: .............................. 148
4.8 GREEN BELT DEVELOPMENT .................................................................... 149
4.9 SOCIO-ECONOMIC DEVELOPMENT............................................................ 150
4.10 IRREVERSIBLE AND IRRETRIEVABLE COMMITMENTS OF ENVIRONMENTAL
COMPONENTS ................................................................................................ 151
4.11 ASSESSMENT OF SIGNIFICANCE OF IMPACTS (CRITERIA FOR DETERMINING
SIGNIFICANCE, ASSIGNING SIGNIFICANCE) ...................................................... 152
CONCLUSION ................................................................................................. 154
CHAPTER-5 ..................................................................................................... 155
ANALYSIS OF ALTERNATIVES (TECHNOLOGY & SITE) .................................... 155
CONCLUSION ................................................................................................. 155
CHAPTER-6 ..................................................................................................... 156
ENVIRONMENTAL MONITORING PROGRAMME ............................................... 156
6.1 TECHNICAL ASPECTS OF MONITORING THE EFFECTIVENESS OF MITIGATION
MEASURES .................................................................................................... 156
6.2 ADVANTAGES OF MONITORING ................................................................. 156
6.3 SAMPLING LOCATIONS ........................................................................ 157
6.4 DATA ANALYSIS ..................................................................................... 158
6.5 REPORTING SCHEDULE .......................................................................... 158 Table 6.1 Monitoring Schedule ................................................................................. 159
6.6 BUDGETORY PROVISIONS FOR EMP .......................................................... 161 Table 6.3 Investment towards EMP, Implementation & its yearly maintenance ............ 161 Table 6.4 CREP Compliance ...................................................................................... 161
CONCLUSION ................................................................................................. 163
CHAPTER-7 ..................................................................................................... 164
ADDITIONAL STUDIES ................................................................................... 164
7.1 RISK ASSESSMENT & DISASTER MANAGEMENT: ...................................... 164
7.2 OBJECTIVES ....................................................................................... 164
7.3 DEFINITION OF ENVIRONMENTAL RISK .................................................. 165
7.4 IDENTIFICATION OF HAZARDS .............................................................. 165 Gen. ToR 3(x) Hazard Identification and details of proposed safety measures................. 165 Table 7.1 Hazard Identification of the Proposed Steel Plant .......................................... 166
7.5 ENVIRONMENTAL RISK EVALUATION...................................................... 169 Table 7.2 – Determination of Risk Potential ................................................................ 169
7.6 DISASTER MANAGEMENT PLAN ................................................................ 170
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Table 7.3 Manpower to be in position ........................................................................ 170 7.7 ROLE OF KEY PERSONS ........................................................................... 172
7.7.1 WORKS MAIN CONTROLLER: .............................................................. 172
7.7.2 SITE INCIDENT CONTROLLER: ........................................................... 173
7.7.3 COMBAT TEAM LEADER .................................................................... 173
7.7.4 RESCUE TEAM LEADER ..................................................................... 173
7.7.5 AUXILIARY TEAM LEADER ................................................................. 174 Table 7.4 ACTION PLAN FOR ON-SITE EMERGENCY ............................................... 174
7.8 SILENT HOUR COMMAND STRUCTURE ...................................................... 175
7.9 ACTIVATION & CLOSING PROCEDURE FOR ON-SITE EMERGENCY.................. 176
7.9.1 ACTIVATION PROCEDURE .................................................................. 176
7.9.2 FACILITIES AVAILABLE FOR ON-SITE EMERGENCY PLAN: ...................... 177
7.10 FACILITIES AVAILABLE ........................................................................ 177
7.11 OBJECTIVE OF ONSITE EMERGENCY PLAN ............................................... 178
7.12 OCCUPATIONAL HEALTH ...................................................................... 179
7.12.1 Occupational Health Hazard ........................................................... 179
7.12.2 EXPOSURE LIMITS ........................................................................ 181
7.12.3 FIRST AID MEASURES ................................................................... 182
7.12.4 EXPOSURE CONTROLS AND PERSONAL PROTECTION ......................... 183 Table 7.5 Health Hazard in Major Shops: ................................................................. 184
7.8 PUBLIC HEARING ................................................................................... 187
7.8 CORPORATE ENVIRONMENT RESPONSIBILITY ............................................ 198
CONCLUSION ................................................................................................. 199
CHAPTER-8 ..................................................................................................... 200
PROJECT BENEFIT .......................................................................................... 200
8.1 PROJECT BENEFIT .................................................................................... 200
8.2 INFRASTRUCTURE DEVELOPMENT .............................................................. 200
8.3 EMPLOYMENT POTENTIAL ........................................................................ 201
8.4 REVENUE GENERATION TO CENTRAL & STATE GOVERNMENT ....................... 202
CHAPTER-9 ..................................................................................................... 203
ENVIRONMENT COST BENEFIT ANALYSIS ...................................................... 203
CONCLUSION ................................................................................................. 203
CHAPTER-10 ................................................................................................... 204
ENVIRONMENTAL MANAGEMENT PLAN (ADMINISTARATIVE)
....................................................................................................................... 204
10.1 EMP IMPLEMENTATION AND MONITORING .............................................. 204
10.2 METEOROLOGY ................................................................................... 204
10.3 EMISSIONS AND AIR QUALITY............................................................... 204
10.4 DRAINAGE SYSTEM ............................................................................. 204
10.5 WATER QUALITY .................................................................................. 205
10.6 NOISE LEVEL ...................................................................................... 205
10.7 OCCUPATIONAL HEALTH ...................................................................... 205
10.8 LABORATORY FACILITIES ..................................................................... 205
10.9 UPDATING OF EMP ............................................................................... 205
10.10 ORGANISATION AND MANPOWER ....................................................... 205
10.11 FUNCTIONS OF EMP CELL ....................................................................... 210
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CHAPTER-11 ................................................................................................... 213
SUMMARY & CONCLUSION ............................................................................. 213
CHAPTER -12 .................................................................................................. 222
CONSULTANT PROFILE ................................................................................... 222
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EXECUTIVE SUMMARY
ToR 1 Executive Summary
i) Project name and location
Proposed Expansion project of M/s. BEL is located over 161.87 ha of land at village-Dauka, PO-
Tentulmuri, PS- Narayangarh, Dist-Paschim Medinipur, West Bengal, which extends from 220
15’ 22.96’’ N to 220 15’ 27.68’’ N and 870 22’ 53.37’’ E to 870 23’ 34.69’’ N with, with 32
AMSL appearing on Toposheet No-73M/6 (F45J6). The proposed expansion is confined over the
same land of 161.87 ha.
ii) Products & Capacities (existing & proposed)
M/s. BEL, was granted EC vide J-11011/28/2008-IA II (I), 2nd January, 2009for 0.5 MTPA
Integrated steel in MBF,DRI, EAF & CCM route; 1.2 MTPACoke Oven & 140 MW CPP which
included both WHRB & FBC. But the unit could install 0.6 MTPA Coke Oven & 40 MW CPP and
has now applied and granted ToR for 1.0 MTPA integrated steel, 1.2 MTPA Non-Recovery Coke
OVEN & 205 mw POWER Plant. The configuration & capacities are as given in table below.
Facility Existing Configuration
Existing capacity in TPA
Proposed configuration
Proposed capacity in TPA
Final capacity
Product End use
Non.Recovery CO Plant
1x0.6 MTPA 6,00,000 1x0.6 MTPA 6,00,000 12,00,000 Lam Coke MBF
CPP(Coke Oven gas) 1x40 MW 40 MW 1x40 MW 40 MW 80 MW Elec. Power Internal use/Sale
DRI Kiln - Nil 4x500 TPD
6,40,000 4,48,000
10,88,000 Sponge Iron EAF & IF
4x350 TPD
CPP (DRI) - Nil 68 MW 68 MW Elec. Power Internal use/Sale
MBF,2.7T/m3day - Nil 2x320m3 5,96,000 5,96,000 Hot Metal EAF & IF
Sinter Plant 1x60m2 2T/m2.hr, 340days
- Nil 1x60m2 10,00,000 10,00,000 Sinter MBF
EAF with LF, 16H/day, 325days
- Nil 2x80T 8,32,000 8,32,000 Liq. Steel LF
LF - Nil 1x25T Holding Liq. steel CCM
C C M - Nil 2,500 TPD 8,15,000 8,15,000 Steel Billet Sale
IF 15H/day, 325 days
- Nil 3x20T 2,92,500 2,92,500 Liq. Steel CCM
C C M - Nil 1,000 TPD 2,80,000 2,80,000 Steel Billet Sale
CPP (BF gas fired ) - Nil 1x22 MW 22 MW 22 MW Elec. Power Internal use/Sale
AFBC - Nil 1x35 MW 35 MW 35 MW Elec. Power Internal use/Sale
A S U - Nil 120 TPD 1,200 m3/hr 1,200 m3/hr
Oxygen Nitrogen
Use in MBF & EAF
iii) a. Requirement of land
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The project area is located at Vill-Dauka, Po-Tentulmuri, PS-Narayangarh in Paschim Medinipur district of
West Bengal. The company has in its possession 161.87 ha of land. The proposed expansion will be
accommodated in available vacant area of this land. This is an industrial barren land.
b. Requirement of Raw material with source of supply.
Major Raw material inventory for project after modification cum expansion with source and mode of
transportation is estimated and given below.
Material Gross Capacity in TPA Source Mode of Transport
Coking Coal 16,80,000 Imported Ship/Rail/Road
Non-Coking Coal 17,96,780 Talcher Rail
Iron Ore 19,98,800 Barbil, Banspani Rail
Iron Ore fines 7,68,000 Barbil, Banspani Rail
Dolomite 1,36,000 Biramitrapur Rail/Road
Lime stone 1,39,000 Biramitrapur Rail/Road
Other chemicals required for the proposed project is
Sl No Item Description Unit Quantity Per Annum
1 DM plant resins KG 342
2 Hydrochloric acid KL 178
3 Caustic soda KG 287
4 Lubricants KG 3,112
5 Lubricants LTR 10,015
c. Requirement of water
The total water requirement after the expansion project will be 13,165 m3/day, which will be sourced
from river Kangsabati. Two intake wells at the river, one at Jinsar 220 23’ 34.42” N and 870 21’ 49.32” E
and other at Uttershimla 220 23’ 19.30” N and 870 23’ 05.03” E has been set up. Transportation of water
from river to project site will cover a pipe length of 23.7km and cross canal, NH-6, Howrah-Kharagpur
Rly. Line and pass along the length of NH-60, and outfall at 220 14’ 45.48” N and 870 23’ 23.08” E.
Permission has already been from Government of west Bengal, SE Rly etc. This water project is to supply
10 MGD i.e. 40,920 m3/day and part of job has already been completed.
d. Requirement of Power
Power requirement after expansion will be 153 MW. Own Captive Power generation will be 205 MW.
After usage balance power of 52 MW will be supplied to State Grid.
e. Requirement of Fuel
16,80,000 TPA Coking Coal, 17,96,780 TPA Non coking Coal will be used as fuel in project.
iv) Process description in brief
Steel production in proposed expansion will be in DRI/MBF-IF/EAF- route. Lump Iron Ore along with
Coal and dolomite will be fed to Kilns for sponge iron production. Similarly, Iron ore agglomerate sinter
will be manufactured in sinter plant and will be fed to MBFs with coke, Oxygen, dolomite & pulverised
coal injection for production of hot metal. Hot metal from MBF & Sponge Iron will be used in IFs and EAFs
for production of liquid steel which will be casted in CCM for production of billets..
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Narayangarh, Dist-Paschim Medinipur, WB
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v) Capital cost of the project, estimated time schedule
The total project cost has been estimated as Rs 4943 crore. This will include pollution control equipments
which will be installed along with process equipments and a CER cost of 18.10 Crore. The plant will be
commissioned and give commercial production in three after obtaining Environmental Clearance.
vi) Site selected for the project
The project is located at Dauka, Tentulmuri, Paschim Medinipur. The expansion has been proposed in the
acquired area on which existing plant is running. It has well developed infrastructure like road network,
railway siding etc. No national park or wildlife sanctuary or eco sensitive zones or places of
archaeological importance are present within 10 km radius around the project and the site does not come
under critical polluted area. Hence alternate site has not been considered.
vii) Baseline Environmental data.
For the preparation of EIA report a monitoring schedule covering winter season of the year was carried
out from 1st Nov 2017 to 31st Jan 2018. The consultant had engaged NABL accreditated laboratory , M/s
Kalyani Laboratories Pvt Ltd for carrying out monitoring under their strict supervision.The impact
identification started with collection of baseline data such as existing ambient air quality, qualities of
ground water, surface water, soil, noise level prevailing in the area and meteorological parameters like
temperature, humidity, wind speed and direction, cloud cover etc.
Land
The general land use/land cover features of the buffer zone include settlements, agricultural land,
vegetation and forest, collieries both in use & disused, wasteland, water bodies, wet land, and industrial
land, infrastructure and others.
Agriculture land of buffer zone is about 66%, followed by 16.5 % rural settlement and about 3.1% dense
forest.
Water
Kangsabati River is of high significance in the region as it caters to the water requirements of most of the
villages and the majority of the industrial units in the region. River is about 20 km away from the project
site. In 1978, the area was affected by flood and there after no flood hazard has been observed since last
40 years. The mean sea level of the river is 26m and the MSL of the plant is 33 m.
Annual avg. Rain fall project area being 1440 mm and project area 20 ha there will be about 3,81,102m3
of rain water harvested per annum and will meet summer supply to plant i.e. lean period of river
Kangsabati.
The analytical results of surface water samples at different location for various parameters reveal that all
the parameters comply with IS: 2296 (Class ‘C’) standards indicating their suitability for drinking and
other purposes after conventional treatment followed by disinfection.
Similarly the analysis results of groundwater samples showed all the parameters are within the
prescribed limits as per IS: 10500 standards for drinking water.
Climate
Climate in the study region is generally dry and hot and is characterized with seasonal variations of temp.,
humidity, rainfall etc.
Summer is from March to June. South West monsoon brings rain to the area from mid June to September.
Post monsoon are October & November. November to February are winter in the area.
The area receives fairly good amount of rainfall from the southwest monsoon during June to September.
Light showers of rain occur during the months of October, November and sometimes in December also
Annual Average rain fall 1440 mm
Meteorological conditions In order to determine the micrometeorological conditions of the study area a temporary micro-
meteorological monitoring observatory was set up near the site from Nov 2017-Jan 2018. The results
were compared with data of IMD station Midnapore. At the site Overall predominant wind direction has
been from North and the North East direction during study period.
The average wind velocity found to be 3.72 m/s and the calm period is 34.83%.
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-
Narayangarh, Dist-Paschim Medinipur, WB
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Ambient air
The study area represents mostly industrial environment. Air quality in the project area is affected by the
presence of polluting industry nearby. The prominent sources of air pollution in the study area are due to
emission from industries, vehicular movement and domestic coal burning as fuel in some parts of the
study area.
During the study period, the concentrations of PM10 measured to vary between 93.6-61.9 g/m3 at
different locations of the study area. The concentrations of PM2.5 varied between 49.8-27.2 g/m3 at
different locations of the study area. During the study period, the average levels of SO2 concentrations at
all location varied from 15.4-6.1 g/m3. The concentrations of NOX values varied between 28.7-10.5
g/m3 at different locations. The concentrations of CO value ranged between 789-342 µg/m3 at different
locations during the study period
Soil analysis
The study area analysis results of the soil parameters show deficiency normal nutrients and micro
nutrients of. The bulk density of the study area ranges from 1.13 to 1.3 gm/cc. The other nutrient content
like nitrogen, potassium and phosphate content of the soil is very low indicating land not suitable for
agriculture purposes. This is to be taken care of in agricultural land as well as growing trees for green
belt.
Flora and Fauna
Flora and Fauna of the study area reveals that no Schedule- I type of fauna found in the study area. In
faunal population; cattle, goats, dogs, rats, insects are common in the study area.
As per IUCN's "Red Data Book", none of the taxa found in this region could be marked as rare or endangered plant species.
Socio Economic
The socioeconomic features around the 10km radius of the plant site have been collected through
primary and secondary data collection. The study area covers 12425 inhabitants. Out of the total
population 53 % are male and 43% are female. SC population is 25%, ST 1.0% and other 74%. 57 % of the
total population is literate.
Priority to be given to local people in employment in proposed expansion project to improve economy of the locality. viii) Identification of Hazard in handling, processing and Storage of material and safety systems
provided.
All the shops will have their own list of hazards, which have been identified and damage to human being
and environment has been discussed with risk management, which can reduce if not mitigated fully. The
major on-site emergency situation may occur from storage and handling, fuel gas, molten metal and slag
handling, acids, alkali storage and handling and electrical short-circuit. Proper safety equipments will be
provided to the workers and proper standard operating procedure will be followed during handling and
processing hazardous material. Hazards in various working area have been identified, its severity has
been estimated and mitigation has been suggested.
Hazard Identification & Risk Analysis for different units has been addressed with identification of most
critical hazard operations.
ix) Likely Impact of the project on air, water, land, flora fauna
Air Environment:
The pollutant emissions from the proposed project will have maximum ground level concentration as
33.48 µg/m3 for PM10, 31.23 µg/m3 for PM2.5, 44.65µg/m3 for NOx and 62.18 µg/m3 for SO2. With
installation of APC systems like bag filters, and ESPs the maximum ground level concentration will come
down to 2.53 µg/m3 for PM10, 1.49 µg/m3 for PM2.5 and 34.11 µg/m3 for SO2.
However there will be occasions when dust venting may be forced due to APC failure although inter
locking provision has been suggested for tripping the unit. Action plan has been suggested to protect
crops of the villagers during such situations. In case of failure of APC immediate action will be taken at
most impact points with water jet mixed system which will be truck mounted.
Water Management
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-
Narayangarh, Dist-Paschim Medinipur, WB
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As the plant water system is designed based on maximum recirculation system. The effluents likely to be
generated from the proposed plant are:
Backwash Waste from Filtration Plant;
Run-off water from Raw Material Storage Yards;
Waste Water from Billet Caster;
Cooling tower blow-down of various shops; and
Plant Sewage & Canteen Effluents.
The effluents will be treated in ETP and will be reused. M/s BEL abides to Zero Discharge Liquid norms
for its existing plant. Rain water harvesting will be done to reduce raw water drawl during lean period of
Damodar.
Noise Pollution Management
The noise level within the plant boundary is occupational noise levels and confined within shops. The
level will be further minimized when the noise reaches the plant boundary and the nearest residential
areas beyond the plant boundary, as elaborate green belt development is envisaged for all along the
boundary for attenuation of noise and fugitive emission. All the equipment in the steel plant will be
designed/operated in such a way that the noise level shall not exceed 85 dB (A) as per the requirement of
Standard.
Solid Waste Management
The comprehensive EMP enlists the management plan for each individual unit.
Solid waste Quantity in
TPA
Utilisation measures
EAF & IF slag 1,20,000 Use in construction work
IF & EAF flue dust 24.000 Will be used in making sinter for use in BF
DRI Dolchar 2,72,000 Use in AFBC to generate steam for power generation
Power plant Fly ash 1,50,750 Supply to Gava Ecocrete Pvt Ltd as per MOU.
DRI ash & dust 5,75,600 Land feel and dump in abandoned coal mines for which
permission to be sought
BF slag 1,84,760 To be used in sinter plant & balance to be Sold to ASO
Cement Ltd as per MOU 20.09.2018
BF sludge + dust 2,93,670 To be used in sinter plant & balance to be Sold to ASO
Cement Ltd as per MOU 29.09.2018
Power plant Bottom Ash 1,00,500 Sold to Gava Ecocrete Pvt Ltd, MOU 30th August, 2018
In case of excess BF slag and sludge over sale, this can be used as raw material for iron ore sinter making.
Measures for Improvement of Ecology:
There is no wildlife sanctuary within the 10 km radius of the proposed plant. The core zone area is devoid
of plantation. There will not be any loss of plantation because of the project. On the other hand, the
company will provide the comprehensive green-belt cover in 33 % of the project area as per the MoEFCC
norms to improve the local ecology. The company plans to acquire the nearby abandoned coal quarries
with deep gorges and holes and will fill the same with the non-hazardous solid waste and will develop
thick green belt cover over the sites. All these steps will considerably improve upon the ecology of the
area.
x) Impact Mitigation Measure
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Narayangarh, Dist-Paschim Medinipur, WB
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Gaseous Emission
a. Hot flue gas with particulate matter, SO2, CO2 and NOx will be generated from DRI kilns, Flue gas
will pass through, DSC, ABC & ESPs for separation of particulate matter and clean gas will be
sucked by ID fans and vented to atmosphere through high stack. Efficiency of ESPs being >99%,
particulate matter emission will come down. In the existing plant 1 no. of ESPs for Cement
rinding units is installed and additional 4 ESPs and 5 Bagfilters will be installed.
b. Fumes generated from Induction Furnace will be cleaned in bag filters and vented to atmosphere
through ID fan and stack. Emission will come down.
c. Sinter plant and FBC will have ESPs to clean gaseous emission which are then sucked by ID fans
and vented to atmosphere.
d. Both DRI Kiln flue gas, Coke Oven gas will have WHRB boiler for removal of heat for generation of
steam for power. Ventury scrubber will be used in MBF to remove particulate matter in the form
of sludge. BF dust and sludge having residual carbon will be used in making sinter.
With this pollution control measure the resultant ground level concentration will come down from
estimated value as follows.
PM10 from 33.48 to 2.53 µg/m3, PM2.5 from 31.23 µg/m3 to 1.49 µg/m3, SO2 from 62.18 to 34.11
µg/m3
Liquid Effluent
a. Industrial waste water from MBFs, DRI kilns and CPP will pass through ETP, where
neutralization and settling will take place. After treatment the turbidity will come down from 60
to <15 NTU, oil & grease from 31 to <5PPM and suspended particle from 1000-5000 to <30 PPM.
b. Domestic waste water will pass through STP having equalization, aeration and settling tank.
Industrial and domestic effluent water after settling tanks will undergo filtration through gravel
& sand bed and will be used for toilet flushing, green belt watering, dust suppression and vehicle
washing.
c. Water quenching will be avoided and dry quenching will be adopted for red hot coke. This will
eliminate waste water generation and treatment from Coke Oven Plant.
Solid and Hazardous Waste
a. Fly ash and bottom ash from CPP will be supplied to Gava Ecocrete Pvt Ltd as per MOU for fly ash
brick manufacturing. Bottom ash , fly ash and kiln accretion from DRI kiln will be used as road
making and land fill material. Possibility of dumping DRI ash & dust in abandoned coal mines to
be explored.
b. BF slag & sludge will be utilized in sinter making and balance will be sold to ASO Cement Ltd as
per MOU. IF slag normally contains about 15% Iron, hence slag will be cooled, crushed and
undergo magnetic separation. Residual iron thus recovered will be recycled to IF for re-melting
and slag which has high silica content and equivalent to river sand will be used as construction
material/land fill.
c. Used oil, DM plant resins and lead batteries like hazardous materials will be handed over to
authorized dealer/suppliers
xi) Hazard Identification & Risk Analysis
It may be observed that the major on-site emergency situation may occur from coal & chemicals storage
and handling; fuel gas handling, molten metal and slag handling, acids and alkali storage and handling and
electrical short-circuit. The off-site environmental disaster may occur if large-scale fire and explosion
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Narayangarh, Dist-Paschim Medinipur, WB
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occurs, the effect of which extends beyond the plant boundary. The off-site environmental disaster may
occur due to significant environmental degradation for a sustained period.
Probable Hazards has been identified through the process of HIRA for major units like ASU, DRI, SMS,
Rolling mill, Sinter & CPP. The respective mitigation majors are also enlisted along with the onsite
emergency Plan. The Environmental management plan includes the environmental Risk mitigation
measures.
BEL has a well-developed Disaster Management Plan consisting of the preparedness plan for onsite and
offsite disasters and the role of key persons during occurrence of any disaster. An emergency cell headed
by Works Main Controller and followed by Site Controller, Combat Leader, Rescue team operates to
prevent any type of disaster. The DMP also states the activation and closing procedure for onsite
emergency along with the responsibilities of each member.
xii) Issues raised during Public Hearing
Public Hearing for proposed expansion from its 0.6 MTPA Non-Recovery Coke Oven and 40 MW Power
Plant to 1.0 MTPA Integrated Steel Plant, 1.2 MTPA Non-Recovery Coke Oven and 205 MW Power Plant at
Dauka, PO- Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, West Bengal by M/s Bengal Energy
Limited was conducted on 15.05.2018, at 12.00 hrs at the project site, WB.
Sl.No Name of Public Issues raised by Public Commitment of P P
1 Sri Sarat Pramanik,
Tentulmuri
Source of water for the plant and
concern on pollution due to
expansion
Water requirement will met from nearby
river for which the company has requisite
permission. Pollution control norms of
statutory authorities will be followed &
proper control measures will be taken for
abatement of pollution. Green belt will be
further strengthened.
2 Sri Subod Dey, Khorigaria
Sri Sukumar Das,
Khorigaria
Concern on pollution due to
expansion, its control so as to
provide a better environment for
local village.
Pollution control norms of statutory
authorities will be followed & proper
control measures will be taken for
abatement of pollution. Green belt will be
further strengthened.
3 Sri Mantu Behari Patra Enquired about development of
the area due to expansion
CSR activities are being carried out
regularly and will also continue on regular
basis.
4 Sri Anil Singh, Banspukuria
Sri Dipak Pal, Tentulmuri
Employment provision for local
people and their safety aspects.
The issue will be addressed.
5 Sri Badal Patra, Tentulmuri Requested the proponent to
assist local people for health
protection and provide food like
gur and channa to the labours.
CSR activities are being carried out
regularly and will also continue on regular
basis.
6 Sri Durgapada Das,
Khorigaria
Sri Dhananjoy Bhuiya,
Khorigaria
Sri Bhadreswar Singh,
Nangunia
Provision of training programs
for skill development to local and
employment opportunities.
CSR activities are being carried out
regularly and will also continue on regular
basis.
7 Sri Sujit Khara,
Malka
Concern about control of
pollution and employment
opportunities for locals.
Pollution control norms of statutory
authorities will be followed & proper
control measures will be taken for
abatement of pollution. Green belt will be
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Narayangarh, Dist-Paschim Medinipur, WB
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further strengthened.
xiii) CER Plan with proposed expenditure
The company will spend 18.10 crores of its project cost on CER activities based on circular . This will be
spent along the construction activities of the project and cover all the issues raised by public during
Public Hearing and as committed by project proponent.
S.N0 Item Description Ist Yr (in lacs)
2nd Yr (in lacs)
3rd Yr (in lacs)
Total (in lacs)
1
Refreshers course to technical
persons, on advanced
industrial training and
practical exposure to
industries, like process, safety,
disaster etc.
Rent Establishment + Training Material +
Stipend+ faculty 60 60 60 180
2
Development of water shed
and renovation of water bodies
in Banspukuria, Tentulmuri
villages
12 Nos of New &
Existing water
bodies @ 4
Nos/Yr. @ Rs
400000
Digging, Paving, de-
siltation & removal
of Aquatic weeds
16 16 16 48
3
Construction of village
community center and its
renovation
3500000/ Village
3 Villages with
community hall,
recreational and
study centers
35 35 35 105
4 Strengthening of approach
roads
Proposing 4 km CC
Approach &
Village Roads
Rs 1200000./Km for
widening &
strengthening
48 48 48 144
5 Adoptation of primary schools
and Anganwadi Centres
3 Schools & 3
Anganwadi
centres
Renovation of the
school building,
construction of
toilets, provide
bench & desk
25 25 25 75
6 Technical and Infrastructural
aid to farmers.
Providing deep irigation points with
electricity, supply of high yield seeds,
fertilizer to poor farmers. The villages will
be decided in consulattion with local
administration.
35 30 65 130
7 Promote artisans
Hand loom and Dhokra metal casting are
famous cottage industries of the area are
in ruined condition to be resumed with
modernisation
15 22 18 55
8 Swatch Bharat Mission
Providing Tractors, Back Hoe cum
toploader, dust bins and development of
the dump yard
300 300 225 825
9 Energy efficient street light Electrification of the village with energy
efficient LED bulbs. 77 78 76 231
10 Plantation and distribution of
saplings in and around the
Adoptation of 5 villages for plantation and
distribution of saplings 5.4 7.2 4.4 17
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Narayangarh, Dist-Paschim Medinipur, WB
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villages
11 Total expenditure 1810
xiv) Occupational Health Measures
Sl. No. Group Item Potential Health hazard Preventive measures
I Raw materials and products handling
Iron ore & Coke, Eye/skin irritation Water sprinkling’ Coal , lime stone/Dolo Respiratory track diseases Dry fogging in
conveyors, ID fan Other fluxing minerals due to Dust, burning due to bag filter, PPE like
safety shoes, Product steel local fire Dust mask and safety
goggles. Acids/Alkalis Water jet for eye
washing II Major shops DRI kiln flue gas CO, dust, heat Pollution Control
Equipments for direct exhaust of the gas
Sinter Plant Dust, heat, Respiratory track diseases, Well ventilation of work place with air ventilating systems
noise Head Ache PPE like gloves, dust mask to prevent dust inhalation
Captive power plant
Fly ash, explosion, noise, vibration, HT, electric equipments, Acid and alkali
Electric shock, injury due to chemicals, burn/ eye injury
Use of PPE, barricading high voltage area.
III Utilities Fuel gas Gas leaks Fire and gas Use of PPE
Distribution Poisoning Electric power
Supply Short circuit Electric shock Use of PPE
IV All shops Falling from
height Collapse of scaffoldings Injury, breaking of bone Proper scaffolding to
withstand Breaking of slings Load and use of safety
belt Tested from time to time.
Falling of heavy People working over Head injury Use of helmet and safety shoes Objects from
height Head, next floor
xv) Post Project Monitoring Plan
Depending upon prevailing predominant wind direction AAQ monitoring stations have been decided
where monitoring instruments shall be installed for measuring polluting parameters at regular intervals.
Similarly Fugitive emission will be monitored twice a month and Stack monitoring will be continuous
with Online monitoring systems. Three locations has been identified for Ground Water and Surface water
monitoring which will be carried out twice in a year. ETP, STP, CT will be monitored once a month or as
per the Standard Operating Procedures.
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-
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CHAPTER-1
INTRODUCTION
1.0 GENERAL
M/s. Bengal Energy Limited (BEL) is a group company which is an agglomeration of
companies actively involved in the trading of steam coal, coking coal, coke and Iron ore
fines etc. It is manufacturer of metallurgical coke & also involved in power generation
&distribution services in Kolkata, West Bengal.
The company has already acquired 161.87 ha of land on which existing project is
operating. The Company was accorded prior Environmental Clearance vide Letter No. J-
11011/28/2008-IA II(I) dated 2nd January 2009 for 0.5 MTPA Integrated Steel Plant, 1.2
MTPA Non-Recovery coke oven plant and 140 MW power Plant.
Out of the facilities granted in EC, the company has installed and running only 0.6
MTPA Non-Recovery Coke Oven and 40 MW Power Plant and balanced facilities have not
been installed and validity period of EC is over. Consent to operate for existing running
facilities issued by West Bengal Pollution Control Board vide letter No-CO 88332 has
been renewed and valid up to 30.3.2022.
The existing operating project is located at-Dauka, P.O-Tentulmuri, PS-Naraingarh, in
Paschim Medinipur district of West Bengal. The location is well connected to rest of India.
The company has come out with expansion proposal for which ToR has already been
issued by EAC (Industry-1) in their 19th meeting held during 8th-9th June 2017. The
expansion proposal is to manufacture 1.0 MTPA steel product by installation of Sinter
Plant DRI kilns, IFs, EAFs, MBF, ASU and 165 MW Power plant in addition to one more
0.6 MTPA Non-recovery Coke Oven unit.
The Government of India has made it mandatory for all developmental projects to
prepare a detailed EIA study so that the impacts of the proposed developmental activity
can be predicted and a suitable management plan can be implemented before
commissioning of a project as per EIA Notification 2006 and amendments thereby.
In view of the above, extensive Base line study has been done as per terms of reference
issued for core zone and 10km radius Buffer zone of project area. EIA/EMP Report has
been prepared in line with the Terms of Reference (ToR) suggested by Environmental
Appraisal Committee (Industry-I).
1.1 PURPOSE OF THE REPORT
The purpose of this EIA report is to collect current base line status, predict adverse
impact on existing environment due to the proposed project &suggest measures to
reduce the burden of environmental impacts for sustainable development. EIA study has
ever increasing importance as a tool for developmental decision-making. Environmental
impact assessment; as an environmental instrument, shall predict proposed activities
that are likely to have a significant impact on the local and regional environment and
hence is subject to a decision for necessary mitigations. It is also used as a planning tool
to promote sustainable development by integrating environmental considerations into a
wide range of proposed action plans.
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The purpose of this EIA study is also to critically analyze the manufacturing process of
different products proposed to be manufactured with reference to types and quantity of
different raw material consumption, possible source of waste water, dust/gas emission
and hazardous waste generation, their adverse impact on environment and health of
flora and fauna & control measures to reduce the pollution and to delineate a
comprehensive environment management plan along with recommendations in proposed
environment management system.
This process is applied prior to major decisions and commitments made by project
proponent while setting up project. A broad definition of environment is adopted. The
social, cultural and health effects are considered as an integral part of EIA. Particular
attention is given in EIA practice for preventing, mitigating and offsetting the significant
adverse effects of proposed project on the environment.
Long term objectives of EIA are to:
1. Protect human health and safety;
2. Avoid irreversible changes and serious damage to the environment;
3. Safeguard valued resources, natural areas and ecosystem components; and
4. Enhance the social aspects of the proposal.
EIA is an administrative process that identifies the potential environmental effects of
undertaking a proposal, and presents these environmental effects alongside the other
advantages and disadvantages of the proposal to the decision-makers. In the vast
majority of EIA procedures this means that the outcome of the EIA process provides
advice to the decision-makers it does not provide a final decision. So, by itself, the EIA
procedures cannot be expected to stop a proposal, although this is an outcome that
some members of the general community and environment groups may expect.
EIA cannot be regarded as a means of introducing an environmental “veto” power into
administrative decision-making processes. Decisions that are unsatisfactory from an
environmental point of view can still be made, but with full knowledge of the
environmental consequences. The final decision about a proposal depends upon the
likely severity of the adverse effects, balanced against other expected benefit.
1.2 IDENTIFICATION OF THE PROJECT & PROJECT PROPONENT:
The project is a red category Integrated Steel expansion project & basically a prime
metallurgical unit proposing to produce 1.0 MTPA steel billets from Sintered Iron Ore and
comes under schedule 3(a) category-A of EIA Notification, 2006.
Gen.ToR 2(ii) Information about the Project Proponent
Managing Director of M/s Bengal Energy Limited is Er.Rajeev Maheshwari. He is an
engineering graduate with a degree in Mining from IIT, Kharagpur and has over 25 years
of overall experience in Mines, Ferro alloys, coal and coke trading business.
Director Mr.Om Jalan, a graduate in Commerce, has over 15 years of experience in the
trading business of coal and coke.
Director – Operations Mr.Navin Maheshwari, Chartered Accountant & Cost Accountant, is
involved in the operational and liaison aspects of BEL.
Chief Project Coordinator Mr.Arun Kumar Maharaj, Mechanical Engineer, has an
experience of over 30 years in power plant, heat exchangers and ESP, responsible for
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rendering his technical expertise in the commissioning and execution of related projects
in Bengal Energy.
President – Projects J K Choudhary, holds a degree in B.Sc (Engineering) and has
worked for many reputed companies, handling top management responsibilities in
Projects, Operation, Maintenance and Marketing namely MMTC Limited, Neelachal Ispat
Nigam Limited, Jindal Steel & Power Ltd, Visa Steel Ltd.
Clientele
Tata Steel, Tata Metaliks, SAIL, Bhushan Power & Steel Ltd, Usha Martin & Mideast
Integrated Steel Ltd. and many more.
1.3 BRIEF DESCRIPTION OF NATURE, SIZE, LOCATION OF THE PROJECT AND
ITS IMPORTANCE TO THE COUNTRY, REGION
1.3.1 NATURE & SIZE OF PROJECT
The existing project of M/s BEL is running with 0.6 MTPA Non-Recovery Coke Oven and
40 MW Power Plant. The proposed expansion is to manufacture 1.0 MTPA steel product
by installation of one more non-recovery Coke oven Plant, Sinter Plant DRI kilns, IFs,
EAFs, MBF, ASU and 165 MW Power plant.
Hence the project is a brown field Red Category steel manufacturing unit. It is a primary
metallurgical industry; manufacturing steel from Iron ore and comes under schedule
3(a), category ‘A’ of EIA notification September, 2006.
1.3.2 LOCATION OF THE PROJECT SITE:
The project is located at-Dauka, P.O-Tentulmuri, PS-Narayangarh, in Paschim Medinipur
district of West Bengal. The project site of M/s Bengal Energy Limited extends from 220
15’ 22.96’’ N to 220 15’ 27.68’’ N and 870 22’ 53.37’’ E to 870 23’ 34.69’’ N, AMSL 32m.
The project has 161.87ha of land which can be found in Survey of India topo sheet No-
F45J8
The existing project has well developed infrastructure and the expansion project will
avail this facility.
Gen. ToR 2(iii) Importance and benefits of the project
1.3.3 IMPORTANCE OF THE PROJECT TO THE COUNTRY AND REGION
India produced 88.97 million tons(mt) , 89.79 mt and 96 mt of crude steel during 2014,
2015 and 2016 respectively. In lieu of this, Govt. of India has drawn following
strategies:
The Minister of Steel & Mines has reiterated commitment of Central Government
to support the steel industry to reach a production target of 300 Million Tonne Per
Annum (MTPA) in 2025.
Government has planned Special Purpose Vehicles (SPVs) with four iron ore rich
states i.e., Karnataka, Jharkhand, Orissa, and Chhattisgarh to set up plants
having capacity between 3 to 6 MTPA.
The Central Board of Excise and Customs (CBEC) has issued a notification
announcing zero export duty on iron ore pellets, which will help the domestic
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industry to become more competitive in the international market. Facts show
importance of setting up steel industry.
Therefore for commercial viability as well as to meet the National target, proposed
expansion is sought for.
1.3.4 NATIONAL STEEL POLICY:
The Indian government announced National Steel Policy (NSP) in November, 2005
envisaging a Compound Annual Growth Rate (CAGR) of 7.3% per annum in the steel
sector up to 2019-20. To achieve this, the NSP aims to increase indigenous production
capacity from 38 MT in 2005 to about 110 MT by 2019-20, through a multipronged
strategy.
However in 2006-07 domestic crude steel production grew at the rate of 10.9%
and consumption at 11.6%, accordingly the estimated for production of steel was
revised in 2008 and was projected at 180MT as target to be achieved by 2019-
20.
In 2010-11 India produced 78MT, in 2012-13 81MT, and in 2013-14 84 MT crude
steel. At the same time world steel production in 2013 and 2014 was 1,607 MT &
1,636MT crude steel respectively.
Need to boost per-capita steel consumption in rural area to improve quality of
life.
Appropriate steps must be taken to ensure adequate and timely supply of basic
Raw materials and processed inputs from domestic and over see sources.
1.3.5 GLOBAL STEEL SCENARIO
In 2017, the world crude steel production reached 1690 million tonnes (mt) and
showed a growth of 4% over 2016.
China remained world’s largest crude steel producer in 2017 (832 mt) followed by
Japan (105 mt), India (101.4 mt) and the USA (82 mt).
World Steel Association has projected Indian steel demand to grow by 7.5% in
2018 and by 7.3% in 2019 while globally, steel demand has been projected to
grow by 3.9% in 2018 and by 1.4% in 2019. Chinese steel use is projected to
grow by 6% in 2018 and show nil growth in 2019.
Per capita finished steel consumption in 2017 is placed at 212 kg for world and
523 kg for China by World Steel Association. The same for India was 69 kg in
2017.
1.3.6 DOMESTIC SCENARIO:
The Indian steel industry has entered into a new development stage, post de-regulation,
riding high on the resurgent economy and rising demand for steel.
Rapid rise in production has resulted in India becoming the 2nd largest producer of crude
steel during the current year (2018) so far, from its 3rd largest status in 2017. The
country is also the largest producer of sponge iron or DRI in the world and the 3rd
largest finished steel consumer in the world after China & USA.
In a de-regulated, liberalized economic/market scenario like India the Government’s role
is that of a facilitator which lays down the policy guidelines and establishes the
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institutional mechanism/structure for creating conducive environment for improving
efficiency and performance of the steel sector.
In this role, the Government has released the National Steel Policy 2017, which has laid
down the broad roadmap for encouraging long term growth for the Indian steel industry,
both on demand and supply sides, by 2030-31.
The said Policy is an updated version of National Steel Policy 2005 which was released
earlier and provided a long-term growth perspective for the domestic iron and steel
industry by 2019-20.
The Government has also announced a policy for providing preference to domestically
manufactured Iron & Steel products in Government procurement. This policy seeks to
accomplish PM’s vision of ‘Make in India’ with objective of nation building and encourage
domestic manufacturing.
Steel industry was de-licensed and de-controlled in 1991 & 1992 respectively.
India is currently the 2nd largest producer of crude steel in the world.
In 2017-18, production of total finished steel (alloy + non alloy) was 126.85 mt, a
growth of 5.6% over last year.
Production of Pig Iron in 2017-18 was 5.73 mt, a decline of 45% over last year.
India was the largest producer of sponge iron in the world. The coal based route
accounted for 79% of total sponge iron production (30.51 mt) in the country in 2017-18.
[Source: Ministry of Steel]
Gen. ToR 12 Any litigation pending against the project and/or any
direction/order passed by any court of law against the project. If so
details thereof. Has the unit received any notice under the section 5 of
Environment (protection) Act, 1986or relevant sections of Air & Water
Act?
1.4 LITIGATION/COURT CASE AGAINST THE COMPANY
No, litigation or court cases are pending against the project nor any direction/order has
been passed by any court of law against the project. The unit has not received any
notice from the regulatory authority under EP Act 1986 or Air & Water Act.
1.5 SCOPE OF THE PRESENT STUDY DETAILS OF REGULATORY SCOPING
CARRIED OUT (AS PER TERMS OF REFERENCE)
The scope of study covers the core zone and the buffer zone covering 10 km radius area
from the boundary of the core zone (plant area). Following are the details of regulatory
scoping carried out:
Literatures have been reviewed and secondary data relevant to the study area
have been collected.
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Environmental monitoring has been conducted to generate baseline data with
respect to soil, air, water & noise as per the terms of reference so as to evaluate
the existing environmental status in the study area.
Incremental levels of pollutants in the study area due to the proposed project
activities have been predicted with the help of software.
Evaluation of the predicted impacts on the various environmental attributes in the
study area has been done using scientifically developed and widely accepted
environmental impacts methodologies.
Environmental Management Plan (EMP) outlining the measures for improving and
restoring the environmental quality of the area for sustainable development have
been worked out.
Regular Environment monitoring program & remedial measure for a clean
environment has been planned.
Details of Occupational & safety Hazards and their mitigation measures have been
made.
1.6 AUTHORIZATION
M/s. Bengal Energy Limited has entrusted M/s Global Tech Enviro Experts Pvt. Ltd.,
Bhubaneswar for the preparation of EIA report for their expansion project.
ToR 2(i) Details of the EIA Consultant including NABET accreditation.
M/S Global Tech Enviro Experts Pvt. Ltd., Bhubaneswar is QCI- NABET accredited “A”
grade consultant Ref: SL No 77.QCI/NABET Notification Dt. March 2019
In accordance to the scope of work, M/s. GTEEPL team visited the project site along with
accredited laboratory team at-Dauka, P.S.-Tentulmuri, in the district of Paschim
Medinipur, W B. During their visit, the team collected samples like Air, Water, Soil &
Noise from the project site for analysis and generation of Base line data and studied
availability of infrastructure facilities like raw materials, water, power and transportation
facilities. The team also made socio-economic study of 10km buffer zone of the project
site to know existing socio-economic status of the locality and studied flora & fauna of
the locality. The representative of M/s.BEL accompanied GTEEPL team during site visit
and Base line study.
1.7 ACKNOWLEDGEMENT:
M/s GLOBAL TECH ENVIRO EXPERTS PVT LTD, Bhubaneswar expresses its deep
gratitude to M/s. Bengal Energy Limited for entrusting the assignment of preparing and
providing all documents required for submission of EIA report and for the active interest
and cooperation extended by the concerned officials of M/s Bengal Energy Limited.
CONCLUSION:
The Company was accorded prior Environmental Clearance to set up 0.5 MTPA
Integrated Steel Plant with coke oven and power plant in January 2009 but then steel
market remained sluggish and the company could not venture to set up steel plant and
could set up a part of coke oven & power plant.
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Now the market has recovered in 2017-18 India’s steel production has reached b126.58
MTPA, and target has been set by the “Ministry of Steel” to achieve the 300 MTPA steel
production by 2030. Hence the company has come up with a fresh proposal for 1.0 MTPA
Integrated Steel Plant in line with the target. The company has acquired sufficient land
to set up the industry but the process route and project configurations are to be decided;
requirement of power, raw material & water to achieve 1.0 MTPA steel to be estimated
and their source and availability to be explored. Cost of the project and completion time
is required to be estimated. Similarly solid waste and waste water generated are to be
estimated. All these aspects need to be addressed in next chapter.
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CHAPTER-2
PROJECT DESCRIPTION
2.0 CONDENSED DESCRIPTION OF THOSE ASPECTS OF THE PROJECT LIKELY
TO CAUSE ENVIRONMENTAL EFFECTS.
M/s Bengal Energy Limited, at: Dakua, Tentulmuri is presently running with 0.6 MTPA
Non-Recovery Coke Oven and 40 MW Power Plant. After proposed expansion M/s BEL will
manufacture 1.05 MTPA steel Billet using facilities of 4x500TPD & 4x350 TPD DRI kilns,
3X20T IF, 2X80T EAF, 2X320 m3 MBF,120 TPD ASU( to produce oxygen & Nitrogen
required for the project), 1.2 MTPA Non recovery Coke oven plant and generate 205 MW
Power from Waste Heat recovery and AFBC.
2.1 TYPE OF PROJECT
The proposed project is 1.0 MTPA Integrated steel expansion project. It is a Primary
metallurgical processing industry to manufacture steel billet for sale through DRI-MBF-
IF/EAF route with facilities of making coke and produce Oxygen & Nitrogen. This being
an integrated steel project comes under Red category polluting industry, but pollutions
will be under control with proper Environmental Management Plan.
2.2 NEED OF THE PROJECT
Steel is a core industry and its demand is strongly linked to the overall economic activity
of the Nation. Given the inherent long-term potential of the Indian economy and its
cyclical nature, the long-term prospects of the steel industry are fairly comfortable. The
demand and production has been growing at a healthy rate for the last few years and
the forecast for the next decade and half is also very promising.
Steel plays a vital role in the development of any modern economy. “Per capita
consumption of steel” is generally accepted as a yardstick of socio-economic
development and living standards of people. No wonder, crude steel production in the
world, since the beginning of last century, has been increasing steadily touching >1.5
Billion Metric Tonne mark in 2014.India produced 88.97 million tons(mt) , 89.79 mt and
96 mt of crude steel during 2014, 2015 and 2016 respectively, where as The Minister of
Steel & Mines has reiterated commitment of Central Government to support the steel
industry to reach a production target of 300 Million Tonne Per Annum (MTPA) in 2025.
As such, no developing country can afford to ignore steel owing to its strategic
importance in development.
The scope for raising the total consumption for steel is huge, Per capita consumption of
steel in India at current levels is about 65 kg. As a comparison per capita steel
consumption in China is 430 kg and the world steel consumption per capita average is
180 kg.
The proposed integrated steel project aims at manufacturing Mild steel& Alloy steel
billets, Coke and Oxygen for sale and internal use. All these products have high market
demand. Steels of different grade has high demand in construction work, equipment
manufacture as well as domestic appliance manufacture and steel as a whole has
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forward and backward linkages in terms of material flow, income and employment
generation.
The facts clearly indicate the importance of this project to manufacture steel.
Gen Tor-4(i) Location of the Project Site Covering village,
Taluka/Tehsil, District and State and Justification for Selecting the
Site, whether Other Sites Were considered.
2.3 LOCATION OF THE PROJECT(maps showing general location, specific
location, project boundary & project site layout)
Location of a manufacturing plant is influenced by important factors like proximity to raw
material resources, infrastructure facilities like road, railway network, power supply etc
and availability of water & other utilities. Considering the above factors and after
inspecting several sites, the company has selected the site at Dauka near Kharagpur in
Paschim Medinpur district of West Bengal.
The location for the proposed expansion project is selected inside existing land At-
Dauka, P.O. Tentulmuri, P.S. Narayangarh Dist. Paschim Medinipur in West Bengal in the
state of West Bengal where existing plant is running. The location is well connected with
road & rail. The NH-60 connecting to Balasore – Rupnarayanpur (Kharagpur) is only 01
Km away from the proposed site & the Balasore-Kharagpur railway line is passing only at
01 Km away from the proposed site. As river Kansabati is flowing 18Km away from the
location, water will be drawn from the river to meet the plant water requirement.
The site is also well connected with the raw material source like coal and iron ore. The
coal will be fetched from Talcher/Ib valley coal fields within 250Km and the iron ore will
be sourced from Joda/Barbil area of orissa, around 200 Km from the proposed
site.Nearest seaport Haladia, Dhamra & Paradeep located nearer to the proposed site.
Location of the proposed integrated steel plant satisfies the requirement of site selection
criteria. The site is not surrounded by heavily populated locations. There There are no
national park, biosphere reserve, historical/archeological sites/monuments and
sea/estuaries etc. within the 10 km radius of the site.
Therefore, the present site fulfils all the basic requirements of the proposed industry and
the statutory requirement of the MoEFCC and hence no alternative site has been
considered. .
2.3.1 GENERAL LOCATION
The project site of M/s Bengal Energy Limited extends from 220 15’ 22.96’’ N to 220 15’
27.68’’ N and 870 22’ 53.37’’ E to 870 23’ 34.69’’ E, AMSL 32m.
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2.3.2 SPECIFIC LOCATION
TOPOSHEET OF STUDY AREA
Gen. ToR 4(ii) A toposheet of the study area of radius of 10km and the
site location on 1:50,000/1:25,000scales on an A3/A2 sheet
(including all eco-sensitive areas and environmentally sensitive
places)
Toposheet of 10km radius buffer zone of project site has been given below.
The Topo sheet shows the connectivity and indicates that the project boundary or the
battery limit does not belong to part of any National Park, wild life sanctuary or Natural/
Biosphere reserve.
Buffer zone also does not contain any features of archaeological/ historical and
cultural/aesthetic importance
From the Toposheet it is seen that
1) There is no major river in the buffer zone of the project site.River Kanska is
outside 10km radius buffer zone
2) Slope is towards Kanska river, i.e. towards north.
3)Kharagpur city is thickly populated and on eastern side of project site.
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Table 2.1 Environment Sensitivity around 10 km radius
Sl.No. Areas Name/
Identity
Aerial distance
(within 10 km.)
Proposed project
location boundary
1 Areas protected under
international conventions,
national or local legislation for
their ecological, landscape,
cultural or other related value
Nil NA
2 Areas which are important or
sensitive for ecological reasons -
Wetlands, watercourses or other
water bodies, coastal zone,
biospheres, wild life sanctuary,
mountains, forests
No such sensitive
areas exist.
NA
3 Areas used by protected,
important or sensitive species
of flora or fauna for breeding,
nesting, foraging, resting, over
wintering, migration
Nil NA
4 Inland, coastal, marine or
underground waters
Nil NA
5 State, National boundaries Nil Not within 10km
radius of project
boundary
6 Routes or facilities used by the
public for access to recreation or
other tourist, pilgrim areas
Nil No such route
present within 10
km. radius
7 Defence installations Nil Not existing
8 Densely populated or built-up
area
Nil Kharagpur town is
beyond 10km
radius
9 Areas occupied by sensitive man-
made land uses (hospitals,
schools, places of worship,
community facilities)
Small places of
worship
Scattered
10 Areas containing important, high
quality or scarce resources
(ground water resources, surface
resources, forestry, agriculture,
fisheries, tourism, minerals)
No such NA
11 Areas already subjected to
pollution or environmental
damage. (those where existing
legal environmental standards
are exceeded)
Nil NA
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12 Areas susceptible to natural
hazard which could cause the
project to present environmental
problems (earthquakes,
subsidence, landslides, erosion,
flooding or extreme or adverse
climatic conditions)
No Zone III of Earth
quake zones
Gen. ToR 4(iv) Google map-Earth downloaded of the project site
Gen. ToR 4(iii) Co-ordinates (lat-Long) of all four corners of the site
2.3.3 PROJECT BOUNDARY & PROJECT SITE LAYOUT
Google -Earth map of M/s Bengal Energy Limited project site, down loaded and has BEEN
shown below been. Co-ordinates of all the four corners of project site have been shown
on satellite picture of the project site.
2.4 SIZE OR MAGNITUDE OF OPERATION (INCLUDING ASSOCIATED ACTIVITIES
REQUIRED BY OR FOR THE PROJECT)
Project configuration & product mix
Gen. ToR 3(ii) Product with capacities for proposed project.
Gen. ToR 3(iii) If expansion project, details of existing products with
capacities and whether adequate land is available for expansion,
reference of earlier EC if any.
This is an expansion project on the same land on which existing plant is running.Prior EC
taken vide F.N0. J-11011/28/2008-IA II(I),2nd January,2008. The existing plant is having
0.6MTPA non-recovery coke oven plant and 40 MW power plant based on waste heat
recovery from coke oven gas.
The expansion project will have one more 0.6 MTPA non-recovery dry quenching Coke
oven plant, 4x500TPD and 4x350 TPD DRI kilns, 2x320m3 MBF, 1x60m2 Sinter plant,
2x80T EAF, 2x20T IF with LF, 120 TPD Air Separation Unit to produce Oxygen and
Nitrogen & 165 MW power generation from Waste Heat recovery & AFBC. So that 1.0
MTPA steel billet Plant, 205 MW power Plant and 1.2 MTPA coke oven plant will be there
after expansion.
Existing project configuration, production capacity, Expansion project configuration,
production capacity and final production capacity of project has been given in the table
2.2 below.
The project has 161.87 ha of land and even after expansion there will be 30.77 ha of
vacant space which can accommodate further expansion. Hence land is adequate for
expansion.
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Table 2.2 Project Configuration Before And After Expansion
Facility Existing
Configuration Existing capacity in TPA
Proposed configuration
Proposed capacity in TPA
Final capacity
Product End use
Non.Recovery C O Plant
1x0.6 MTPA 6,00,000 1x0.6 MTPA 6,00,000 12,00,000 Lam Coke MBF
CPP(WHRB COB) 1x40 MW 40 MW 1x40 MW 40 MW 80 MW Elec. Power Internal use/Sale
DRI Kiln - Nil 4x500 TPD
6,40,000 4,48,000
10,88,000 Sponge Iron EAF & IF
4x350 TPD
CPP (WHRB DRI) - Nil 68 MW 68 MW Elec. Power Internal use/Sale
MBF,2.7T/m3day - Nil 2x320m3 5,96,000 5,96,000 Hot Metal EAF & IF
Sinter Plant 2T/m2.hr, 340days
- Nil 1x60m2 10,00,000 10,00,000 Sinter MBF
EAF with LF, 16H/day, 325days
- Nil 2x80T 8,32,000 8,32,000 Liq. Steel LF
LF - Nil 1x25T HoldingLiq. steel CCM
C C M - Nil 2,500 TPD 8,15,000 8,15,000 Steel Billet Sale
IF15H/day, 325 days - Nil 3x20T 2,92,500 2,92,500 Liq. Steel CCM
C C M - Nil 1,000 TPD 2,80,000 2,80,000 Steel Billet Sale
CPP (BF gas fired ) - Nil 1x22 MW 22 MW 22 MW Elec. Power Internal use/Sale
AFBC - Nil 1x35 MW 35 MW 35 MW Elec. Power Internal use/Sale
A S U - Nil 120 TPD 1,200 m3/hr 1,200 m3/hr
Oxygen Nitrogen
Use in MBF & EAF
2.5 TECHNOLOGY AND PROCESS DESCRIPTION:
Gen. ToR 3(ix) & Additonal ToR 15 Process description along with
major equipments and machineries, Process flow sheet(Quantitative)
from Raw material to products to be provided.
2.5.1 TECHNOLOGY
The process route selected by M/s BEL for 1.0MTPA steel making is through DRI-MBF-IF
and EAF-LF-CCM route. The technology is well proven. In order to utilize iron ore fines
and waste materials sinter will be produced & used in Blast furnace. The unit wise
process description has been discussed below.
12
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2.5.2 PROCESS DESCRIPTION
Additional ToR 16 Details on design and manufacturing process for all the units
1.Coke Oven
Coking coal is crushed & screened and charged in oven of batteries. The shape of
Coal/coke bed is parallelepiped & located in the upper part of the oven. The oven
operates under negative pressure.
Chargrd coal is heated in oven and volatile matter is released from coal and burns inside
on top of the coal bed utilizing air entrained through the various ports/openings
(channels) located in both side doors and the oven roof called primary air.
This burning of VM provides the heat required for the coke making process. Partially
combusted gases exit the top chamber through "down comer" passages in the oven wall
and enter the sole flue. Combusted gases collect in a common tunnel and exit via a stack
which creates a natural draft in the oven for circulation. Secondary air is introduced into
the sole flues which completes combustion.
Due to the temperatures generated, all of the potentially polluting hydrocarbons and
byproducts are completely burnt within the oven and avoid pollution.
The coking front advances from the bottom and from the top, joining somewhere in the
middle. The design of the flues and the control of the air flow allow the coking rate at the
top and bottom of the coal bed to be equalized.
Heat generated due to combustion is only partially utilized in making Coke and balance
heat goes with waste fluegas and recovered in WHRB generating steam at pressure
which drive turbogenerator and generates power.
The cool waste gas is cleaned in a flue gas desulfurization plant prior to being discharged
to the atmosphere Desulphurization is carried out by aspersion of lime slurry on the
gas. At least 80% of the SO2 generated during coking is eliminated. This equipment
generates solid calcium sulfate and sulfide as a waste
EIA/EMP report of M/s Bengal Energy Limited, At-Dauka, P.O.Tentulmuri, PS-
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COKE OVEN FLUE GAS FLOW PATH
Coke oven gas of 93,000 to 1, 15,000Nm3/hr. at temperature of 9000C to 12000C comes
out of each battery. The gas composition will be about
CO2 7.1 %
H2O 13.0 %
N2 71.2 %
SPM 76.0 mg/m3
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SO2 224 ppm
CO gas can be cooled down to 160-1700C after heat recovery in boilers. After recovery
of waste heat Coke Oven gas can be vented to atmosphere through ID fan & high stack.
Stamp charging of coal in the ovens will be adopted. Stamp charging technology
facilitates to produce high strength & high quality BF coke. Stamp charging reduces
emission during charging and minimizes door leakages.
Non-Recovery type Coke Oven has following advantages
Various types of coal can be blended for production of coke without affecting the
quality of coke.
Cost of production is less due to usage of low rank coal.
Emission can be minimized as ovens are operated in negative pressure and
operated in close loop system.
Utilization of waste heat for generating steam and power.
Lower Capital investment.
Major Equipements of Coke Oven after expansion has been given in Table 2.3
Table 2.3 Configuration Coke Oven Plant
Sl. No Component Existing for 0.6
MTPA
Proposed for
expansion0.6 MTPA
Total
1 No. of Battery 04 04 08
2 No.of Ovens 160 160 320
3 Coal stamping box 02 02 04
4 Charging car 02 02 04
5 Pushing car 02 02 04
6 Hot coke car 02 02 04
7 Quenched Coke
Pusher
02 02 04
8 Flue dampers for
stacks
04 04 08
Quality of LAM Coke From 1.2 MTPA Cove Oven Plant
Ash 2.5 % Max
Sulphur 0.6 % Max
Phosphorus: 0.03 % Max
CSR 63-66%
CRI 23-25%
M 10 8 Max
M 40 82 Min
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Steam Turbo Generator
Multistage, Nozzle governed, Horizontal spindle, two bearings, Impulse type bleed cum
condensing steam Turbine suitable to receive steam flow of 140-160 TPH at 64 kg/cm²
pressure, 480°C temperature and 35 to 40 MW power can be generated from 0.6 MTPA
Coke Oven Plant.
Additional ToR 10 System of coke quenching adopted with justification
Coke Dry quenching
Dry Coke Quenching is an energy efficient and environmental friendly technology. In this
process, Red-hot coke at about 1,100°C is charged into the coke cooling tower, and inert
gas normally Nitrogen is blown into the tower from the bottom. Heat exchange takes
place with the circulating inert gas. After the gas is heated to a high temperature like
800°C, it is introduced to waste heat recovery boiler to convert water in the boiler tubes
into steam. The temperature of the coke at the cooling tower outlet is reduced to approximately 200°C.
DRY QUENCHING FLOW SHEET
Inert Gas moves upward and Coke moves downward by gravity and in the process, they
exchange heat. Coke is discharged at the bottom. The passage time of the coke through
the chamber / cooling chamber is around 5 to 6 hours and the rate of inert gas required
for cooling is around 82,000 Nm3/hr.
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The hot Inert gas coming out from cooling chamber contains heavy coal dust &
suspended particles. Coal dust may deposit on water tubes of WHRB and reduce its heat
transfer efficiency hence inert gas is passed through Primary & Secondary dust collectors
Justification of dry quenching
Due to advantages as stated below, dry quenching is justified.
Advantage of Dry quenching
The moisture content of coke produced by dry cooling as around 0.2 % as
compared to that of around 5 % in wet quenched coke. It helps in reducing the
coke rate in blast furnace. Moisture in coke needs additional heat in the blast
furnace for evaporation.
Use of dry cooled coke reduces the coke rate in the blast furnace by around 2 % -
2.5% as per blast furnace units.
Since the hot coke is cooled gradually by the inert gas, it is free from surface pore
and internal cracks normally present in the wet quenched coke
Water consumption is reduced significantly & waste water handling is ruled out.
The waste heat is recovered in general can produce steam @500-700kg/T of
coke, hence 140-185 kwn/T of coke can be generated. So from proposed
0.6MTPA coke oven it is expected that about 8MW power can be generated.
2.DRI Kiln
Sponge Iron is the metallic form of iron produced from reduction of iron oxide below the
fusion temperature. It is obtained when iron oxide (generally lumpy iron ore –
“Hematite”) is reduced to metallic form in solid state itself. Since there is no melting,
external shape is retained. Color changes from red to black. Due to removal of oxides
there is 30% reduction in weight. The true density changes from about 4.4 to 7.8
gm/cm3. Thus, there is about 54% reduction in true volume and this is manifested in the
formation of pores throughout the interior of sponge iron pieces. Under the microscope,
a sponge like structure is seen and hence it is named sponge iron, but it is not at all soft
like sponge as the name suggests.
Two processes of direct reduction of Iron ore is prevailing all over the world. 1) Gas
based & 2) solid or Coal based.
M/s BEL is proposing 4 rotary DRI kilns of capacity of 500 TPD and 4 nos. 350 TPD
capacity based direct reduction of hematite ore by SL / RN process technology.
Coal based processes
Customized or Indigenous Process:
In India, the coal based DRI production process employs a rotary kiln as the main
reactor wherein the process of reduction of the iron oxide is carried out with coal as
reductant. Refractory lining of about 150-200 mm thickness is given inside the kiln to
protect the shell. The kiln has a general slope of 2.5 - 3% down towards the discharge
end. There is air blowers mounted on the kiln shell having dampers to provide required
air for combustion at different heating zones.
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Sized iron ore and coal in required proportion are fed in to the kiln with the help of the
weigh feeders at the feed end. Due to the rotational motion of the kiln and due to the
slope provided, the charge moves forward to the discharge end. Thermocouples are
mounted on the kiln to measure and control the temperature of the different heating
zones. Fine coal is also injected through the discharge end of the kiln with the help of the
coal injector machines & lobe compressor, to meet the additional carbon and volatile
matter requirement of the reaction. Kiln discharge material which is a mixture of sponge
iron and char (mixture of unreduced iron, uncalcinated limestone, gangue and semi
burnt coal) is taken to a rotary cooler. Water is sprayed on the cooler shell to indirectly
cool the kiln discharge mix to about 120°C. The cooler also has a slope of about 2.5%.
The cooler discharge falls onto a hopper and taken through conveyors for screening of
fines and coarse materials. After separating the -3 mm and +3 mm sizes in the product
screen, the cooler discharge mix is subjected to magnetic separation where sponge iron
is separated from char. Sponge iron and char of coarse and fine sizes are stored in
separate silos or hoppers.
The reducing gases generated from the combustion of the coal, flow counter current to
the direction followed by the solids and emerge from the feed end. The kiln is maintained
at a positive pressure of about +5 mm water column. The flue gases then pass through
the gravitational Dust Settling Chamber (DSC) and pass on to the After Burning
Chamber (ABC) located right above the DSC. In the ABC, the residual CO is converted
to non- toxic CO2. Therefore, in ABC the off-gas laden with combustible matter is burnt.
On the top of the ABC, there is an emergency cap to maintain the kiln pressure by
letting out the accumulated gases.
The latest trend in DRI plant is to use Electrostatic Precipitator for dust trapping. In this
system, the flue gas, at about 900 °C - 950°C, is taken to a Gas Conditioning Tower
(GCT) where quenching water is added to cool the gas to about 150°C. The cooled gas
then travels to the Electrostatic Precipitator (ESP). Dust is trapped in the ESP and the
flue gas is let out using chimney.
DRI plants install Waste Heat Recovery Boilers (WHRB) after the ABC, to utilize the
waste heat content of the flue gas. The WHRB generates steam at high pressure and use
it to run turbines and produce electricity.
Reaction mechanism of coal based DRI kiln:
There are two major temperature zones in the kiln. The first pre-heat zone is where the
charge is heated to 900 — 1000°C. The second metallization zone is held fairly constant
at 1000-1050°C.
The charge into the kiln consists of a mixture of iron oxide lump, fluxes such as
limestone and/or dolomite (amount depending of sulfur content of the coal) and medium
volatile non-coking coal. In the pre-heating zone, the moisture is driven off first, and
then the hydrocarbons and hydrogen evolve by thermal decomposition of the coal.
As the combustible gases rise from the bed of solid material, a portion of the gases is
burnt in the free board above the bed by controlled quantities of air introduced through
the air tubes. As the kiln rotates, the primary mode of heat transfer is by radiation to the
tumbling charge and subsequently by internal solids mixing and renewal of the exposed
bed surface.
In the pre-heat zone, the reduction of iron oxide proceeds only to ferrous oxide (FeO)
(Equation 1).
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Fe203 + CO = 2 FeO + CO2............................ (I)
Final reduction to metallic iron occurs in the metallization zone by reaction of CO with
FeO to form CO2 and metallic iron (Equation II).
FeO + CO = Fe + CO2 ........................... (II)
Most of the CO2 reacts with the excess solid fuel in the kiln and is converted to CO
according to the Boudouard reaction (Equation III).
CO2+C= 2CO............................ (III)
Coals with higher reactivity are preferred as they provide rapid conversion of CO2 to CO,
thereby maintaining reducing conditions in the kiln metallization zone. The highly
endothermic reaction of coal with CO2 prevents the bed from overheating and attaining
high temperature that could lead to melting or sticking of the charge.
High coal reactivity decreases the reduction zone bed temperature but increases the
relative capacity. Desired bed and gas temperature in the freeboard can be achieved
with high reactivity fuels even with very high throughput rates.
DRI kiln flow sheet of M/s BEL.
3. Mini Blast Furnace:
Blast furnace is a vertical shaft furnace that produces liquid metal from lump iron ore /
and sinter by the reducing action of carbon(coke) at a high temperature in the presence
of a fluxing agent limestone. Blast furnaces consist of several zones: a crucible-shaped
hearth at the bottom of the furnace; an intermediate zone called a bosh between the
hearth and the stack a vertical shaft (the stack) that extends from the bosh to the top of
the furnace; and the furnace top, which contains a mechanism for charging the furnace.
The furnace charge, or burden, of iron-bearing materials (e.g., iron-ore pellets and
sinter), coke, and flux (e.g., limestone) descends through the shaft, where it is
preheated and reacts with ascending reducing gases to produce liquid iron and slag that
accumulate in the hearth. Air that has been preheated to temperatures from 900° to
1250° C together with injected fuel such as pulverized coal is blown into the furnace
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through multiple tuyeres (nozzles) located around the circumference of the furnace near
the top of the hearth; these nozzles may number from 12 to as many as 40 on large
furnaces. The preheated air is, in turn, supplied from a bustle pipe, a large-diameter pipe
encircling the furnace. The preheated air reacts vigorously with the preheated coke,
resulting in both the formation of the reducing gas (carbon monoxide) that rises through
the furnace, and a very high temperature of about 1,650° C that produces the liquid iron
and slag.
The bosh is the hottest part of the furnace because of its close proximity to the reaction
between air and coke. Molten iron accumulates in the hearth, which has a tap hole to
draw off the molten iron and, higher up, a slag hole to remove the mixture of impurities
and flux. The hearth and bosh are thick-walled structures lined with carbon-
type refractory blocks, while the stack is lined with high-quality fireclay brick to protect
the furnace shell. To keep these refractory materials from burning out, plates, staves, or
sprays for circulating cool water are built into them.
The stack is kept full with alternating layers of coke, ore, and limestone admitted at the
top during continuous operation. Coke is ignited at the bottom and burned rapidly with
the forced air from the tuyeres. The iron oxides in the ore are chemically reduced to
molten iron by carbon and carbon monoxide from the coke. The slag formed consists of
the limestone flux, ash from the coke, and substances formed by the reaction of
impurities in the ore with the flux; it floats in a molten state on the top of the molten
iron. Hot gases rise from the combustion zone, heating fresh material in the stack and
then passing out through ducts near the top of the furnace.
Technology: High temperature melting of Iron ore/Sinter using coal, coke and Oxygen.
Design parameter:
BF Volume: 2 x 320 cum
Productivity: 2.70 t/cum/day/Furnace
Charging system PLC controlled batching, weighing and
Charging by belt Conveyors
No. of working days: 345 days
Tapping 10 taps/day (avg.)
In order to reduce the coke rate and to ensure furnace productivity it is proposed to
install three checker filled type stoves. The stoves will be fired by clean blast furnace
gas. The stoves are designed to provide hot blast at a temperature of 1150 deg C.
PCI system
The Pulverized coal dust injection system will be adopted to reduce costly coke
consumption.
Raw coal will be ground to produce coal of 80% below 75 microns. Inert atmosphere will
be maintained in the ball mill for safety. The ball mill will be connected to bag filter. The
powder coal will be stored in the fine coal silo and injected through tuyeres.
Gas cleaning plant
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A gas cleaning plant to clean the raw BF gas from dust catcher with the following main
technological parameters is envisaged. A gravity type dust catcher (inner diameter 8.5
m) will be installed forcollection of larger size dust from raw blast furnace gas. A spiral
conveyor will be installed below the dust catcher to collect dust and the dust will be sent
to sinter plant through trucks. The fine dust laden gas will subsequently be passed
through double venture scrubbers for further arrest of dust. The advantage of this kind
of scrubber is that is greatly reduces investment cost and its maintenance is easy. In
ventury scrubber with variable throat water will be spread at a control rate to obtain
desired cleanliness of gas. The gas than will pass through a cyclone for removal of
moisture and finally the gas passes through an automatic leaf type gate valve filter and
clean gas at a pressure of 0.08-1.0 kg/ cm2 will be delivered for stove heating and power
plant. The water from gas cleaning plant shall be classified in rake classifiers and BF
Sludge in the form of cake will be transported for use in sinter plant as it contains more
than 40% Fe2O3 and about 37% carbon.A flare stack will be provided to burn
excess/unused BF gas. Water seal pot will be used to prevent back firing.
BF gas has the following characteristics
Very low calorific value (CV) in the range of 700 to 850 Kcal/Cu m. CV is very
much dependent on the coke rate.
It has a high density. It is around 1.250 Kg/Cu m at the standard temperature
and pressure (STP) which is 0 deg C and 1 atm. Pressure. This density is highest
amongst all the gaseous fuel. Since the density is higher than the density of air it
settles in the bottom in case of a leakage.
It has low theoretical flame temperature which is around 1,4550 C.
It has low rate of flame propagation. It is lower than any other common gaseous
fuel.
BF gas burns with a non- luminous flame.
Auto ignition point of BF gas is around 6300 C.
BF gas has lower explosive limit (LEL) of 27% and upper explosive limit (UEL) of
75% in an air gas mixture at normal temperature and pressure.
The high pressure of BF top gas is utilized to operate a generator (Top gas
pressure Recovery Turbine – i.e. TRT in short). TRT can generate electrical
energy (Power) up to 35 kWh/ ton of hot metal, i.e. about 2.5 MW without
burning any fuel..
Slag granulation system
Liquid slag coming out of blast furnace will be granulated by high pressure water Jet
(below box). The slag will flow in the slag runner in the cast house in the end of which a
granulator will be installed. The solidified slag granules and water mix will flow into a
settling tank, where the solids will settle down at the bottom. Hot clear water will flow
into a clean water tank for recycling. The granulated slag will be lifted by a grab crane
and taken to the storage area by trucks.
Pig casting machine and ladle repair shop
Two pig casting machines will be provided to cast hot metal into pigs as required. The
pig casting machine will be of strand type. The weight of each pig can be below 10kg for
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ease of handling. From the machine, the pigs will be collected directly in a pig handling
truck, placed below the pig casting machine. The loaded pig handling truck will be taken
out to storage/despatch area after weighment in the weigh bridge.
Pig casting machine will be provided with to cast the liquid hot metal into pigs. There will
be a ladle repair shop adjacent to PCM for handling the ladle brought in for relining.
Technological parameters of MBF
No of blast furnace 2
Useful volume, m3 320
Productivity, t/d m3 2.66
I % iron in HM 92
Coke rate (dry), kg / THM 470
PC injection, kg /THM 80
Slag rate, kg / THM ( Tons of Hot Metal) 300
Top pressure, kg/cm2 (g) operating 0.8
About 2.5 MW power can be generated from BF Top gas by setting up pressure Recovery
Turbine.
4. Induction Furnace
BF-Basic OxygenFurnace route is selected for integrated steel Plants having annual
production capacity>1.0 MTPA. DRI-EAF-IF route of steel making is adopted for mini
steel plants of capacity 0.5 to 1.0 MTPA.
India is the first country using Induction Melting Furnaces for making mild steel. As a
matter of fact, EAFs are not making mild steel of structural quality for over a decade
now. The bulk of structural quality mild steel for long products is manufactured by
Induction Melting Furnaces. The EAF units have also installed Induction Melting
Furnaces. There are several reasons for the popularity of Induction Melting Furnaces for
making steel. They consume less power comparing EAFs. Expenditure on electrode is nil.
They use lesser quantity of refractory. Initial investment is less on plant and equipment.
Thus, there are economic advantages in making steel through Induction Furnaces route.
M/s BEL proposes medium frequency coreless Induction Furnace. A coreless furnace has
no inductor or core, unlike the channel furnace. Instead, the entire bath functions as the
induction heating area. Copper coils encircle a layer of refractory material surrounding
the entire length of the furnace interior. Running a powerfulelectric current through the
coils creates a magnetic field that penetrates the refractory and quickly melts the metal
charge material inside the furnace. The copper coil is kept from melting by cooling
waterflowing through it.
The furnace coil, which produces the electromagnetic field is not designed to get hot.
Although some heat is conductedfrom the molten bath through the lining to the coil,
most ofthe heat load on the coil is caused by current flowing throughit. This requires that
it becontinually cooled, not only to increase its electrical efficiency but to prevent it from
melting.
Typically, the cooling system is built into the coil itself whichis made of hollow copper
tubing in which the cooling waterflows. The water picks up the heat caused by the
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current aswell as heat conducted from the metal through the refractoryand carries it to a
heat exchanger for removal.
M/s Bengal Energy Limited proposes to install 3x20T, 10H IFs. The charge will be
approx:32% hot metal, 62% DRI, 6%scrap and pig iron.
Furnace transformer rating= 7MVA
5. Electric Arc Furnace
Steel making in India utilizes oxygen as well as electric energy. About 56% of total steel
is made using electric route. Out of this 56%, 22% steel is made on Electric Arc
Furnaces (EAF) and rest on Induction Furnace (IF). Lately, there has been varying
inclination towards adapting EAF technology for steel making in India. This is mainly
because of factors such as investment cost, operational cost, raw material availability,
government policies etc.In Electric Arc Furnace steel making method, scrap or DRI or
some amount of hot metal are added to the furnace. Arcing is done to melt the solid raw
material. Oxygen is blown to reduce the carbon.
EAF works with the principle of generating electric arc on the raw material and melting it
with heat. Normally connected to a transformer of 3 phase electrical source, graphite
electrodes are used for transferring the electrical energy to the raw material kept in the
vessel and creating the arc. It is a batch process and when molten metal is tapped to the
ladle it is called as ‘heat’, hence to specify the electric arc furnace mainly two points are
required: Heat Size & Transformer Capacity.
The EAF are of heat size varies from 5T to 300T. This can process any raw material like
scrap, DRI or hot metal. EAFs were developed with the idea of melting scrap. In the
beginning, these were used mainly for foundries and for small alloy making units. But
knowing the advantages of productivity, energy utilization, metallurgical working etc,
EAF became popular in integrated steel plants also with all heat sizes.
Advantages of EAF are many. It is the equipment which can be tailor designed,
specifically suiting the requirement of the process. In different countries based on the
raw material availability, technology suppliers adjust the design of EAF. In western
countries, where scrap availability is high, EAF operates for scrap melting and in Middle
East, where gas based DRI is available; EAFs are designed for flat bath operation.
In case of operation of an EAF, the cost of electricity is the major component. In case of
IF the requirement of electricity is similar like EAF. However, in EAF, part of the electrical
energy can be substituted by chemical energy (exothermic reaction of carbon with
oxygen) leading to lower costs.
Steel quality depends upon possibility and efficiency of the particular melting unit to
remove undesired elements like C, S, P etc. On this frontEAF score over IF.
In case of EAF when raw material is DRI, dephosphorization can be done in EAF and
desulphurization can be done during ladle refining. Such metallurgical work is not
possible in IF.
After melting the raw material, if the liquid melt contains P higher than the specified
limits, P is converted to oxides with oxygen blowing and remains in slag of EAF. De-
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phosphorization occurs near steel melting point, by maintaining an oxidizing atmosphere
i.e. Oxygen blowing which increases the content of oxygen in the metal bath.
M/s BEL proposing 2x80T, 16 H EAF for making alloy steel of low S &P.Hot metal will be
transferred from blast furnace to steel melt shop at one end of the furnace aisle. Hot
metal will be charged into the EAF, utilizing the shop crane, through side launder.
Production MS & CS billets
2x80T EAF and 3x20T IF will consume about 68% solid charge and 32% hotmetal from
MBFs and produce liquid steel. This will be treated in ladle Furnace for secondary
metallurgical treatment before casting in to billets.The grades of steel of production of
saleable billets has been proposed as follows:
CS IS:1875/71
CS IS:2830/75
CS IS: 2831/75
MS IS: 432/66
MS IS: 2062/69
6. LADLE FURNACE (LF)
LF will be equipped with arc heating, inert gas stirring, wire feeding and alloy addition
facilities. This unit will also be utilized to hold the heat for an extended period of
timeshould it be necessary for reasons, such as sequencing of heats in CCM. Provision
for bottom purging with Ar/N2 will be provided.
The refining cycle time in the LF will normally be around 30 to 40 minutes, depending on
the extent of treatment and holding required. All heats from EAF can thus be
conveniently handled by LF.
Number of units: One (1)
Nominal capacity: 80 tons
Transformer rating: 15MVA
Type of unit: Lift / lower roof type
The furnace cover (roof) will be of the lifting and lowering type. The ladle will be brought
to the treatment position on a transfer car. The LF cover will be water-cooled. LF unit will
be equipped with ferro-alloy storage bunkers and addition facilities, wire feeder, hand
held temperature measurement and sampling device and inert gas rinsing facility from
ladle bottom.
Argon rinsing station
Provision of an on-line argon rinsing installation will be kept in the layout for rinsing of
the steel and temperature measurements. The steel grades not requiring temperature
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adjustment and alloy additions and also not requiring hold up for sequencing operations
can be directly delivered to CCM, after rinsing and temperature measurements.
Vacuum degassing (VD) unit (optional)
It is proposed to install one VD unit for treatment of steel for low gas content. In
addition, for evacuation of gases, rinsing if steel by inert gas through porous plug and
small amounts of alloy addition for trimming temperature measurement and sampling
can be done. Treatment time in VD unit will be around 30 minutes.
Liquid steel handling
Liquid steel from the IF and EAF will be tapped into a preheated ladle, while it is placed
on a transfer car. Each ladle will be equipped with a slide gate system and fitted with
porous plug at the bottom for inert-gas stirring. The steel in the ladle will be tapped free
of slag as far as practicable. The transfer car will transfer the steel ladle into the LF aisle
for treatment at LF. After treatment, the ladle will be placed on the lifting and lowering
type ladle turret of the CCM by the overhead crane. On completion of the casting, the
slag in the ladle will be dumped on the ground in a specified area. The ladle will then be
taken back to the preparation area and placed on the ladle stand for slide gate and
porous plug setting and preheating.
7. CONTINUOUS CASTING MACHINE (CCM)
No. of machines One Hi-speed caster
No. of strands Three with provision for 4th strand.
Type of machine Tubular moulds, bow type and multi-point
unbending
Steel grade to be cast Alloy and special steels including auto
grades, spring steel (Si-Mn), free cutting
steel, LC/HC steel.
Ladle capacity, T: 80 and 25
Ladle handling Ladle turret
Size range to be cast: Size / Length 120-140 Sq.mm / 6 to 12 m
Design Speed Up to 6.0m/min
Billet cutting device: Auto gas cutting machine
Method of discharge: On horizontal discharge roller table to turn
over cooling bed with billet packet device
The CC machine will be equipped with ladle shroud manipulator to protect the metal
stream from atmospheric oxidation during teeming operation. Necessary tundish
preparation facilities, moulds and Segment assembly, testing and storage facilities will
also be provided. Automatic control system for functioning of the billet casting
equipment including casting speed, primary/secondary cooling water system and billet
transfer system up to the end of cooling bed will also be provided. Provision of
emergency water supply to caster will be made.
8. SINTER PLANT
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The two main technologies for agglomeration are sintering and pelletizing. The sintering
process is adopted for agglomerating relatively coarse iron ore fines whereas pelletizing
is adopted in case of very fine ores generated during beneficiation.
The sintered iron ore, which comes out as big cakes at discharge end is broken to –150
mm size lumps by a sinter breaker. Then the sinter is sent to the sinter cooler. The cold
sinter is sent by conveyor to the cold sinter crushing and screening building which
generates the different size products:
5 to 50 mm size sinter is sent to blast furnaces.
–5 mm size return fines are sent to proportioning building.
Apart from conservation of iron ore by utilizing the ore fines, instead of discarding, the
other benefits of charging sinter into blast furnace are listed below:
Utilization of steel plant wastes, such as flue dust, mill scale, coke breeze etc.
during the sintering process.
Decrease in coke rate of blast furnace.
Increase in productivity of blast furnace.
Reduction of charging of raw lime stone and dolomite into BF.
Decrease in production cost of iron.
M/s BEL is planning to install sinter plant for catering to its blast furnaces requirement
and reduction of hot metal production cost.
The process of sintering iron ore fines is defined as an agglomeration process in which
coarse iron ore fines (-10 mm size) are joined together by firing them together in the
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presence of carbonaceous fuel so as to generate incipient fusion between the particles.
The fused particles join together and form cake. These are then cooled and crushed to
desired size and screened before sending them to blast furnace.
It is found that fluxed sinters are more beneficial to blast furnace as compared to non-
fluxed sinter. This is because, by charging the entire flux requirement of blast furnace
into the sinter mix the heat required for calcinations of fluxes could be reduced to a
great extent. Such a step led to reduction in heat load inside the blast furnace resulting
in decreased coke rate.
In order to obtain good quality sinter, the ore fines, fluxes, fuel and dust from de-dusting
plants etc. have to be mixed in proper proportions. For this purpose, the materials are
kept in separate bunkers and calculated amounts are collected from respective bunkers
by means of weigh feeders on to a single conveyor which transports them to a mixing &
nodulizing drum. The sinter mix components are thoroughly mixed inside a rotating
drum which also helps in formation of small nodules of the sinter mix. The nodular size
of the mix helps in achieving adequate permeability of the sinter mix bed when charged
on to the sintering machine. Measured amount of water is also mixed in the sinter
charge for achieving proper modulization.
The mix from the mixing and nodulizing drum is taken to the sintering building and
charged into the sintering machine which is an continuous chain made up of pellets
having gratings to permit suction of atmospheric air through the sinter mix during the
movement of the sintering bed from one end to the other.
Immediately after completion of charging on the sintering strand, the sinter mix enters
into a heating zone where the carbon particles of the coke breeze get ignited.
Simultaneously, air is sucked through the sinter mix bed by means of suction boxes
(below the pallets) which are connected to the suction fan. While the sinter machine with
sinter mix bed moves forward, the combustion front in the sinter bed moves downwards.
By the time a particular cross-section of the sinter bed reaches the discharge end, the
combustion front reaches bottom of the sinter mix and the sintering process gets
completed.
Technological parameters of Sinter plant
No of Sinter Plant 1
Useful Area, m2 60
Productivity, t/ m2.hr 2.1
I % iron in sinter 65 (minimum)
No of working days in a year 340
Fuel for ignition BF gas
Calorific value of BF gas 700-800 kcal/m3
Size of Sinter for BF feed +5 to - 50 mm
9. OXYGEN PLANT
Atmospheric air is the main input to the Oxygen Plant and it is sucked by air
compressors through filter media, air enters a purifier consisting of twin Molecular Sieve
driers, working alternatively. The Molecular Sieves remove the Carbon dioxide &
moisture from the process air before the air enters Air SeparationUnit.
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The air has to be cooled to sub- zero temperatures for liquification & the cryogenic
refrigeration & the cooling is provided by highly efficient turbo expander, which cools the
air to temperature almost below -165 to-1700C.
Oil free, moisture free and Carbon Dioxide free air enters into low pressure plate fin type
Heat exchanger where the air is cooled below sub- zero temp, by air expansion process
in the turbo expander.Due to the excellent thermal efficiency we can achieve a
temperature difference delta t as low as 20 C at the warm end of these exchangers.
Air gets liquefied when it enters the air separation column & gets separated into oxygen
& nitrogen by the process of rectification.
In cold box, air is separated into its components by means of distillation which employ a
thermal process known as cryogenic rectification to separate the individual components
from one another in order to produce high-purity nitrogen, oxygen and argon in liquid
and gaseous form. Oxygen & nitrogen so obtained is compressed to 30 bars and sent to
Bullets/Steel melt.
Liquid Oxygen is available at the outlet of the ASU at a purity of 99.6%.
Liquid Nitrogen is also available at the outlet as a alternate product at purity of
99.99%(up to 3ppm as required).Nitrogen gas will be available as a byproduct.
Production capacity of the Oxygen Gas Plant is 1 x 1200 m³/hr. Out of the gaseous
oxygen, Liquid Oxygen & Nitrogen is 120 TPD & liquid argon is 3 TPD. Adequate bullets
for oxygen store will be installed. The oxygen will be supplied in processing plants as
and when required. No water or fuel is required in the manufacturing process though
compressors and other machines need cooling water to remove heat of compression.
The dust free atmospheric air is sucked in by a multi-stage air compressor through a
filter and compressed to the working pressure. After each stage, intermediate coolers
and water separators are provided. The compressed air then passes through the
evaporation pre-cooler and then to the alumina-molecular sieve battery where the
moisture and carbon di-oxide are removed from the process air. It then passes through
the heat exchanger No.1 where it is cooled by the out-going waste nitrogen and product
oxygen. A part of this cold air then flows through an expansion machine and the balance
through the 2nd heat exchanger. An expansion valve, RI, controls the ratio of the two
air streams. Both these streams of air then unite in the medium pressure column where
it partially liquefies. The liquid air (rich liquid) then passes through the expansion valve
R2 to upper column, which is at lower pressure than the medium pressure columns.
Similarly, the liquid nitrogen (poor liquid) travels from the medium pressure column to
the upper column through an expansion valve R3 where the separation of oxygen and
nitrogen occurs. Nitrogen being more volatile passes out as a gas from the top of the
column of the Oxygen plant and this waste nitrogen flows through both the heat
exchangers cooling the in-coming air. Similarly, the product oxygen is also passed
through the two heat exchangers to cool the incoming air and then to the filling manifold
via a liquid pump.
Air separation plants produce nitrogen, oxygen and argon using air as raw material and
electrical power & cooling water as utilities. While there are variations in process details,
reflecting desired product mix and other factors, all air separation plants below to one of
two general process categories.
10. POWER PLANT
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Additional ToR 9 Plan for utilization of energy in off gases (coke Oven,
Blast furnace)
Total power production has been envisaged at 205 MW, including existing 40 MW based
on running Coke Oven Plant.
Sum up of 205 MW: 40 + 40 MW power shall be produced by utilizing waste heat of
gases from coke oven for which 4 X 2 numbers of waste heat recovery boilers shall be
installed with 2 numbers of turbo generator sets of 40 MW each. 90 MW Power shall be
produced by utilizing waste heat of DRI kilns, and Blast furnace gas for which waste heat
recovery boilers and gas fired boiler with 1 number turbo generator set would be
installed. Generation of remaining 35 MW power has been envisaged based on AFBC
Boiler.
WHRB and AFBC Boilers will have same specifications, which are as follows.
Working Pressure 66kg/cm2 abs
Super heater temperature 4850C
BFW temperature 1300C
Operating hours 365x24hrs
The boilers will be complete with evaporator steam drum, mud drum, bank of super
heaters, economizers, ID fans, ESPs and internal piping etc. Soot blowing and de super-
heating system will also be provided.
Emergency DG Set
No. 2000 kVA emergency DG set will be provided to cater the loads during emergency
conditions. The DG set will be sized considering the essential loads like steam turbine
lube oil system, generator seal oil systems, Air pre-heaters, turning gear motor, jacking
oil pumps, lifts, battery chargers, emergency AC lighting, etc. during any emergency
condition. The DG Set will be started automatically in case of failure of AC Power. Manual
starting facility from Central Control Room will also be provided in addition to automatic
starting.
2.5.1 PROCESS AND MATERIAL FLOW DIAGRAM
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2.5.3 MATERIAL BALANCE:
Material Balance of 2x320m3 MBF
Input in TPA Output in TPA
Sinter 6,04,000 Hot Metal 5,96,000
Hematite ore 2,58,000 BF slag 1,84,760
Coke 2,86,080 BF sludge+ dust 2,93,670
PCI 42,910 BF gas 1,76,560
Dolomite 60,000 - -
Total 12,50,990 Total 12,50,990
Material balance of 1x60m2 Sinter Plant
Input in TPA Output in TPA
Iron Ore fines 7,68,000 Sinter 6,72,000
Lime stone/dust 96,000 Flue gas 2,76,500
Dolomite fines 76,500 - -
Coke breeze 62,400 - -
BF Dust & sludge
Recycle
2,73,600 - -
Total 12,76,500 Total 12,76,500
Material balance of 4x500 TPD & 4x350 TPD DRI Kilns
Input in TPA Output in TPA
Hematite Iron Ore 17,40,800 Sponge Iron 10,88,000
Coal 8,61,700 Dolchar 2,72,000
Injection Coal 5,36,500 DRI dust 5,93,850
Air injection 6,08,900 Flue gas 52,62,350
Lime stone 43,500 Fly Ash 12,27,300
Combustion Air 46,52,100 - -
Total 84,43,500 Total 84,43,500
Material balance of 3x20T IF & 2x80T EAF
Input in TPA Output in TPA
DRI 6,30,000 Liquid Steel 11,24,000
Hot metal 5,39,000 Slag 1,20,000
Pig 57,000 Flue+ Dust 24,000
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Scrap 22,000
Ferro alloys 20,000
Total 12,68,000 Total 12,68,000
Iron balance
Fe from DRI@85% =5, 35,500 TPA Liquid steel 11, 24,000 TPA
Fe from HM & Pig @92% = 5, 48,320 TPA
Fe from Scrap @95% = 20,900 TPA
Ferro alloys ~19,500 TPA Total 11, 24,220 TPA
Material balance of1.2 MTPA Coke Oven Plant
Input in TPA Output in TPA
Coking CoalNet & Dry 16,80,000 LAM Coke & coke breeze 12,00,000
Coke Oven gas 4,80,000
Total 16,80,000 Total 16,80,000
Material balance of 35 MW Power Plant
Input in TPA Output in TPA
Char 2,72,000 Fly Ash 1,50,750
Non-coking coal 1,12,500 Bottom Ash 1,00,500
- - Flue gas 1,33,250
Total 3,84,500 Total 3,84,500
Energy Balance for 35 MW power plant
Char 31.5TPH@ 1800kcal/kg = 20.62 MW
Coal 13.02 TPH @ 3100 kcal/kg = 14.68 MW
Total = 35.20 MW
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Table 2.4 Sources and type of Pollution from the Proposed Project & mitigation
measure
Sl.
No
.
Section/
Unit Operation
Emission
released waste
generated
Types of
pollution
Mitigation
measures
1. Raw
Material
and scrap
Handling
Stock pile,
crushing,
screening,
material transfer &
charging etc.
Fugitive dust
emission
Air pollution, soil
& water pollution
Water sprinklers, Fully
covered conveying, dry
fog, suction swivel hood,
bag filter, green belt 7
storage of material on
concrete floor/under shed
2 Induction
Furnace
Melting of sponge
iron, pig and scrap
Fume and slag Air pollution &
soil pollution
Bag filter, high stack, iron
recovery & slag disposal
3 MBF Reduction of iron
ore/ sinter by coke
at 16000C
CO, CO2& Nox; BF
slag & sludge. Hot
water from
granulation of slag
Air pollution.
Thermal & soil
pollution
Slag granulation. Sludge
and slag use in sinter
making & sale to cement
plant, ventury scrubber,
burning of excess BF gas
to generate power
4 EAF Quality steel
production using
HM from MBF,
scrap & DRI
Fume and slag Air pollution &
soil pollution
Bag filter, stack, iron
recovery from slag and
slag disposal
5 Sinter plant Agglomeration of
sized iron ore fines
by fusion at
12000C
Particulate matter,
CO2& NOx
Air pollution, ESP and high stack
6 CCM Casting
continuously
molten steel in
multi strand
casters
Spillage of hot
liquid metal and
contact with hot
water and mill
scale
Water pollution Settling tank, mill scale
recovery & recycle.
7 AFBC Production of
Steam for power
generation
Particulate matter,
CO2, SO2, NOx and
generation of fly
and bed ash
Air pollution Land
pollution, Noise
pollution & water
pollution
ESP, high stack, silencer
for steam venting, ETP
8 Non
recovery
Coke Oven
Production of coke
and Generation of
Steam for power
generation
Particulate matter,
SO2 & NOx
Air pollution,
thermal pollution
& Water pollution
Waste heat recovery from
COG, Dry quenching of red
hot coke to avoid water
pollution, heat recovery
from DQC
9 DRI kilns Production of
Sponge iron using,
Iron ore, coal &
lime stone
Particulate matter,
SO2 & NOx
Air pollution,
thermal pollution
Water pollution &
soil pollution
Dust settling chamber,
After burning chamber,
Waste Heat recovery &
ESP
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2.6 PROJECT DESCRIPTION, INCLUDING DRAWINGS SHOWING PROJECT
LAYOUT, COMPONENTS OF PROJECT ETC. SCHEMATIC REPRESENTATIONS OF
THE FEASIBILITY DRAWINGS WHICH GIVES INFORMATION IMPORTANT FOR
EIA PURPOSE.
2.6.1 LAND DETAILS
M/s BEL has in its possession of 161.87 ha of land on which existing plant is running and
proposed expansion facilities will be accommodated in the vacant spaces available on
this land. The entire land will be used for setting up plant facilities, rain water
harvesting, water & raw material storage, solid waste dumping yard and development of
green belt.
ToR-4 (vii) Land use break up of total land of the project site
(identified and acquired), government/private-agricultural, forest,
wasteland, waterbodies, settlements etc. shall be included (not
required for industrial area)
The project of M/s Bengal Energy Limited is located at Dauka, Tentulmuri, Dist-West
Medinipur, and West Bengal. It is the core zone and the project boundary or the battery
limit does not belong to part of any National Park, wild life sanctuary or Natural/
Biosphere reserve. It also does not contain any features of archaeological/ historical and
cultural/aesthetic importance.
Table 2.1 Land schedule of project site core zone
Land Type Area in ha
Industrial land 161.87
Forest Land 0
Water Logged land 0
Agricultural Land 0
The total land of 161.87 ha has been acquired by M/s BEL and is available for the project
and its expansion will be carried out on the vacant areas within the existing plant boundary. The detailed breakup of the land is given in the table below:
The entire land will be used for setting up plant facilities, rain water harvesting, raw water, product, raw and waste material storage and establishing green belt.
Table 2.1A Land utilisation of project site core zone
Sl. No. Different Units Area in ha.
1 Existing plant Facilities 14.97
2 Proposed plant Facilities 24.28
3 Raw Material Storage 13.00
4 Water storage Facility 5.20
5 Rain water harvesting 5.20
6 Solid Waste disposal area 12.21
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7 Internal roads & others 2.83
8 Green belt 53.41
9 Vacant Space available for further
expansion
30.77
Total 161.87
Gen. ToR-4(xi)Status of acquisition of land. If land is not complete
stage of the acquisition process and expected time of complete
possession of the land.
M/s Bengal Energy Limited has acquired entire land of 161.78ha. It has no forest, waste
land, water bodies nor settlements inside acquired land. Existing coke oven Plant is
running on this land. Expansion facilities will be accommodated on vacant spaces of this
land.
Gen. ToR-4(xii)R & R details in respect of land in line with state
Government Policy.
Entire land has already been acquired and existing plant is operating on this land. No
settlement was there and so R&R has not been required.
2.6.2 PROJECT LAYOUT
The Project general layout showing existing and expansion facilities have been shown
below.
Gen. ToR 4(v) & Additional ToR 14 Layout map indicating existing as
well as proposed unit indicating storage area, plant area, green belt
area, utilities etc. If located within an Industrial
area/Estate/Complex, Layout of Industrial Area indicating location of
unit within the Industrial Area/Estate.
The raw material handling system for storage and supply of various raw materials has
been located near the consumer section. All the major users are connected to this
system by conveyors. All raw materials are proposed to be received in dump trucks and
unloaded in the raw material receiving yard. Sufficient space is earmarked to cater to the
needs of all the units of the plant.
All the plant facilities are laid out considering the need for optimized earthwork, rational
material flow, economy in operations and the space requirements for rational
development. The layout also takes into account the stage wise commissioning of the
individual units of the proposed project.
The plant layout has been made in such a manner so that the material flow from the
units will be smooth and convenient, considering the process flow chat.
The power plant has been located near waste gas source suitably considering the
location of the DR plants & coke oven from which the major fuel sources for power
generation will be available. Adequate space is provided in all the production blocks for
accommodation the immediate service facilities such as the sub-stations, water
recirculation, yard utilities etc.
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PROJECT LAYOUT MAP WITH PROJECT COMPONENTS
The general layout of the plant has been developed with requisite provision for
landscaping and greenbelts with a view to avoid adverse impact on the environment.
33% of total land is earmarked for this purpose. Existing facilities have been shown in
blue colour and proposed facilities in pink.
2.6.3 RAW MATERIAL INVENTORY
The major raw material for Coke oven Plant, Integrated Steel Plant and AFBC Boilers will
be as follows:
Gen.ToR 3(iv) List of Raw materials required and their source along
with mode of transportation.
Material Gross Capacity in
TPA
Source Mode of Transport
Coking Coal 16,80,000 Imported Ship/Rail/Road
Non-Coking Coal 17,96,780 Talcher Rail
Iron Ore 19,98,800 Barbil, Banspani Rail
Iron Ore fines 7,68,000 Barbil, Banspani Rail
Dolomite 1,36,000 Biramitrapur Rail/Road
Lime stone 1,39,000 Biramitrapur Rail/Road
Transportation of Raw material as well as products will be done only by Environmental
compliant Bharat/Euro III vehicles. Mater to be transported fully covered to avoid
spillage on Roads. Materials will be transported to the site through the existing railway
siding.
Sp ToR(vii) Project proponent shall identify railway siding points to be
used frequentl.
The company has developed its own railway siding for transporation of raw materials and
products. Permission exists for siding at Benapur Station on Kharagpur-Balasore-
Bhadrak Section of South Eastern Railway. The permission letter has been attached as
Annexure II
Specific ToR (ix) Plan for concreted floor with covered storage
(sheds) of Raw material and coal shall be provided in the EIA EMP
report.
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Raw material will be partly indigenous and partly imported, but all of them might have
various trace elements harmful to animal of plant health, when leached by rain water
and finally mixed with surface or ground water.
Dolchar is a byproduct of DRI kilns but it is considered as Raw material for AFBC.
All the Raw materials to be stored under shed and over concrete floor.
Additional ToR 11 Trace metals Mercury, Arsenic, and fluoride
emissions in the raw material
M/s Bengal energy is proposing to get imported coal as raw material for its project.
Hence average value of trace elements has been taken into consideration, which are as
follows.
Average range & Average values for trace elements in international coal
Element Average range mg/kg Average, mg/kg
As 0.36-9.8 2.69
B 11-123 47
Be 0.1-2.0 1.0
Cd 0.01-0.19 0.093
Hg 0.03-0.19 0.091
Pb 1.1-22 7.0
Se 0.15-5.0 2.15
Cr 2.9-34 17.6
Cu 1.8-20 10.8
Ni 1.5-21 11.1
Zn 5.1-18 12.7
Source: (Creelman, 2002)
Toxicity of trace elements
Cd has no known biological function. It accumulates in the kidneys and liver. It is
carcinogenic and can cause emphysema and fibrosis of the lung
Cr is also carcinogenic. It accumulates in the liver and spleen. Cr exists in the non-toxic
form Cr (III) and tends to be absorbed onto clays, sediments and organic matter. It is
therefore not very mobile in the environment. Cr(VI) is more mobile and more toxic
Exposure to Hg causes neural and renal damage, and cardiovascular disease. Organo-
mercury compounds bio-accumulate, particularly in fish.
Pb causes anaemia and has cardiovascular, neurological and gastrointestinal effects.
Some compounds are animal and possibly human carcinogens.
Although Se is an essential element, the safe range is narrow. Elevated levels cause
gastrointestinal disturbance, liver and spleen damage, and anaemia.
B-rich soils can limit plant growth resulting in decreased crop yields. Limits have been
adopted on the permissible levels of B in wastewater and water for irrigation.
Mitigation measure of toxic trace elements
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Boiling Points of Hg, As, Se, Cd and Pb are 356.70C, 6130C, 684.80C, 766.80C & 17490C
respectively. In coal fired system of power plants or DRI Kilns temperature remains
above BP of these elements except Pb.
For a typical coal combustion plant the most important gaseous species are As asAsO,
As4O6, and As2O5, Cd as elemental Cd and CdO, Hg as elemental Hg, Pb as PbO, Sb as
SbO, Se as SeO2, and Zn as element Zn. Co, Cu, Ni and some of the Cr are not
volatilised and found in PM2.5 fly ash particles as ferrite spinels
Source :Zevenhoven and Kilpinen (2001)
Class 1: Elements that are approximately equally concentrated in the fly ash and bottom
ash, or show little or no small particle enrichment. Examples include manganese (Mn),
beryllium (Be), cobalt (Co), and chromium (Cr)
Class 2: Elements that are enriched in the fly ash relative to bottom ash, or show
increasing enrichment with decreasing particle size. Examples include arsenic (As),
cadmium, (Cd) lead (Pb), and antimony (Sb)
Class 3: elements which are emitted in the gas phase (primarily mercury (Hg) and, in
some cases, selenium (Se)).
Trace elements when vaporised, deposit on surface of finest ash particle at reduced
temperature and get separated in ESPs Or Bagfllters. These are then used in making
bricks or cement and get fixed with them and does not affect the environment.
Gen. ToR 3(v) other chemicals and materials required with quantities
and storage capacity.
In addition to above stated major Raw material following materials will also be required.
Sl No Item Description Unit Quantity Per Annum
1 DM plant resins KG 342
2 Hydrochloric acid KL 178
3 Caustic soda KG 287
4 Lubricants KG 3,112
5 LDO/HSD LTR 10,015
LDO & HSD are coming under Petroleum Class B. No license needed for transport or
storage of Petroleum Class ‘B’ (Non-Bulk) in quantity not exceeding 2500 ltrs. And in
container not exceeding 1000 ltrs.
Additional ToR 17 Details on environmentally sound technologies for
recycling of hazardous materials as per CPCB guidelines may be
mentioned in case of handling scrap and other recycled materials.
The project will use heavy building scrap materials so as to avoid generation of dioxins
and furans from residual paints of scrap. The hazardous materials like used oil, oily
cotton waste, used lead cells, spent resins are generated from the process will be sold
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to authorized recyclers.BF dust & sludge contains toxic trace elements along with C & Fe
so it will be used up in Sinter which otherwise could have affected environment.
3(viii) The project proponent shall furnish the requisite documents
from the contract authority in support of drawl of ground water and
surface water and supply of electricity.
2.6.4 WATER REQUIREMENT
3(vii) Requirement of water, power,with source of water, status of
approval,water balance diagram, manpower requirement
Additional ToR 18 Details on requirement of energy and water along
with its source and authorization from the concerned department.
Location of water intake and outfall points(with co-ordinates)
Water will be required to control temperature rise in various process. There will be
circulating water in close or open circuit. Non-contaminated water will be reused in the
process after cooling. Contaminated water will be settled, treated, filtered and reused
and there by fresh water requirement will be reduced. Loss of water as non-recoverable
waste water and through evaporation are to be made up to circulating circuit as fresh
make up water.
Table 2.3 Water Requirement
Sl. No Facilities Make up water
requirement
Cum/day
1 4 X 500TPD, 4 X 350 TPD, DRI plant 255
2 Captive power plant 205 MW 6,150
3 Blast Furnace 2,300
4 Coke Oven Batteries 108
5 EAF & IF (1 MTPA) 2,200
6 Sinter Plant 1x60m2 1,125
7 Water for drinking & Sanitation purpose(domestic) 200
8 Compensation for losses in soft water circuit 100
9 Contingency requirement 100
9 Total Make up water 12,538
10 Losses at plant water balancing , reservoir & raw
material plant
627
Total Raw water requirement from river 13,165
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Although fresh make up water requirement will be about 12,538m3/day to meet losses
during transportation and storage, and provision for contingency taken into consideration
water drawl from river will be 13,165m3/day.
The probable source of supply of raw water for the project shall be Kangsabati river.
Water intake facilities at source and conveying main shall be provided for ensuring raw
water supply to plant on a continuous basis. The capacity of plant water balancing
reservoir, catering to plant make –up water needs, is considered to provide for a
contingent storage of seven days. This capacity is arrived at on the assumption that raw
water supply to plant shall be made possible on a continuous basis.
2.6.4.1 Water management &balance diagram
Fig 2.6 Water Balance Diagram
Specific ToR(viii) The plant shall be to zero liquid discharge
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Waste water generated from various units will be about 6,387 m3/day and domestic
waste water will be about 270 m3/day. This will be treated in Neutralization tank, filtered
through sand/gravel bed and will be used for toilet flushing, dust suppression, road and
vehicle washing and green belt.
There will be Zero discharge outside project boundary.
2.6.4.2 Location of water intake and outfall points (with co-
ordinates)
Water for the project of M/s BEL will be sourced from river Kangsabati. Two intake wells
at the river, one at Jinsar 220 23’ 34.42” N and 870 21’ 49.32” E and other at Uttershimla
220 23’ 19.30” N and 870 23’ 05.03” E has been set up. Transportation of water from
river to project site will cover a pipe length of 23.7km and cross canal, NH-6, Howrah-
Kharagpur Rly. Line and pass along the length of NH-60, and outfall at 220 14’ 45.48” N
and 870 23’ 23.08” E. Permission has already been from Government of west Bengal, SE
Rly etc. This water project is to supply 10 MGD i.e. 40,920 m3/day and part of job has
already been completed.
Permission exists for drawl of 14,400 m3/day of water from Kangsabati River.The water
permission letter is attached as annexure III
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2.6.5 POWER REQUIREMENT& GENERATION
The requirement of power for project will vary with stages of development. Even after
the commissioning of the captive powers, grid support will be required.
Construction power would be taken from available 132KVA/220KVA line for which
discussion is under progress with WSEB. Construction power required for the proposed
plant will be about 500kVA.
Power requirement for the project after expansion are estimated as follows:
Unit Power requirement in
MW(approx.)
1,2 MTPA Coke oven 03.00
4x500 TPD & 4x350 TPD DRI Kilns 12.00
2x320m3 MBF 11.00
1x60m2 Sinter Plant 05.50
2x80T EAF with LF& CCM 64.00
3x20T IF with LF 21.00
ASU 02.00
Lighting & domestic use 01.50
A/c& ventilation, Air compressor, Water
Pumping system etc.
12.50
Power Plant internal consumption 20.50
Total 153.00
Air conditioning
Package air conditioning units will be provided for the following areas.
1. Coal handling control room
2. Ash handling control room
3. ESP control room
4. DM Plant control room
5. Switchyard control room
6. Administration Building
Split air conditioning units will be provided for the following areas:
1. Conference room
2. Laboratory
Ventilation system
The ventilation system envisaged for the plant will achieve the following.
Scavenging out structural heat gain and heat load from various equipment, hot
pipes, lighting etc.
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Reduction of air pollution due to generation of obnoxious gases / aerosol
contaminants like acid fumes, dusts etc.
Following areas are proposed for ventilation
Turbine building
Coal mill building
ESP building (equipment room)
Air compressor room
AC plant room
DM plant MCC room
Raw water pump house
Clarified water and fire water pump house
CW pump house
Chlorination Room
Miscellaneous rooms in powerhouse building like cable spreader room,
electrical switchgear room, battery room, toilet, elevator machine
room etc.
Battery room in Switchyard
DG set building
Workshop
Captive Power generation
Source Power generation in MW
WHRB of Coke Oven gas 80
WHRB of DRI Kilns 90
AFBC utilizing dolchar 24.5
CDQ & TRT system 10.5
Total 205
Generation 205 MW
Consumption 153 MW
Surplus Power 52 MW
About 8.0 MW power will be generated from dry coke quenching system & 2.5 MW power
will be generated from TRT of Blast furnace; totaling 10.5 MW, hence AFBC generation
will be reduced by same amount, so that pollution load will be reduced.
There will be Infrastructure to draw power from grid during construction period; same
infrastructure will be utilized for supply of balance power to state grid.
Specific ToR (x) Project proponent shall plan for solar light system for
all common areas, street lights, villages, parking around the project
area.
Specific ToR (xi) Project proponent plan for LED lights in their offices
and residential areas.
Following power saving measures shall be taken up for the project.
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1) LED lights in control room and working area
2) Solar light system for internal roads, street lights, village lighting etc
3) Variable Frequency drive for ID fans and blowers.
4) Capacitor back to improve power factor.
5) MBF top gas pressure recovery turbine to be set up to generate atleast 35
KW/ton of hot metal produced
Emergency DG Set
No. 2000 kVA emergency DG set will be provided to cater the loads during emergency
conditions. The DG set will be sized considering the essential loads like steam turbine
lube oil system, generator seal oil systems, Air pre-heaters, turning gear motor, jacking
oil pumps, lifts, battery chargers, emergency AC lighting, etc. during any emergency
condition. The DG Set will be started automatically in case of failure of AC Power. Manual
starting facility from Central Control Room will also be provided in addition to automatic
starting.
2.6.6 SOLID WASTE GENERATION
Specific ToR(xii)& Additional ToR 8 Proponent shall submit plan for
solid waste management. Plan for slag utilization.
Additional ToR 12 Trace metals in waste material especially slag .
Additional ToR 19 Details on toxic metal content in the waste material
and its composition and end use (particularly slag).
Additional ToR 20 Details on toxic content( TCLP), composition and
end use of slag.
Total solid waste generation and its management has been given in table 2.4
below
Table 2.4 Solid Waste Generation
Solid waste Quantity
in TPA
Utilisation measures
EAF & IF slag 1,20,000 Use in construction work
IF & EAF flue dust 24.000 Will be used in making sinter for use in BF
DRI Dolchar 2,72,000 Use in AFBC to generate steam for power
generation
Power plant Fly ash 1,50,750 Sold to Gava Ecocrete Pvt Ltd
DRI ash & dust 5,75,600 Land feel and dump in abandoned coal mines
for which permission to be sought
BF slag 1,84,760 To be used in sinter plant & balance to be Sold
to ASO Cement Ltd as per MOU 20.09.2018
BF sludge + dust 2,93,670 To be used in sinter plant & balance to be Sold
to ASO Cement Ltd as per MOU 29.09.2018
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Power plant Bottom
Ash
1,00,500 Sold to Gava Ecocrete Pvt Ltd, MOU 30th August,
2018
Composition of BF dust/Sludge
Component Concentration in BF dust/sludge in % (w/w)
C 24–40
Fe 15–40
Ca 1.4–5.7
Zn 0.1–0.5
Pb 0.02–0.07
Na 0.02–0.47
K 0.20–0.80
S total 0.20–1.3
BF slag & dust contains C & Fe in substantial amount it will be used in sinter making and
used as raw material in MBF. Flue dust from IFs & EAF will also be used in sinter making.
Composition of EAF & IF Slag
Similarly IF and EAF slag only contains Fe and Silica. Fe is recovered by magnetic
separation and is used as substitute of slag
So, TCLP test is not envisaged as toxic trace elements are not present.
Hazardous waste management
Hazardous waste generated from the project are Resins from DMplant, spent oils which
are to be handed over to authorized dealers/suppliers.
2.6.7 MANPOWER REQUIREMENT
Based on the unit operations & services, it is estimated that the total requirement of
manpower for the facilities proposed will be about 1,355 persons and a summary of
manpower is given below:-
Table 2.5 Summary Of Manpower Requirement
Department
/ Section
Shifts Total per
week
day
Total on
Pay Roll General I II III
Coke Oven
Plant
20 60 60 60 200 230
Sponge Iron
Plant
15 100 100 100 315 325
BF 10 30 30 30 70 75
EAF & IF 10 75 75 75 235 250
Captive Power
Plant
15 50 50 50 165 175
Sinter Plant 5 20 20 20 65 70
Maintenance,
Adminstration,
30 40 40 40 170 175
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marketing of
product &
procurement
of Raw
material
Quality
Assurance and
Lab
5 15 15 15 50 55
Total 110 390 390 390 1280 1355
Table 2.6 Category-wise break-down of manpower
Category Total
Management personnel 65
Technical specialist 150
Supervisory staff 185
Highly skilled staff 225
Skilled 535
Semi-skilled staff 167
Office staff 28
Total 1,355
Gen. ToR 3(i) Cost of Project and time of completion
2.6.8 TOTAL CAPITAL COST
The total capital cost include cost of plant & machinery, Pre-operative expenses and
others.
Table 2.7 Total capital cost of Project
Units Cost in Rs.
Crore
Land & Site development 40.00
Infrastructure development 200.00
Civil and structural steel work 1,000.00
Mechanical & electrical equipment (as erected) 2,481.90
CER activities as per PH issues 18.10
Design, engineering & consultancy 160.00
Plant cost 3,900.00
A Plant Cost 3,900.00
B Other fixed Investment
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Preliminary expenses: 58.50
Preoperative expenses 39.00
Sub total (B) 97.50
C Contingency: 195.00
D Interest during construction 250.00
E Margin money for working capital: 500.00
Total Capital Cost: A+B+C+D+E = 4942.50 ~4943.00 Crores
Capital Cost , Rupees - Crores 4,943.00
Equity 1,482.90
Borrowing 3,460.10
2.6.9 PROJECT COMPLETION TIME
Estimated time of implementation of the project is 36 months, the breakup of time
schedule is as follows:
Railway siding construction work will take approximately 12 months. It is envisaged that
certified equipment data required for design of equipment foundations will be made
available by equipment suppliers within the shortest possible time form the date of
placement of firm orders on them.
The total duration of structural steel work is estimated at 10 to 30 months
Equipment manufacture and delivery
Manufacturing and delivery of major equipment for proposed plants is to be made
available within a period from ‘Placement of Order’ date as follows:
IF and EAF: 15 months
DRI: 15 months
CPP: 18 months
BF: 12 months
SP: 12 months
Erection of equipment for the plant facilities will commence after availability of civil &
structural fronts as well as receipt of equipment at site to match the sequence of
erection
Erection of equipment is to be completed by 9 and 10 months from the
commencement of erection work for coke oven.
Erection of equipment for captive power plant is to be completed by 8
to 10 months from the commencement of erection work for CPP.
Erection of equipment is to be completed by 9 and 10 months from the
commencement of erection work for DRI kilns 1 to 4 respectively
Erection of equipment is to be completed by 9 and 10 months from the
commencement of erection work for DRI kilns 5 to 8 respectively
Erection of equipment is to be completed by 7 - 9 months from the
commencement of erection work for Blast Furnace.
Erection of equipment is to be completed by 7-9 months from the
commencement of erection work for Sinter Plant
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Erection of equipment is to be complete by 11 months from the
commencement of erection work for steel melt shop.
Trial run and commissioning
After completion of erection of equipment for plants, commissioning activities will be
taken up sequentially. This will consist of cold run; hot run and performance guarantee
tests. Commercial production will commence after completion of all performance tests.
Test, trial run and commissioning of different plants are scheduled for completions from
“Placement of Order” are given here-under:
Power Plant: 21 months
DRI Plant: 18 months
Blast Furnace: 12 months
Sinter Plant: 12 months
IF and EAF: 12 months
2.7 DESCRIPTION OF MITIGATION MEASURES INCORPORATED INTO THE
PROJECT TO MEET ENVIRONMENTAL STANDARDS, ENVIRONMENTAL
OPERATING CONDITIONS OR OTHER EIA REQUIREMENTS (AS PER REQUIRED
SCOPE)
Following pollution mitigation measures have been proposed to be incorporated into the
project to meet environmental standard of air, water, noise and soil.
Air
a) DSC, ABC, ESPs with ID fans and high stack for DRI Kilns
b) ESP & high stack for Sinter plant & power plant
c) Bag Filters with ID fans and high stacks for: 1) IFs
2) EAFs
3) Raw material Handling Plant
d) Dust catchers with Ventury Water scrubbers: MBFs
e) Green belt covering entire boundary line as dust sink for the project
f) WHRB for DRI kilns and Coke oven plant to avoid thermal pollution of air.
Water
a)Domestic water treatment STP
b) Industrial water treatment ETP
c) Recycle/Reuse of treated water and Zero waste water discharge out side project
boundary.
d) Dry quenching of red hot coke to avoid waste water generation
Noise
a) Procurement of low noise making, silent type machinery for installation
b) Acoustic enclouser for sound producing machines
c) Green belt development surrounding project area
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d) Providing ear guards to working personnel and air tight control rooms.
Soil
a) Storing of Raw material and solid waste on impervious floor and under shed.
b) Utilisation/disposal soon as possible
c) Avoiding use of polythene. M/s BEL is a polythene free industry.
Detail mitigation measures have been given in Ch-4
2.8 ASSESSMENT OF NEW & UNTESTED TECHNOLOGY FOR THE RISK OF
TECHNOLOGICAL FAILURE.
M/s Bengal Energy Limited has proposed steel production through well proven DRI-MBF-
EAF/IF technology. No untested or new technology has been proposed.
CONCLUSION
This chapter has given an elaborated description about the type, need, location
environmental sensitivity, magnitude of the project and technology, process description,
along with requirement of raw material, water, power, manpower etc.
Being a red category polluting industry, it is likely to have environmental impacts on the
local ecology (Air, Water, Noise, Soil, Vegetation, animal & Human being). Therefore
there is need for present base line study of project area, which will be influenced due to
emissions & effluents from project.
Socio economy, geology, hydrogeology, flora & fauna of the area surrounding project
need to be studied which may be affected due to the project this will also help in
quantifying the impact caused due to the expansion project. In order to ascertain the
impact of proposed project on the environment it is essential to study the baseline
environment of the surrounding area. In the forth coming chapter the baseline study has
been carried out.
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CHAPTER-3
DESCRIPTION OF EXISTING ENVIRONMENT
3.0 INTRODUCTION
This chapter describes the existing environmental baseline status of M/s Bengal Energy
Ltd. at Dauka, PO- Tentulimuri, P.S-Naraingarh, in the district of Paschim Medinipur, WB
and its surrounding areas. It includes the physical environment (comprising
meteorology, air, water and land components), biological components and socio-
economiy, which may get affected due to the expansion of M/s Bengal Energy Ltd, as an
integrated steel plant.
“Environment “in EIA context mainly focuses on , but not limited to physical, chemical,
biological, geological, social, economic and aesthetic dimensions along with their
complex interactions which affects individuals, communities and ultimately determines
their forms, character, relationship and survival.
The major purposes of describing the environmental settings of the study area are:
To understand the project need and environmental characteristics of the area.
To assess the existing environmental quality.
To identify environmentally significant factors or sensitive geographical and
biological locations.
3.1 STUDY AREA, PERIOD & COMPONENTS
M/s Bengal Energy Ltd has its existing Coke oven and power Plant at Dauka, Tentulmuri
in Paschim Medinipur district of West Bengal. The project site extends from 220 15’
22.03’’ N to 220 14’ 26.31’’ N and 870 22’ 53.38’’ E to 870 23’ 10.63’’ N with Average
altitude of 32 m
3.1.1 STUDY AREA
The study area comprises three parts for the generation of baseline data collection:
Core zone – The plant site where the proposed expansion will be under taken.
Buffer zone- It consist of 10 km aerial coverage around the core zone.
Environmental Sensitive zone- it extends up to 15 km aerial coverage around the
project site.
The brief description of the present environmental scenario obtained from primary
(monitored) data and partly from the secondary source (Govt. offices) the description
covers the major environmental components like.
1) Physio-chemical (air, water, soil, noise etc.),
2) Biological (flora, fauna & ecology),
3) Human (Socio-economic) &
4) Aesthetics
3.1.2 STUDY PERIOD
Base line study period of core and buffer zone of project site was winter, from 1st
November, 2017 to 31st January 2018.
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3.1.3 COMPONENTS
SITE DESCRIPTIONS
The location of the site in the Indian Map of 1: 10, 00, 000 scale followed by 1: 50, 000
for the preparation of 10 Kilometers of terrain features with 100/200 meter contour to
generate the 3 dimensional view of the project site all these explain physio-geographical
condition of the study area.
SITE CONNECTIVITY
The location is well connected by road and Rail. NH-16 connecting to Balasore–
Kharagpur is only 0.6 Km away from the project site & Balasore-Kharagpur railway line
is passing only at 0.5 Km away from the site. River Kangsabati is flowing 15 Km away
from the location
Fig 3.1 Location of Site
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3.2 PHOTOGRAPHS OF PROJECT SITE
Gen.ToR 4(vi) Photographs of the proposed and existing (if
applicable) plant site. If existing, show photographs of
plantation/green belt in particular.
Some photographs of the project site showing existing plant & vacant space for
expansion.
3.3 TOPOGRAPHY
The land surface of the area is characterised by hard rock uplands, lateritic covered area,
and flat alluvial and deltaic plains. Extremely rugged topography is seen in the western
part of the area and rolling topography is experienced consisting of lateritic covered
area. These rolling plains gradually merge into flat alluvial and deltaic plains to the east
and south east. The soil is fairly fertile. Kangsabati, Silabati, Subarnarekha, Keleghai and
their tributaries are the main rivers of the area.
The soil is fertile alluvial and the area is flat. To the west, the Chota Nagpur
Plateau gradually slopes down creating an undulating area with infertile laterite rocks/
soil. The landscape changes from dense dry deciduous forests in the west to marshy
wetlands in the east.
The alluvial portion may be further subdivided into two divisions. First, it is a strip of
purely deltaic country nearer to the Hooghly and the Rupnarayan, intersected by
numerous rivers and watercourses subject to tidal influences.
3.3.1 LAND USE PATTERN OF BUFFER ZONE
Tor 5 (ii) Land Use Map Based on High Resolution Satellite Imagery
LAND USE PATTERN OF 10KM BUFFER ZONE OF PROJECT SITE
LAND USE
Area
(Sq. km)
Area (%)
Canal 1.49 0.4
Crop land 243.91 66.0
Dense forest 11.58 3.1
Groves 0.23 -
Industry 2.70 0.7
Institution 5.56 1.5
Open forest 6.96 1.9
Plantation 3.96 1.0
Quary 0.14 -
Railway 1.10 0.3
Reservoir 0.27 -
River 1.51 0.4
Road 4.37 1.2
Scrub forest 5.57 1.5
Scrub land 3.11 0.8
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Settlement 61.07 16.5
Tank 10.00 2.7
Urban area 6.66 1.8
Total 370.19 100
Out of the total study area, major portion is agricultural land which covers 66%,
Settlement contributes 16.5% and forests land 4.6%. So, agricultural products become
the main source of income of the local people.
The study area can be classified as given below;
Crop Land (243.91 Sq Km) : The major portion of the study area is covered by crop
land, the major crop grown is Paddy and is grown throughout the year. The area is not
well connected with canal irrigation system mostly deep borewell is dended for irrigation
purpose.
Farmers to be encouraged for adopting farming of crops by using modern techniques,
dairy farming to meet the need of the industrial population.
Forest (28.3 Sq Km): Total forest area is fairly well. The scrub land present can be
converted to plantation purpose which may increase the forest cover.
Industry (0.27 Sq Km.) : Industry is negligible in the study area.
River & Canals (3.0 Sq Km.) River Kanshabati is the main river flowing beside the
study area. Canal irrigation system needs to be increased looking into the crop land and
fertility of the soil in this area.
Tank & Resirvoir (10.27Sq km): Both are considered as wetlands are a good sign of
ecological importance, but the pollution parameters are to be checked regularly.
The major land use pattern is crop land, it means majority of the people depends on
agriculture. Settlement is in 61.07 sq.km area. Forest land covers around 10% of total
land. Average Rain fall in the area is 1400 mm and there is potentiality of good crop.
Industry covers only 2.3% of 10km radius study area.
Tor 4(viii) List of Industries with name and type within study area
Sl.
No. Name of Industry
Type Distance
in km
Direction
w.r.t
project
1
Essen Fabricators Pvt Ltd (Heavy
Engineering Division)
Steel foundary 9.17 NW
2 Supreme Industries Ltd
Plastic
Manufacturing
7.13 S
Tor 5(i) Permission and approval for use of Forest Land if any and
recommendation of the status forest deparment (if applicable)
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The project area does not have any forest land. The entire land has been has been
converted to Industrial land. Hence forest clearance is not applicable.
Tor-5(iii) Status of application submitted for obtaining the stage I
forestry clearance along with latest status shall be submitted.
The proposed project does not have forest land and the expansion is intended to be
carried out within the existing premises. So, stage I forest clearance is not applicable.
Tor-5(iv) The Projects To Be Located Within 10km Of The National
Parks, Sanctuaries, Biosphere Reserves, Migratory Corridors Of Wild
Animals The Project Proponent Shall Submit The Map Duly
Authenticated By Chief Wildlife Warden Showing These Features Vis-
À-Vis The Project Location And The Recommendations Or Comments Of
The Chief Wildlife Warden-Theoren.
There is no such National Parks, Sanctuaries, Biosphere Reserves, Migratory Corridors of
Wild Animals within the 10 Km radius of the project. So, map duly authenticated by
Chief Wildlife Warden is not envisaged.
Tor-5(v) Wildlife Conservation Plan Duly Authenticated By The Chief
Wildlife Warden Of The State Government For Conservation Of
Schedule I Fauna , If Any Exists In The Study Area
Not applicable
Tor-5(vi) Copy Of Application Submitted For Clearance Under The
Wildlife (Protection) Act, 1972 To The Standing Committee Of The
National Board For Wildlife
Not Applicable
Additional ToR 3 For large ISPs s 3-D view i.e DEM(Digital Elevation
Model) for the area in 10 km radius from the proposal site.
3-D view i.e DEM (Digital Elevation Model) of buffer zone of 10km radius has been given
below.
The digital elevation map of the study area depicts that the high elevation is 61.1m in
the North West region of the area and 10.5m in South West and eastern part. It shows
there is a slope gradient towards SW from NW.
3.4 ESTABLISHMENT OF BASELINE FOR VALUED ENVIRONMENTAL
COMPONENTS AS IDENTIFIED IN THE SCOPE WITH METHODOLOGY ADOPTED.
BASE MAP OF ALL ENVIRONMENTAL COMPONENTS.
To quantify and interpret the additional impacts due to air emissions, effluent discharge,
solid waste dumping and noise propagation due to expansion of Steel plant at a later
date, it is necessary to know the present quality of environment with respect to various
attributes considered under impact identification. The environmental factors include air,
water, noise, soil, land use, flora & fauna, socio-economic and demographic pattern in
order to understand the base line environment quality a monitoring schedule covering
Post-Monsoon season of the year was carried out from the month of November 2017 to
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January 2018.The impact identification started with collection of baseline data such as
ambient air quality, quality of ground water, surface water, soil, noise and
meteorological parameters like temperature, humidity, wind speed and direction, cloud
cover etc. The field studies/ site survey/ interaction with different government agencies
was carried out to collect data/ information pertaining to flora & fauna, climate, socio-
economic and demographic factors, land use pattern, forests, geology, geomorphology,
hydrology, hydro-geology, soil and agriculture, mineral resources etc. This chapter
describes the existing baseline environmental condition in of the 10km radius area of M/s
Bengal Energy Ltd. Project site study area.
3.5 BASELINE STATUS OF STUDY AREA
3.5.1 CLIMATIC CONDITIONS OF THE STUDY AREA
The climate in the study region is generally hot and humid and is characterized with
seasonal variations of temperature, humidity, rainfall etc. The year is mostly divided into
following season.
Sl. no. Season Month
1 Winter December to February
2 Summer March to May
3 South west
Monsoon
June to September
4 Post Monsoon October and November
The climate setting of the area has been arrived by generation of primary data to
ascertain the values and validating with the existing secondary data from the nearest
IMD station at Midnapore.
Temperature
The temperature profile of this region is presented in the following table.
Table-3.2: Temperature Profile of the study area
Sl.
No.
Description Minimum
Temperature (0C)
Maximum
Temperature (0C)
1 Summer Season 24.0 41.0
2 Winter Season 14.0 30.0
3 Monsoon season 22.0 38.0
Humidity
The maximum and minimum humidity values of the region are given below.
Table-3.3: Maximum and Minimum Humidity of the Study Area
Maximum humidity 66%
Minimum humidity 53%
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Rainfall
The area receives fairly good amount of rainfall from the southwest monsoon during
June to September. Light showers occur during the months of October and November.
The average annual rainfall of the study area is 1440 mm. The rainfall characteristics of
the region are given in the following Table-3.4.
Table-3.4: Rainfall Pattern in the Region
Predominant rainy season (monsoon) July to September
Average annual rainfall (mm) 1440
Most rainy Month July, August
Soil
The soils of the study area are mainly red earth comprising loamy sands, sandy loams
and clay loams. The soils of Paschim Medinipur district are predominantly red laterite
and alluvial.
3.5.2 METEOROLOGICAL CONDITIONS DURING STUDY PERIOD.
Meteorology of the study area plays an important role in air pollution dispersion. The
prevailing micro-meteorological conditions at the site regulate the dispersion and the
dilution of air pollutants in the atmosphere. The predominant wind speed at the core
zone will decide the direction and the distance of the most affected area from the
proposed activity. Regional meteorological scenario helps to understand the trends of the
climatic factors. It also helps in determining the sampling stations in predicting the post
project environmental scenario. Meteorological perameters exerts a critical influence on
Air Quality as the pollution arises from the interaction of atmospheric contaminants with
adverse meteorological conditions such as temperature inversions, atmospheric stability
and topographical features like hills, canyons and valleysplays a major role.
The critical weather elements that influence air pollution are wind speed, wind direction,
temperature, which together determines the atmospheric stability.Hence it is an
indispensable part of any Air Pollution Studies and required for interpretation of baseline
information.
Monitoring Period
Meteorological data was collected for the study period of three months (November 2017
to January 2018). The data collected during the monitoring period represents the winter
season.
In order to determine the micrometeorological conditions of the study area a temporary
micro-meteorological monitoring observatory was set up near the site. The following
parameters were recorded at hourly intervals continually during the study period.
Wind speed
Wind direction
Relative humidity
Temperature
Cloud cover
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Wind speed and direction are measured by anemometer; air temperature by
thermometer, relative humidity is measured by hygrometer and cloud cover recorded
through visual interpretation. The localized data generated in the study area have been
compared with the data compiled from the nearest IMD observatory at Midnapore. At the
meteorological station wind speed & direction, temperature, relative humidity and cloud
cover were recorded at hourly intervals throughout the monitoring period. Total rainfall
for the entire monitoring period was also recorded. The summarized meteorological data
is given in Table-3.5.
Wind roses on eight-sector basis (N, NE, E, SE, S, SW, W, NW) have been drawn for 00-
24 hours. From the analysis of data the overall predominant wind direction has been
from North to South followed by North-East to South-West. The average wind velocity is
3.72 m/s and the calm period is 34.83%. Details of the overall wind frequency
distribution during the study period at the site is given in Table 3.5. The Wind Rose
diagrams for winter season are given as Fig-3.2, Fig-3.3, Fig-3.4 , Fig-3.5 and Fig-
3.6.
Table-3.5: Summarized Meteorological Data at site.
Temperature
The mean maximum and the mean minimum temperatures recorded during the study
period are 10.0ºC and 33.0ºC respectively. The relative humidity varied between 55% to
66% during the study period.
Rainfall
No rainfall was recorded during the study period and there was clear sky.
Station ID: 42803 Run ID: Dauka
Year: 2017-2018
Date Range: November 1st. - January 31st.
Time Range: 00:00-23:00
Table-No. 3.6: Overall Wind Frequency Distribution
Period
Wind Speed
(Km/Hr)
Temperature
(oC)
Relative
Humidity (%) Rainfall Cloud
cover
(Oktas)
Mean Max Min Avg Max Min Avg Max Min Avg
24 hr
Max
(mm)
Total
(mm)
Nov.-
2017
12.8 0.3 3.1 32 14 15 66 62 63 Nil Nil 0
Dec.-
2017
12.7 0.4 3.0 30 11 12 65 56 61 Nil Nil 1
Jan.-
2018
12.9 0.3 2.9 33 12 10 63 55 60 Nil Nil 0
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Wind Direction 0.5 - 2.1 2.1 - 3.6 3.6 - 5.7 5.7 - 8.8 8.8 - 11.1 >= 11.1 Total
348.75 - 11.25 0.195592 0.028581 0.000000 0.000000 0.000000 0.000000 0.224174
11.25 - 33.75 0.000344 0.000000 0.000000 0.000000 0.000000 0.000000 0.000344
33.75- 56.25 0.153926 0.012741 0.000000 0.000000 0.000000 0.000000 0.166667
56.25-78.75 0.016529 0.000000 0.000000 0.000000 0.000000 0.000000 0.016529
78.75-101.25 0.051309 0.006543 0.000000 0.000000 0.000000 0.000000 0.057851
101.25-123.75 0.008953 0.000689 0.000000 0.000000 0.000000 0.000000 0.009642
123.75-146.25 0.025482 0.002755 0.000000 0.000000 0.000000 0.000000 0.028237
146.25-168.75 0.024449 0.003444 0.000000 0.000000 0.000000 0.000000 0.027893
168.75-191.25 0.023760 0.005510 0.000000 0.000000 0.000000 0.000000 0.029270
191.25-213.75 0.003788 0.000000 0.000000 0.000000 0.000000 0.000000 0.003788
213.75-236.25 0.039945 0.002755 0.000000 0.000000 0.000000 0.000000 0.042700
236.25-258.75 0.006198 0.000344 0.000000 0.000000 0.000000 0.000000 0.006543
258.75-281.25 0.010675 0.002066 0.000000 0.000000 0.000000 0.000000 0.012741
281.25-303.75 0.002410 0.000689 0.000000 0.000000 0.000000 0.000000 0.003099
303.75-326.25 0.017906 0.000689 0.000000 0.000000 0.000000 0.000000 0.018595
326.25-348.75 0.001033 0.000000 0.000000 0.000000 0.000000 0.000000 0.001033
Sub-Total: 0.582300 0.066804 0.000000 0.000000 0.000000 0.000000 0.649105
Calms: 0.350895
Missing/Incomplete: 0.000000
Total: 1.000000
Frequency of Calm Winds: 34.83%
Average Wind Speed: 3.72 m/s
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3.5.3 AMBIENT AIR QUALITY
The ambient air quality in one locations in core zone and eight locations in impact
(Buffer) zone i.e. 10 Km radius of the study area around the proposed project site as the
center taken to form the baseline information over which the predicted impacts has been
superimposed to find out the net impacts on the air quality of the surrounding
environment of the project area. The design of the network of ambient air quality
monitoring stations in the study area was done based on the following criteria.
Meteorological conditions on a synoptic scale & predominant wind direction
derived from plotted wind rose
Topography of the study area
Representation of the regional background levels
High population area
Air pollution in the project area is not bad . The prominent sources of air pollution in the
study area are due to emission from, vehicular movement and domestic fuel as coal
burning in some parts of the study area.
The pollutants of concern area are Particulate Matter (PM10 and PM2.5), SO2, NOX and CO.
Ambient air quality monitoring in the study area was carried out for the pollutants of
concern as per the project requirement. The selected sampling locations for air quality
study are shown in Fig-3.7. Air quality monitoring stations were selected. All the
ambient air quality monitoring stations were installed on flat roof, at least 3m above the
ground level with no obstructions and ensuring free flow of the wind.
Duration of sampling
The Duration of Sampling of Particulate Matter (PM10), Particulate Matter (PM2.5), SO2,
NOX, was each twenty-four-hourly continuous sampling per day and CO was sampled for
8 Hours continuous thrice in 24-hour duration monitoring. The Monitoring was conducted
for two days in a week for four months. This was to allow a Comparison with the present
revised standards mentioned in the latest gazette notification of MoEFCC 2009.
Sampling Frequency
The Ambient Air Quality Parameters along with their Frequency of Sampling are given
below
Table 3.7 Monitored parameters and frequency of sampling
Parameters Sampling Frequency
Particulate Matter (PM10) 24 Hourly Sampling twice a week for 3 months
Particulate Matter (PM2.5) 24 Hourly Sampling twice a week for 3 months
Sulphur Dioxide (SO2) 24 Hourly Sampling twice a week for 3 months
Oxides of Nitrogen (NOX) 24 Hourly Sampling twice a week for 3 months
Carbon Monoxide (CO) 8 Hourly Sampling for 24 Hour twice a week for 3
months
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Instrument Used for Sampling
Respirable Dust samplers (APM 460BL, FPS 550) have been used for monitoring
Particulate Matter (PM10, PM2.5). Gaseous Pollutants like SO2, NOX, were collected in the
impinger of attachment box (APM - 411) connected with RDS.
In General, the following points were taken in to consideration during sampling
Height of the sampler inlet 3 – 10 m above the ground level.
The Sampler more than 20 m away from large trees.
Distance of the sampler to any air flow obstacle i.e. buildings, more than two
times the height of the obstacle above the sampler.
There was unrestricted air flow in three of four quadrants.
Table 3.8 Techniques used for ambient air quality analysis
Sl. No. Parameter Technique Technical Protocol
1 Particulate Matter (PM10) Respirable Dust Sampler
(Gravimetric Method)
IS: 5182 Part IV
2 Particulate Matter (PM2.5 ) FP Sampler (Gravimetric
Method)
IS: 5182 Part IV
3 Sulphur Dioxide Modified West and Gaeke
method
IS: 5182 Part II
4 Oxides of Nitrogen Jacob & Hochheiser
method
IS: 5182 Part VI
5 Carbon Monoxide NDIR IS: 5182 Part X
Table-3.9: National Ambient Air Quality Standards as per MoEF Notification
under Schedule-VII, Rule- 3(3B). dt 18.11.09
Sl. No.
Pollutant (in µg/m3)
Time
Weighted Average
Concentration in Ambient Air
Industrial,
residential, Rural and Other Area
Ecologically
Sensitive Area (Notified by Central Govt.)
Methods of Measurement
1 Sulphur Dioxide (SO2) (µg/m3)
Annual * 24 hours **
50 80
20 80
- Improved West and Gaeke - Ultraviolet fluorescence
2 Nitrogen Dioxide (NO2) (µg/m3)
Annual * 24 hours **
40 80
30 80
- Modified Jacob & Hochheiser (Na-Arsenite)
3
Particulate Matter (size less than 10µm) or PM10
(µg/m3)
Annual * 24 hours **
60 100
60 100
- Gravimetric -TOEM - Beta attenuation
4
Particulate Matter (size less than
2.5µm or PM2.5) (µg/m3)
Annual *
24 hours **
40
60
40
60
- Gravimetric - TOEM
- Beta attenuation
5 Ozone (O3) (µg/m3) 8 hours ** 1 hour **
100 180
100 180
- UV photometric - Chemilminescence -Chemical Method
6 Lead (Pb) (µg/m3) Annual * 24 hours **
0.50 1.0
0.50 1.0
- AAS/ICP method after sampling on EPM 2000 or
equivalent filter paper
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- ED-XRF using Teflon filter
7
Carbon
Monoxide (CO) (mg/m3)
8 hours ** 1 hour **
02 04
02 04
- Non dispersive Infra Red (NDIR) spectroscopy
8 Ammonia (NH3) (µg/m3)
Annual * 24 hours **
100 400
100 400
- Chemiluminescence - Indophenol blue Method
9 Benzene (C6H6) (µg/m3)
Annual * 05 05
- Gas chromatography based
continuous analyzer - Adsorption followed by GC analysis
10 Benzo(a)Pyrene (BaP) – particulate
phase only(ng/m3)
Annual * 01 01 - Solvent extraction followed by HPLC/GC analysis
11 Arsenic (As)
(ng/m3) Annual * 06 06
- AAS/ICP method after sampling on EMP 2000 or equivalent filter paper
12 Nickel (Ni) (ng/m3) Annual * 20 20
- AAS/ICP method after sampling
on EMP 2000 or equivalent filter paper
* Annual arithmetic mean of minimum 104 measurements in a year at a particular site taken
twice a week 24 hourly at uniform intervals.
** 24 hourly or 08 hourly or 01 hourly mentioned values, as applicable, complied with 98 % of
the time in a year, 2 % of the time; they may exceed the limits but not on two consecutive days
of monitoring.
ToR-6(ii) AAQ data at 8 locations for PM10, PM2.5, SO2, NOx, CO and
other parameters relevant to the projects shall be collected.
Table- 3.10 A: Details of Ambient Air Quality Monitoring Locations
Sl.
No.
Locations Distance
(Km) Direction Type of area
1 Keshariya 7.0 NW Plantation Area
2 Bargopal
4.7 SE Rural & Residential
Area
3 Daharpur 5.89 S Proximity to Industries
4 Nutandih
5.54 SW Rural & Residential
Area
5 Silti 5.7 SW Residential Area
6 Belti 6.8 SW Residential Area
7 Shalkha
7.0 N Rural & Residential
Area
8 Mirjapur
5.1 E Rural & Residential
Area
Source: Monitoring, Period: Nov’2017 to Jan ‘2018, Site Specific AAQ Data
Selection Criteria: The AAQ monitoring location were selected in the down ward
movement of air in that particular season, which was dectected by running windrose
with monthly micrometerological data of that area.
The sampling locations are given in Fig 3.12.
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Table 3.10 B Summary of Ambient Air Quality Result
Location Code
Location Name
PM10 (µg/m3) PM2.5 (µg/m3) SOX (µg/m3) NOx(µg/m3) CO (µg/m3)
Max Min 98th perc
Max Min 98th perc
Max Min 98th perc
Max Min 98th perc
Max Min 98th perc
A1 Keshuriya 80.2 68.1 80.2 35.3 30.0 35.2 9.6 8.2 9.6 12.6 11.2 12.6 465 395 465.0
A2 Bargopal 79.8 62.8 79.7 35.7 27.6 35.5 9.4 6.1 9.4 12.6 10.5 12.6 431 372 430.5
A3 Daharpur 92.3 66.8 85.8 43.5 29.4 39.5 9.6 6.2 9.5 18.9 14.7 18.2 417 357 415.6
A4 Nutandihi 76.3 61.9 74.2 33.6 27.2 32.6 7.6 6.2 7.0 17.5 14.2 17.3 473 384 459.7
A5 Silti 77.4 65.7 77.1 36.4 30.9 36.3 8.4 6.1 8.4 16.3 13.8 16.3 403 342 401.2
A6 Belti 75.8 64.8 74.8 33.3 28.5 32.9 9.1 7.8 9.0 15.8 13.5 15.6 409 350 403.9
A7 Salkha 77.5 64.3 76.4 34.1 28.3 33.8 8.8 7.3 8.7 15.2 12.2 15.0 450 373 443.7
A8 Mirjapur 75.8 65.4 75.8 33.4 28.8 33.4 8.2 7.1 8.2 17.5 15.1 17.5 413 357 413.0
Range Value 92.3-61.9 43.5-27.2 9.6-6.1 18.9-10.5 473-342
NAAQS (Nov 2009) 100 (24 hours) 60 (24 hours) 80 (24 hours) 80 (24Hourly)
1 hour average : 4000 µg/m3 8 hour
average : 2000µg/m3
INSTRUMENT USED AND METHODS OF
MEASUREMENT
Fine Particulate Sampler SLE- 105 and
Gravimetric
Attachment SLE-133 Spectro photometric analysis (West-Geake
method)
Attachment SLE-133 Spectro photometric analysis (West-Geake
method)
Improved West and Gaeke
Non dispersive Infra Red (NDIR)
Spectroscopy
PROTOCOLS IS-5182 (Part-23) 2006,
Gravimetric EPA Guideline
IS-5182 (Part-2) 2001, West & Gaeke
IS-5182 (Part-6) 2006, Jacob & Hieocher
IS- 518 2 (Part 10 )2006
PM10 & PM2.5 concentration was maximum around the main gate area of the plant, as transport vehicles to and fro from the plant was
more on 17.11.17. In Daharpur also the AAQ concentration was high because of burning of paddy fields on dt. 12.01.18.
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Out of the eight locations in the study area, the maximum concentration for PM10 of 92.3
g/m3 was recorded at Daharpur and the minimum concentration of 61.9 g/m3 at
Nutandih Village. The 98th percentile values ranged between 93.6 – 61.9 g/m3 at all the
locations of core as well as buffer zone are below the CPCB norms. The 98 percentile
values for Daharpur village in buffer zone has high variation, due to its proximity to
Supreme Industries Pvt Ltd. The vehicular movement contributes to maximum pollution
in the area.
Out of the eight locations in the study area, the maximum concentration for PM2.5 of 43.5
g/m3 was recorded at the Daharpur. Location with the minimum concentration of 27.2
g/m3 was recorded at Nutandih. This is due to the fact that these locations are still
virgin in their nature owing low disturbance of the surrounding environment and the
existing physiography. This observable concentration values are a result of existing
“kaccha” village roads. Daharpur sampling location was located nearer to a plastic
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Industry and hence a higher value for PM 2.5 compared to other location was observed
here.
Out of the eight locations in the study area, the maximum concentration for SO2 of 9.6
g/m3 was recorded at Keshariya & Daharpur area with the minimum concentration of
6.1 was recorded at Bargopal & Silti monitoring locations. The 98th percentile values
ranged between 6.1-9.6µg/m3 at all the locations are within NAAQS.
Out of the eight locations in the study area, the maximum concentration for CO of 465
μg/m3 was recorded at Keshariya Observation site with the minimum concentration of
362 μg/m3 recorded at Silti Location. The 98 percentile values (in the range of 371-230
μg/m3) at all the locations are below the CPCB norms.
Due to the undisturbed physiography of the study area along with the low veichular
mobility in this area, the CO concentration was well within the limit prescribed as per
NAAQS standard and except for the Keshuriya location where concentration of CO is on a
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comparably higher side due to veichular movement and presence of small and cottage
industries.
The maximum concentration for NOx of 18.9 g/m3 was recorded at Daharpur Village
with the minimum concentration of 10.5 g/m3 at Bargopal. The 98 percentile values at
all the locations are within NAAQS standards.
ToR-6(iii) Raw data of all aaq measurement for 12 weeks of all
stations as per frequency given in the naqqm notification of nov. 2009
along with-min.- max. Average and 98% values for each of the aaq
parameters from data of all aaq stations should be provided as an
annexure to the eia report.
Raw AAQ data is attached as Annexure IV
Additional ToR 5 PM present in ambient air must be analysed for
source analysis/RSPM generated from plant operation
Table 3.10A: Chemical characterization of RSPM (PM10)
RSPM µg/m3 Keshariya Daharpur
Calcium as Ca µg/m3 1.45 1.41
Magnesium as Mg µg/m3 0.25 0.11
Sodium as Na µg/m3 0.02 0.01
Potassium as K µg/m3 0.02 BDL
Chromium as Cr µg/m3 BDL BDL
Aluminum as Al µg/m3 0.11 0.11
Silica µg/m3 0.01 0.01
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Lead as Pb µg/m3 BDL BDL
Zinc as Zn µg/m3 0.01 BDL
Iron as Fe µg/m3 0.02 0.01
Poly-aromatic hydrocarbon µg/m3 BDL BDL
PAH at all the monitoring stations is in low proportionate to have any impact on
From the ambient air quality monitoring carried out for three months (Nov 2017 to Jan.
2018) during the study period, it is found that the critical pollutants like PM10, PM2.5, SO2,
NOX and CO in buffer zone are within the permissible limits. Ambient Air Quality in the
study area may be attributed due to vehicular traffic on the State highway which is
adjacent to the BEL and vehicular rush on NH 16, the railways diesel engines, and
unchecked domestic fuel burnings etc in the study area.
MIXING HEIGHT
ToR-6(i) Determination Of Atmospheric Inversion Level at The Project
Site and Site-Specific Micro-Meteorological data using Temperature,
Relative Humidity, Hourly Wind Speed and Direction and Rainfall.
Mixing Height or Mixing Depth is used by meteorologist’s to quantify the vertical height
of mixing in the atmosphere. The concept ofmixing height (MH) is based on the principle
that when the atmosphereis heated from below due to the solar radiation, it becomes
unstable andgives rise to vertical motion and mixing. Mixing height is thus, defined asthe
top of a surface based layer in which vertical mixing is relatively vigorous and the lapse
rate is approximately dry adiabatic. These conditions are normally seen during cloudless
condition during day time.In the case of a ground based inversion, the mixing height is
zero or absent. Forecasting of mixing height is done with the aid of the vertical
Temperature profile. A radiosonde is sent aloft and temperatures atvarious altitudes are
radioed back. The altitude at which the dry adiabatic line intersects the radiosonde
measurements is taken as themaximum mixing depth (MMD). The MMD is a function of
stability. Inunstable air, the MMD is higher while it is lower in stable air. There is
aseasonal variation of mixing height. During summer daylight hours, MMDcan be a few
thousand meters, where it can be a few hundred meters inwinter. It also varies during
the course of a day. It is lowest at night andincreases as the day progresses. With a
measure of both MMD and windspeed with respect to height, we get a good idea of the
amount of pollutant dispersion. The mixing height shows increasing trend during the day
with theincrease of surface air temperature, achieving maxima around the timeof
maximum surface temperature and later in the afternoon over rural /open areas in fair
weather situation. However, it is more likely to remainpersistent to heights of roughly a
hundred meters or so over urban areasowing to slower cooling than rural / open areas.
Inversion height is used to quantify the vertical height of mixing in the atmosphere. The
concept of inversion height is based on the principle that when the atmosphere is heated
from below due to the solar radiation, it becomes unstable and gives rise to vertical
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motion and mixing. It is thus defined as the top of a surface based layer in which vertical
mixing is relatively vigorous and the lapse rate is approximately dry adiabatic.
For project region as can be seen from mixing height curve in winter, given below the
minimum height is at 6-7AM and maximum 1-2 PM
As can be seen from data given by IMD, Delhi the minimum mixing height at M/s BEL
project area is 40-80m and maximum mixing height is 1000-1150m.
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ToR-4(ix) Geological features and Geo-Hydrological status of the Study Area
shall Be Included
3.5.4 GEOLOGY OF THE STUDY AREA
The parent rock of Midnapore district is a mixture of metamorphic rocks of sedimentary
origin and igneous rocks both basic and acidic. Laterite, the characteristic formation of
the district, occupies a large tract. The thickness of the laterite varies from place to place
but is not known to exceed 15 m in this area. The sandy loam and loamy soil of reddish
or reddish-brown color covers the upper layers of almost the whole area. Three litho-
units are identified in study area:
(i) Laterite by its bluish red tone with coarse texture
(ii) Older Alluvium by its reddish tone with fine texture
(iii) Newer Alluvium
The rock is composed of disconnected vesicles. Multi-dimensional fractures may serve as
infiltration path for ground water replenishment, but not suitable for bulk supply of
water. The older alluvium formation consists of an intercalation of sandy and clayey
layers. Grain size varies from extremely coarse angular pebbles to fine sand and silt,
which have a good ground water bearing capability. The newer alluvium formation, on
the other hand, consists of a succession of clay and sand layers. Coarse sand bodies are
somewhat extensive and can act as excellent aquifers.
About 80% of the state's landmass is underlain by pre-cambrian rocks, the oldest rocks
in the earth's crust. The remaining area is composed of rocks belonging to Gondwanas,
Quarternary & Recent formations. The geological set up of the state is not only
favourable for discovery of wide variety of valuable ores and minerals but there is
distinct possibility of substantial increase in the resources.
The study area is not a compact unit and consists of widely, dissimilar tracts of
expansive and fairly open country, dotted with isolated peaks, inaccessible forests, river
valley and mountainous terrain. Broadly speaking it is an undulating table-land of
different elevations broken up by rugged hill ranges and cut off by torrential hill streams
and the river Kansabati. Varied landforms characterize the physiographic set-up of the
area. The area presents conspicuous physiographic variations marked by hills with
intervening intermontane valleys, isolated hillocks and flat to gently undulating plains.
The area is drained by the Kansabati river and its tributaries. The drainage pattern of the
area is dendritic. The general slope of the district is from north to south.
3.5.5 GEOMORPHOLOGYOF THE STUDY AREA
The geological map depicts 80% of geological formation is alluvium with sand silt and
clay, 10% Alluvium with fine sand, silt & clay and rest 10% in the North West of the area
is Lateritic soil.
The general topography of the study area is gradually undulating to flat where the area
is sloping from North and South. It is marked by low isolated hill ranges or hillocks.
Broadly speaking it is an undulating table-land of different elevations broken up by
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rugged hill ranges and cut off by torrential hill streams and the river Kansabati. Because
of this undulating, hilly and sloping nature of landscape, the area is subject to rapid
runoff leading not only to soil erosion but also to scarcity of water for both agriculture
and drinking purpose. These are generally in the form of boulders or rocky knobs. The
direction of these hill ranges is from North West to South East. There are patches of
sheet rocks scattered all over the area with very little natural vegetative cover. The
average ground level of the study area is about 32 m above the MSL.
3.5.6 WATER ENVIRONMENT:
Hydrogeology
The spatial distribution of groundwater is not uniform, area has very shallow (1.5 m bgl)
to very deep (9.2 m bgl) water table. Deep water table occurs adjacent to the foot hill.
Higher well yields indicate relatively greater groundwater availability than areas with low
well yields.
Ground water in the area occurs under unconfined conditions in the top most weathered
mantle (5-22 m thick) of the different lithological units present in the region. The
occurrence and movement of groundwater in the deeper zones are controlled by
secondary porosities like joints, fractures, faults etc and also by the bedding planes in
the Gondwana sedimentary rocks. Ground water in the sedimentary rocks also occurs in
the primary porosity offered by interconnected joints in coarse grained sandstones, etc.
The faults and dykes present in the area are of particular significance as the faults
provide natural plane of seepage, while dykes have a tendency to impound water along
its gradient direction. The quality of ground water is, in general, good and is suitable for
domestic, industrial and irrigational purposes except in some cases where it is
contaminated with minor seepage water from the nearby coal mines, when it becomes
bacteriologically unsatisfactory.
Depth of Groundwater and Variations
Dug wells are more common in the study area. Nearly 30% of the wells are shallow type
and water table is within 8m depth. The deep dug wells are up to a depth of 17m. The
study of fluctuation in ground in groundwater levels by the groundwater board (CGWB)
reveals that the fluctuation is in the order of 1.85m to 3.90m during post-monsoon and
4.29m to 8m during pre-monsoon.
Surface Water
The main drainage network of the study area includes River Kansabati and its tributaries
in the form of canals and streams. The directions of flow of most of the rivers are
controlled by slope which in general is towards North to South East as it was evident
from the flow of the rivers in the study area and the availability of groundwater in the
region (Figure-3.14). Kansabati river is of high significance in the region as it caters to
the water requirements to most of the villages and the majority of the industrial units in
the region. Besides Kansabati river, other steams and the few tanks and small reservoirs
in the study area constitute the drainage in the study area.
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ToR 4(x) Details of the drainage of the project up to 5 km radius of
study area. If the site is within 1km radius of any major river, peak
and lean season river discharge as well as flood occurrence frequency
based on peak rainfall data of the past 30 years. Details of the flood
level of the project site and maximum flood level of the river shall all
so be provided. (Mega green field projects)
Kangsabati river is about 16.7 km away from the project site. The HFL is 16.5 km from
the project site.In 1978, the area was slightly affected by flood but no flood hazard was
observed in the project site.
The drainage map in the study area shows the drainage pattern is from North West
uplands to Sowth East low lands, there are numerous water bodie and no measure River
flows within the study area, a small River called as Kalighai passing in the western part
of the area.
A number of water samples from river, pond, dug well & bore well were collected from
different locations within study area as shown in Figure- 3.12.The water samples were
collected and analyzed for physical, chemical and microbiological characteristics as per
CPCB guidelines and approved methods. The sampling station location is given in Table-
3.12 and the analysis results of surface and groundwater are given in the Table-3.12A &
3.12B
Gen. ToR 6 (iv) Surface water quality of nearby river (60m upstream
and downstream) and other surface drains at 8 locations as per
CPCB/MoEFCC guide line.
Gen.ToR 6 (vi) Ground water monitoring at minimum 8 locations shall
be included.
Surface water and Ground water are the essential elements of life process, Water plays
an important role in the world economy. Approximately 70% of the freshwater used
by humans goes to agriculture and rest 30% for domestic use. Water moves continually
through the water
cycle of evaporation, transpiration (evapotranspiration), condensation, precipitation,
and runoff.
So in the ecological point of view it an abiotic component which interacts with the life
forms for their existence (Human & Animals), so water parameters are taken for analysis
prior to setting of any industry, which can there after be evaluated wheter there is any
change in the water quality, if so then the source can be identified, and remediation can
be taken.
Table- 3.12: Surface and Groundwater Sampling Locations
Sl.
No. Code Location
Distance
(KM) Direction
W r t proposed plant
site
Surface water
1 SW1 60m Upstream of Kangsabati
River 16.9 N
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2 SW2 60m downstream of
Kangsabati River 16.6 N
3 SW3 Pond water of Nutandih 5.5 SW
4 SW4 Pond water of Dauka 1.04 E
5 SW5 Pond water of Rampura 0.7 S
6 SW6 Pond water of Bagberia 2.2 W
7 SW7 Pond water of Banspukuria 1.8 S
8 SW8 60m downstream of Kalighai
River 4.7 E
Groundwater
1 GW1 Dug well of Daharpur 5.89 S
2 GW2 Tube well of Nutandih 5.54 SW
3 GW3 Tube well of Silti 5.7 SW
4 GW4 Dug well of Keshariya 7.0 NW
5 GW5 Dug well of Bargopal 4.7 SE
6 GW6 Tube well of Belti 6.8 SW
7 GW7 Tubewell of Shalkha 7.0 N
8 GW8 Tubewell of Mirjapur 5.1 E
The analysis report of surface water and ground water is given in Annexure B and
Annexure C respectively.
Site selection criteria
Surface water: Nearest water bodies like pond, stream, were selected which are falling
into rivers during monsoon, so sampling points were taken adjacent to the plant for
surface water analysis.
Ground Water: Bore wells were selected in nareby villages with close proximity to the
industry.
Add Tor 13 Trace Metal in Water
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Table 3.12 A Ground Water analysis result
PARAMETERS Unit Daharpur Nutandihi Silti Kesharuiya Bargopal Belti Salkha Mirjapur
Desirable Limits
Permissible Limit
Protocol
A. PHYSICAL
1 Colour (apparent) Hazen < 1.0 < 1.0 < 1.0 < 1.0 < 1.0 < 1.0 < 1.0 < 1.0 5 25 IS3025:PART04:1983
2 Odour
-- Agreeable Agreeable Agreeable Agreeable Agreeable Agreeable Agreeable Agreeable
UO IS3025:PART05:1983
3 Taste
Agreeable Agreeable Agreeable Agreeable Agreeable Agreeable Agreeable Agreeable
Agreeable
IS 3025:PART7&8:1984
4 Turbidity NTU 0.2 0.3 0.3 0.4 0.5 0.1 0.3 0.2 5 10 IS 3025:PART10:1984
5 pH -- 7.1 7.3 7.1 7.2 7.5 7.1 7.2 7.4 6.5-8.5 IS3025:PART11:1983
6 Electrical Conductivity (EC) μS/cm
532 588 580 609 626 547 592 549
7 Total Suspended Solids (TSS) mg/l
< 0.4 < 0.4 < 0.4 < 0.4 < 0.4 < 0.4 < 0.4 < 0.4
8 Total Dissolved Solids (TDS) mg/l
294 322 320 334 342 300 324 302 500 2000 IS 3025:PART10:1984
B. CHEMICAL
9 Calcium Hardness as CaCO3 mg/l
60 64 56 72 100 64 76 56 IS 3025:PART40:1991
(Reaff 2003)
10 Magnesium Hardness as CaCO3 mg/l
32 36 32 32 16 40 20 36 IS 3025:PART46:1994
11 Total Alkalinity as CaCO3 mg/l 74 80 70 84 94 82 78 74 200 600 IS 3025:PART23:1986
12 Total hardness Mg/l 92 100 88 104 116 104 96 92 200 600 IS 3025:PART21:2009
13 Residual Chlorine mg/l < 0.04 < 0.04 < 0.04 < 0.04 < 0.04 < 0.04 < 0.04 < 0.04 0.2 1 IS 3025:PART 26
14 Phenolic compound as C6H5OH mg/l
< 0.001 < 0.001 < 0.001 < 0.001 < 0.001 < 0.001 < 0.001 < 0.001 0.001 No
Relaxation IS 3025:PART43:1992
15 Sulphate as SO4 mg/l 35.4 32.4 24.2 26 28.6 38.6 21.4 46.4 200 400 IS 3025:PART24:1986
16 Chloride as Cl mg/l 32 36 32.6 31.4 28.4 26.4 34.5 32.2 250 1000 IS 3025:PART32:1992
17 Cyanide as CN mg/l
< 0.01 <0.01 < 0.01 <0.01 < 0.01 < 0.01 < 0.01 < 0.01 0.05 No
Relaxation IS 3025:PART27:1986
18 Selenium as Se mg/l
<0.005 < 0.005 <0.005 <0.005 <0.005 <0.005 <0.005 <0.005 0.01 No
Relaxation IS3025:PART 56:1988
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19 Ammonia(as total ammonia-N), mg/l, Max mg/l
< 0.3 < 0.3 < 0.3 <0.3 < 0.3 < 0.3 < 0.3 < 0.3 0.5 No
Relaxation IS 25:PART:34:1988
20 Mineral oil mg/l
< 0.025 <0.025 < 0.025 < 0.025 < 0.025 < 0.025 < 0.025 < 0.025 0.5 No
Relaxation Clause 6 of IS 3025(Part 39)
21 Fluoride F- mg/l 0.08 0.28 0.29 0.29 0.28 0.28 0.31 0.32 1.0 1.5 IS 3025 (PART 60)
22 Calcium as Ca2+
mg/l 24 25.6 22.4 28.8 40 25.6 30.4 22.4 75 200 IS 3025:PART40:1991
23 Magnesium as Mg2+
mg/l 7.78 8.75 7.78 7.78 3.89 9.72 4.86 8.75 30 100 IS 3025:PART46:2008
24 Iron (Fe) mg/l
0.1 0.12 0.11 0.13 0.21 0.21 0.11 0.09 1 No
Relaxation IS 3025 (Part 53) : 2009
25 Nitrate mg/l
1.8 2.8 2.3 2.3 2.3 2.3 2.5 2.4 45 No
Relaxation IS 3025 (Part 34) : 2009
26 Copper (Cu) mg/l < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 0.05 1.5 IS 3025:PART42:1991
27 Manganese (Mn) mg/l < 0.05 < 0.05 < 0.05 < 0.05 < 0.05 < 0.05 < 0.05 < 0.05 0.1 0.3 IS 3025:PART46:1994
28 Arsenic (As) mg/l 0.001 0.003 0.0025 0.0035 0.004 0.0018 0.0013 0.0011 0.1 IS 3025:PART37:2003
29 Lead (Pb) mg/l
< 0.005 < 0.005 < 0.005 < 0.005 < 0.005 < 0.005 < 0.005 < 0.005 0.01 No
Relaxation IS 3025:PART47:1992
30 Zinc (Zn) mg/l 0.012 0.06 0.015 0.015 0.025 0.012 0.016 0.01 5 15 IS 3025:PART49:2006
31 Chromium (Cr) mg/l
< 0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 0.05 No
relaxation IS 3025:PART52:1988
32 Nickel as Ni mg/l
<0.01 <0.01 <0.01 <0.01 <0.01 <0.01 <0.01 <0.01 0.02 No
relaxation IS 3025:PART54:1994
33 Mercury (Hg) mg/l
<0.0005 < 0.0005 <0.0005 <0.0005 <0.0005 <0.0005 <0.0005 <0.0005 0.001 No
relaxation IS 3025:PART48:1994
34 Cadmium (Cd) mg/l
< 0.001 < 0.001 < 0.001 < 0.001 < 0.001 < 0.001 < 0.001 < 0.001 0.003 No
relaxation IS 3025:PART41:2003
35 Aluminium (Al) mg/l
< 0.02 <0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 < 0.02 0.03 0.2 IS
3025:PART55:2003
36 Anionic Detergents as(IMBAS) mg/l
<0.1 < 0.1 <0.1 <0.1 <0.1 <0.1 <0.1 <0.1 0.2 1.0 Annex KIS 13428
37 Boron (B) mg/l < 0.1 < 0.1 < 0.1 < 0.1 < 0.1 < 0.1 < 0.1 < 0.1 0.5 1.0 IS 3025:PART57:1992
C. BACTERIOLOGICAL
38 Total Coliform at 370C
MPN index / 100ml
Absent Absent Absent Absent Absent Absent Absent Absent 10 50 IS 1622:1981 (Reaff 2003)
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6.9
7
7.1
7.2
7.3
7.4
7.5
7.6
pH
Description
The analytical results of ground water samples at different location for various
parameters reveal that all the parameters comply with IS: 10500 standards indicating
their suitability for drinking and other purposes
Deliberation:
pH: pH of Groundwater in the area is neutral; alkalinity is primarily a measure of
dissolved bicarbonate and carbonates.The geological findings shows that lime stine
strata in not so well defined.
Electrical Conductivity: Electrical Conductivity depends on the amount of dissolved
solutes in the ground water; Water with high conductivity may have objectionable taste,
cause staining, and precipitate scale in pipes and containers. EC of water was between
532-626μS/cm
Total dissolved solids: (TDS) is the portion of total solids that has passed through a
filter, and the remaining water then evaporated, leaving the TDS residue. TDS is often
used as an indicator of the suitability of that groundwater for various uses. Total
dissolved solids values typically increase with sample depth or the distance that
groundwater has traveled from recharge area to sample site & anionic salts present. TDS
in the area is between 294-342 mg/l which fairly below the standard.
Heavy Metals: Metals are inorganic substances consisting of positive ions and
containing no carbon. Heavy metals, which may be found in groundwater, have a specific
gravity at least five times that of water. Ground water of that area have very less
concentration of heavy metals which is below the limits.
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Hardness: hardness is defined as the concentrations of dissolved calcium and
magnesium expressed as an equivalent amount of calcium carbonate,iron also partially
responsible for hardness in water, Total hardness of ground water in that area was in
between 88-116 mg/l. wchich is morerately hard but suitable for consumption.
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Table 3.12 B Surface Water analysis result
Sl. No.
Characteristics Unit IS:2296-1982
Class ‘C’ Limits
RiverKansabati U/s
River Kangsabati
D/s Nutandihi Dauka Rampura Bagberia
Banspukuria
River Kalighai
D/s Protocol
1 pH - 6.5-8.5 7.23 7.32 7.51 7.62 7.31 7.53 7.34 7.64
IS 3025:PART11:1983 (Reaff 2002)
2 DO mg/l 4 6.8 6.2 5.2 5.2 4.8 5.8 5.2 5.2 IS 3025:PART58:2006
3 BOD mg/l 3 5 8.4 6.8 8.2 8.8 8.2 8.2 7.4 IS 3025:PART44:1993
4 COD mg/l -- 28 32 18 20 25 22 24 32
APHA-23rd
Edition (5220 B):2017
5 Total Coli form
MPN/100 ml
5000 >1600 >1600 >1600 >1600 >1600 >1600 >1600 >1600 IS 1622:1981 (Reaff 2003)
6 Colour
True Colour Units
300 1 1.2 1.8 1.4 1.4 5.2 8.3 1 IS 3025:PART04:1983 (Reaff 2002)
7 Conductivity µS/cm -- 583 622 350 414 428 421 429 317
APHA-23rd
Edition (2510A):2017
8 Fluoride (as F) mg/l 1.5 0.32 0.31 0.33 0.29 0.34 0.38 0.36 0.24 IS 3025:PART60:2008
9 Cadmium mg/l 0.01 <0.001 <0.001 <0.001 <0.001 <0.001 <0.001 <0.001 < 0.001 IS 3025:PART41:1992
10 Chloride (as Cl) mg/l 600 22.3 28.4 5.2 4.6 5.4 7.5 24.2 15.1 IS 3025:PART32:1988
11 Chromium (as Cr+6
) mg/l 0.05 <0.05 < 0.05 <0.05 < 0.05 <0.05 <0.05 <0.05 <0.05 IS 3025:PART52:2003
12 Cyanide (as CN) mg/l 0.05 <0.01 <0.01 <0.01 < 0.01 <0.01 <0.01 <0.01 <0.01 IS 3025:PART27:1986
13 Total Dissolved Solid
mg/l 1500 334 386 236 228 265 230 236 148 IS 3025:PART15:1984 (Reaff 2002)
14 Selenium mg/l 0.05 <0.01 <0.01 <0.01 <0.01 <0.01 <0.01 <0.01 <0.01 IS 3025:PART56:2003
15 Sulphate (as SO4) mg/l 400 22.2 4 26.1 34.7 34.6 29.8 35.1 5.1 IS 3025:PART24:1986
16 Lead mg/l 0.1 <0.01 <0.01 <0.01 < 0.01 <0.01 <0.01 <0.01 < 0.01 IS 3025:PART47:1994
17 Copper mg/l 1.5 <0.01 <0.01 <0.01 < 0.01 <0.01 <0.01 <0.01 <0.01 IS 3025:PART42:1992
18 Arsenic mg/l 0.2 <0.01 <0.01 <0.01 < 0.01 <0.01 <0.01 <0.01 < 0.01
IS 3025:PART37:1988 (Reaff 1999)
19 Iron mg/l 50 0.52 1.22 0.06 0.12 0.09 0.08 0.2 0.32 IS 3025:PART53:2003
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20
Phenolics compounds (as C6H5OH)
mg/l 0.005 <0.001 <0.001 <0.001 <0.001 <0.001 <0.001 <0.001 <0.001 IS 3025:PART43:1992
21 Zinc mg/l 15 0.026 0.07 0.11 0.1 0.01 0.1 0.2 0.06
IS 3025:PART49:1994 (Reaff 2003)
22 Anionic detergents (as MBAS)
mg/l 1 < 0.1 <0.1 <0.1 < 0.1 <0.1 <0.1 <0.1 < 0.1 Annex K of IS 13428:2005
23 Oil & grease mg/l 0.1 <0.025 < 0.025 <0.025 <0.025 <0.025 <0.025 <0.025 < 0.025 IS 3025:PART39:1991
24 Nitrate (as NO3) mg/l 50 3.6 1.32 2.4 1.2 2.4 2.6 2.8 2.3 IS 3025:PART34:1988
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The analysis result of Surface Water:
Discussion
Heavy Metals: Heavy metals, which may result from chemical leaching of bedrock, water
drainage, and runoff from banks, the discharge of urban industrial and rural agricultural
wastewaters, are widely present in water and sediments. Heavy metals like Zn, Mg, Cu, Fe
are essential for the aquatic life process in low concentration, but metals like As, Hg, Cd are
not required even in low concentration. Except Iron in Teesta river iron was found to be high
may be due to mining activities of industries situated in the upstream, all other metal
concentration is below the prescribed limit.
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Discussions
Nitrates in streams, ponds, and estuaries causes eutrification and damage to aquatic
life. Sulfates can be naturally occurring or the result of municipal or industrial discharges
water passing through rock or soil containing gypsum and other common minerals, or of
atmospheric deposition.Chlorides are not usually harmful to people; however, the
sodium part of table salt has been linked to heart and kidney disease. Sodium chloride
may impart a salty taste. rocks containing chlorides, agricultural runoff, wastewater from
industries,oil well wastes,effluent wastewater from wastewater treatment plants, road
salting, rocks containing chloride, agricultural runoff, wastewater from industries,oil well
wastes, effluent wastewater from wastewater treatment plants road salting. Most of the
pareameters are within the limit and within the norms of IS: 2296 Class ‘C’.except BOD
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Dissolved Oxygen & Biochemical Oxygen demand
DO is the amount of gaseous oxygen dissolved in the water. Oxygen enters the water by
direct absorption from the atmosphere, by rapid movement, or as a waste product of
plant photosynthesis. Water temperature and the volume of moving water can
affect dissolved oxygen levels.Aquatic organisms need dissolved oxygen to respire It is
necessary for the survival of fish, invertebrates, bacteria, and underwater plants. DO is
also needed for the decomposition of organic matter.The DO content in all the locations
are between 4.8-6.8 mg/l, Rampura pond was a stagnant water pond so the DO
concentration was low i,e 4.8 mg/l.
BOD Biochemical Oxygen Demand is the amount of dissolved oxygen needed by
aerobic biological organisms to break down organic material present in a given water
sample at certain temperature over a specific time period.is the amount of oxygen
required to reduce the organic carbon present, BOD in the samples were between 5.0-
8.4 which is higer than the limit mostly because of discharge of sewage in to the surface
water.
Gen.ToR6 (v) whether the site falls near to polluted stretch of river
identified by CPCB/MoEFCC
Discussions
No stretch of river length has been identified as polluted stretch.
3.5.7 SOIL CHARACTERISTICS
Introduction
Soil analysis is done in the apprehension that if there is any threat to soil fertility, soil
erosion or change in land use after commissioning of the plant like spillage of oil,
hazardous materials, high surface runoff, escavation of top soil.
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Agriculture is the main occupation in the study area. Hence it is essential to determine
the agriculture potential of the soil from the area and identify the impacts of urbanization
and the industrialization in the area.
Methodology
For studying the soil profile of the region 6 soil sampling points were selected to assess
the existing soil conditions in and around the project area. Soil samples were collected
during the winter season which was analyzed for physical and chemical properties. Soil
samples were collected from three different depths, 5-10 cm, 10-20 cm and 20-30 cm
below the surface. The samples were homogenized and the quantity was reduced by
coning and quartering method. The samples were packed in polyethylene bags and sent
to lab & analyzed.
West Bengal state represents a wide variety of geological, climatic, vegetational and
physiographic features that have an impact on the soil formation and various types of
soil. These soils have direct distinct morphological and physico-chemical properties that
influence the plant growth and the cropping pattern in the region.
Soil Types
The prevailing soil types in the study area are mostly alluvial and lateritic in nature. The
general characteristics of these soils are given below.
Alluvial soil
High in fertility
Newly formed alluvial soils are called ‘ Khader’ and old soils are ‘Bhanger’
Found mostly in flood plain and deltas of river Damodar and its tributaries.
Laterite soil
Very low in fertility
Formed in the monsoon climatic regions
Mixture of clay and red soils
Thus the sampling locations are decided based on one or more criteria listed below:
To determine the existing soil characteristics of the study area
To determine the impact on soil characteristics due to the activities of the existing
industries located in the study area
To determine the impact on agricultural productivity of soil due to the proposed
activity
Mojor land mass in the centre vertical area is covred by Fine Vertic Ochraqualfs in the
western position Fine Loamy coarse lomy soil is covered, in the extreme Eastern area
Fine Typic Haploquipts soil is found.
The details of the soil sampling locations are given in Table- 3.13.
Tor-6(viii) Soil Characteristics As Per CPCB Guidelines.
Soil samples were collected from agricultural fields, pasure lands within the buffer zone.
As maximum land use is for agricultural use so Soil samples were mostly collected from
crop fields.
Table- 3.13: Details of Soil Quality Monitoring Locations
Station
Code
Location Distance(Kms) Direction Land Use
(w.r.t project site)
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S1 Project site -- --
S2 Nutandih 5.54 SW Crop Land
S3 Silti 5.5 SW Crop Land
S4 Keshariya 7.0 N Grass
Land/Grazing field
S5 Bargopal 4.6 SE Crop Land
S6 Belti 6.8 SW Crop Land
The analytical results of the soil samples collected during the study period are
summarized in Table 3.13 A.
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Table 3.13 A Soil Analysis Results
Sl.No Parameter Project site Nutandihi Silti Kesharuiya Bargopal Belti
1 Colour Yellowish Grey Yellowish Grey Yellowish Grey Yellowish Grey Yellowish Grey Yellowish Grey
2 Texture Silty Clayey Loam Silty Clayey Loam Silty Clayey Loam Silty Clayey Loam Silty Clayey Loam Silty Clayey Loam
3 Water holding capacity % 46.4 46.8 45.8 46.3 45.7 47.1
4 pH 7.21 7.23 7.41 7.28 7.96 7.12
5 Electrical conductivityµmhos/Cm
389 387 378 394 401 388
6 Co-efficient of permeability m
3/Sec. At
20OC
1.2x10-3 1.2x10-4 1.2x10-3 1x10-4 1.1x10-4 1.2x10-3
7 Bulk Density Gm/cc 1.16 1.13 1.21 1.2 1.2 1.3
8 Porosity % 23 22 24 22 21 25
9 Organic carbon % 1.13 1.14 1.12 1.19 1.13 1.17
10 Calcium % 2.5 3.6 3.7 0.87 1.02 0.98
11 Organic matter % 2.02 2 1.98 5.05 4.95 5.23
12 Phosphate (PO4) mg/Kg 0.019 0.018 0.016 0.014 0.007 0.015
13 Iron Fe mg/Kg 1258 1728 1087 12580 13258 11782
14 Manganese mg/Kg 1174 1392 1204 1274 1328 1167
15 Chromium mg/Kg 0.01 0.02 0.022 0.01 0.02 0.022
16 Potassium % 0.08 0.07 0.06 0.04 0.06 0.08
17 Total Nitrogen % 0.019 0.022 0.023 0.095 0.088 0.079
18 Texture
I Sand %w/w 29 32 30 27 25 28
Ii Silt %w/w 38 39 41 44 45 48
iii Clay %w/w 23 29 29 29 30 24
Test Method A text Book Of Soil Analysis By T.C.Baruah & H.P.Barthakur
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0
2000
4000
6000
8000
10000
12000
14000
in m
g/kg
Iron
Manganese
Chromium
0
5
10
15
20
25
30
Porosity
Co-efficient of
permeability
Bulk Density
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Discussion
Porosity: is a measure of how much open space is there inbetween soil particles, this
space can be between grains or within cracks or cavities of the rock. Porocity in the area
varies from 21%-23% which is moderately porous.
Permeability: is how ease can water pass through the pores, here in the analysis
report permability is very low as because clay percentage is more and alluvium deposit is
more. Permwbility is low and is between 1x10-4 to 1.2x10-3 as the soil texture is clayey.
Nitrogen Potassium Phosphorus: Nitrogen in soil comes through physical
(atmospheric nitrogen fixation), biological fixation and through biological process from
bacteria & blue green algae. Nitrogen range is between 0.019% to 0.095%.
Phosphorous: Phosphorous is mainly derived from rocks and bones as natural source.
Phosphorous percentage ranges between 0.007% to 0.019%.
Potassium:It is mainly derived from rocks, mineral surface and animal
wastes.Potassium ranges between 0.04% to 0.08%.
These three element plays a vital role in plant growth, generally all these elemets are
supplemented artificially to the crop fields, the area has level of phosphorus,
monoculture of a crop has resulted in depletion of natural minerals in that area.
The soil fertility can be increased naturally by growing multiple crops and intercropping
ang growing leguminous plants.
The soils of the study area are predominantly yellowish gray in colour and Silty loamy in
Texture and also slightly alkaline/neutral in nature. The analysis results of the soil
parameters are within limits. The bulk density of the study area ranges from 1.13 to
1.3gm/cc. The other nutrient contents like nitrogen, potassium and phosphate content of
the soil is very low.
3.5.8 NOISE ENVIRONMENT:
Tor-6(vii) Noise Levels Monitoring At 8 Locations Within The Study
Area.
The physical description of sound concerns its loudness as a function of frequency. Noise
in general is an unwanted sound, which is composed of many frequency components of
various types of loudness level distributed over the audible frequency range. Sound
Pressure Levels (SPL’s) are measured in decibels on the A-weighted scale, dB (A), where
the A-weighting scheme accounts for the sensitivities of the human ear over the audio
spectrum.
Reconnaissance Survey and Identification of Sampling Locations
A preliminary reconnaissance survey was undertaken to identify the major noise
generating sources in the area. The noise at different noise generating sources based on
the industrial activities, commercial activities, traffic, noise at sensitive areas like
hospitals and schools have been identified. The noise monitoring has been conducted at
all the identified location in the study area once in a season during the study period and
Measured noise levels, displayed as a function of time, is useful for describing the
acoustical climate of the community. Noise levels recorded at each station with a time
interval of about 60 minutes are computed for equivalent noise levels. Equivalent noise
level is a single number descriptor for describing time varying noise levels. The
equivalent noise level is defined mathematically as
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Leq = 10 Log L / T∑ (10Ln/10)
Where, L = Sound pressure level at function of time dB (A)
T = Time interval of observation
Noise levels during the night time generally drop, therefore to compute Equivalent noise
levels for the night time, noise levels are increased by 10 dB (A) as the night time high
noise levels are judged more annoying compared to the day time. Noise levels at a
particular station are represented as Day Night equivalents (Ldn). Day Night equivalent
is the single number index designed to rate environmental noise on daily / 24 hourly
basis.
Mathematically Ldn is given by
Ldn = 10 Log {1/24 (16 x 10(Ld/10) + 8 x 10(Ln/10)}
Where Ld = A weighed equivalent for day time period (6am-10 pm)
Ln = A weighed equivalent for night time period (10 pm to 6 am)
Assessment of Noise Levels
The main objective of noise level assessment is to identify all the sources acceptable and
unacceptable to the study region. The acoustical environment varies dynamically in
magnitude and character throughout most communities. The noise level variation can be
temporal, spectral and spatial. The maximum impact of noise is felt on urban areas,
which is mostly due to the commercial / industrial activities and vehicular movement
during peak hours of the day.
The assessment of noise pollution in the study area has been carried out keeping the
above said considerations. The existing status of noise levels within the study zone has
been undertaken through reconnaissance, identification of existing noise sources, land
use pattern for monitoring of baseline noise levels.
Sources of Noise
An inventory was conducted for evaluating the sources of noise generation in the study
area. It was observed that the major sources of noise generation in the study area were
from the Industries, Commercial activities and vehicular movements etc.
Typical considerations in environmental noise assessment can be divided into two
separate categories, one related to noise sources and other related to potential
receivers. Two quantities are needed to describe completely the strength of the source.
1- Sound Power Levels
2- Directivity
Sound Power levels measure the total sound power radiated by the source in all
directions and directivity is a measure of the difference in radiation with direction. The
concept of sound power level and directivity index makes it possible to calculate the
sound pressure level (BSPL) created by source. The impact of noise sources on
surrounding community depends on:
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Characteristics of noise sources (instantaneous, intermittent or continuous in
nature). It is well known that a steady noise is not as annoying as one that is
continuously varying in loudness.
The time of the day at which noise occurs, for example, loud noise levels at night
in residential areas are not acceptable because of sleep disturbance.
The location of the noise source, with respect to noise sensitive land use, that
determines the loudness and period of noise exposure.
The environmental impact of noise can have several effects varying from Noise Induced
Hearing Loss (NIHL) to annoyance depending on loudness of noise levels. The
Environmental Impacts of noise from the plant activities is carried out by taking into
consideration the various factors:
Potential damage to hearing
Annoyance
Potential physiological responses
General community responses
Noise Levels in the Study Area
Nine noise monitoring stations were identified for the assessment of the existing noise
levels keeping in view the nature of the monitoring location i.e. residential areas in
villages, schools, bus stations etc. The distance and the direction of the noise monitoring
locations with reference to the Project site is given in the Table -3.14.
Eight locations were selected within one km radius around the plant boundary so that
immedeate impact can be measured.
Station
Code
Location Direction Distance (kms) Description of
Location
(w.r.t project site)
N1 Boundary wall of NE side - 0 Proximity to NH
16
N2 Boundary wall of NW side - 0 Proximity to
Railway Track
N3 Boundary wall of SE side - 0 Proximity to NH
16
N4 Boundary wall of SW side - 0 Proximity to
Railway Track
N5 Rampura Batitaki SW 0.58 Settlement
N6 Dauka NW 0.86 Settlement
N7 Shyamalpur W 0.32 Settlement
N8 Tentulmuri E 0.94 Settlement
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Table -3.14. Noise Monitoring Values
Station
code Location village Lday Lnight Ldaynight
N1 Boundary wall of NE side 52.3 43.3 51.8
N2 Boundary wall of NW side 54.2 43.5 42.3
N3 Boundary wall of SE side 56.1 44.6 44.2
N4 Boundary wall of SW side 54.4 42.2 41.9
N5 Rampura Batitaki 59.2 41.7 47.1
N6 Dauka 57.3 44.1 45.2
N7 Shyamalpur 55.7 42.4 43.2
N8 Tentulmuri 53.6 44.1 43.2
CPCB
Norms
For Industrial Area
75
70
For Residential Area
55
45
Discussion
The noise reading taken were within the limits as there is no such noise generating
source except vehicular movement. During fesivals the noise level increases.
3.6 TRAFFIC STUDIES:
Gen. ToR 6 (ix) Traffic study of the area, type of vehicles, frequency
of vehicles for transportation of material, additional traffic due to
project, parking arrangement etc.
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Traffic study
M/s Bengal Energy Ltd has sheds for parking of cars and two wheelers for employees
and visitors near administrative building and various shops. Sheds have been ear
marked for different users. These sheds are inside plant boundary having large vacant
space in front of sheds for movement of vehicles.
Raw material & product transportation vehicles have different entry route and space has
been earmarked for parking of heavy vehicles with arrangement of rest room for drivers.
This is near main gate inside plant boundary near security post. The area has to be
further developed to accommodate additional vehicles due to expansion of project.
Traffic load for proposed expansion.
For study of additional transport load on existing road NH-16 was selected at 1km from
Rampura toll plaza through which raw material and products for the project will pass.
Study was made for two days in November 2017, 28th Tuesday and 29th Wednesday and
again another two days 22nd January Monday and 23rd January 2018.
Traffic count was monitored continuously for 24 hours each day. Both way traffic
movements were counted which consisted both heavy and light vehicles as well as two
wheelers and three wheelers.
The average hourly readings have been tabulated below.
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Time in hours No. of Vehicles for 4 days averaged hourly
Multi
axils
vehicle
Heavy
Motor
Vehicles
Light
Commerci
al Vehicles
Cars Three
/Two
Wheeler
s
Total
06.00-07.00 18 250 48 38 15 369
07.00-8.00 15 240 35 45 30 365
08.00-09.00 13 200 50 60 25 348
09.00-10.00 14 185 40 55 33 327
10.00-11.00 18 180 25 60 35 318
12.00-13.00 18 298 20 40 12 388
13.00-14.00 19 265 15 55 9 363
14.00-15.00 20 182 20 40 5 267
15.00-16.00 20 178 34 67 7 306
16.00-17.00 19 182 20 60 6 287
17.00-18.00 15 176 22 50 20 283
18.00-19.00 26 180 24 40 22 292
19.00-20.00 20 198 26 60 24 328
20.00-21.00 20 138 20 55 20 253
21.00-22.00 22 175 16 38 18 269
22.00-23.00 26 210 20 46 10 312
23.00-24.00 22 298 22 20 0 362
24.00-1.00 15 265 20 20 0 320
1.00-2.00 10 214 20 15 0 259
2.00-3.00 15 210 15 18 0 258
3.00-4.00 18 215 25 45 0 303
4.00-5.00 12 228 28 45 3 316
5.00-6.00 15 240 35 40 8 338
TOTAL 410 4907 600 1012 302 7231
Equivalent
PCU
1845 16,680 600 1012 227 20,364
Heavy motor vehicles constituted largest traffic volume i.e. 68% followed by light
commercial vehicles and passenger cars 14%.
M/s BEL will require 16,80,000 TPA coking coal imported, 16,05,130 TPA non-coking
coal, 19,12,173 TPA Iron ore lump, 8,00,000 TPA I/o fines, 80,417 TPA Dolomite and
1,20,870 TPA lime stone
The company has its railway siding inside project boundary and Raw material will be
transported through rail and unloaded at Rly.siding. It is expected that sometimes lime
stone and Dolomite will be transported on road using environmental compatible
Euro/Bharat II/III vehicles. Hence maximum 2 lakh TPA raw material and 1.0 MTPA,
billet will be transported through road, which translate to 3,333TPD i.e. 200 trucks/day
and taking to and from into consideration 400 additional heavy motor vehicle (1360
PCU)will be on road due to project.
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Taking 1,355 employees and their family into consideration, school going buses, it is
expected that another 2000 PCU will be on road. Although it will be on other connecting
roads, we consider 1000 PCU on NH-16., totaling 2360 say additional 2,500 PCU load on
NH-16. Total PCU load 22,864 and level of service B, being 40,000 PCU, the total load on
NH-16 will be only 50% of its rated capacity.
Design Service Volume for Four-Lane Highways in PCUs per day
Terrain Design Service Volume for Four-Lane Highways in PCUs
per day
Level of Service 'B' Level of Service 'C'
Plain and rolling 40,000 60,000
Mountainous and steep 20,000 30,000
Source: Manual of specification & standard, Planning commission, GOI
3.7 ECOLOGICAL ENVIRONMENT OF THE 10KM. RADIUS OF THE STUDY AREA:
Gen. ToR 6(x) Detailed description of Flora & Fauna (terrestrial and
aquatic) existing in the study area shall be given with special
reference to rare, endemic and endangered species. If schedule- I
fauna is found within the study area, a wild life conservation plan
shall be prepared and furnished.
3.7.1 Ecological Overview
Ecology comprises of abiotic factors as air, water, land and forces of nature like light,
gravity and molecular energy, biotic components including human beings, animals,
plants and microorganisms. The relationship among the biotic & abiotic factor is known
as Ecology.
Nature has supported and maintained life on earth since time immemorial and will
continue to do so in the future. But, once the alteration of nature’s initial stage occurs,
its ability to revert back is lost. Over the years ecological and along with it the loss of
biological diversity has become a national and a global concern. Ecological studies with
theconcern for developmentwithout dreading socio-economic and environmental
conditions and the realization that there is a limit to nature’s sustainability.One of the
important aspects of Environmental Impact Assessment in the view to conserve
environmental quality, biodiversity and sustainability.
The phyto-diversity and dynamics of vegetation of the area includes the composite
growth and development of green belt in a habitat with particular circumscription and
selected composition. It may vary from site to site even from place to place due to
fluctuation of ecological factors as the episode of the population in every moment at
every corner, like monsoon filled by herbs, shrubs, trees and parasites of varied kinds
but during winter most of the elements become vanish due to unfavorable conditions.
During summer a few of them are present due to the acclimatization in the said habitat.
The dominancy is found in case of trees rather than shrubs and followed by herbs.
Forest Cover:
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As per classification, the forest under Medinipur Forest Division Sal is the dominant
species, Sal coppice Forests, Open scrub forest with sporadic sal, open forest with
sporadic sal and thorny forest, plantations. The chief associate of Sal (Shorea robusta)
care Pterocarpus marsupium, Madhuca latifolia, Diospyros melanoxylon , Lagerstroemia
pervifolialora, Terminalia tomentosa, Anogeissus latifolia, Bombax ceiba. Adina cordifolia,
Buchanania latifola, Garuga pinnata
3.7.2 Objective:
The main objectives of ecological environmental study are:
1. To assess the nature and distribution of vegetation in and around the
study area;
2. To assess the distribution of animal life in the study area;
3. To assess the present status of geomorphology:
4. To assess the present status of water and soil quality;
5. To assess the present status meteorology:
6. To assess the biodiversity and to understand the resource potential of that
area; and
7. To understand the nature of pollution and to assess the impact of pollution
on the ecosystem.
For this study a team of Global Tech Enviro Experts Pvt. Ltd. visited the site for
identifying & collection of data. The different methods adopted for the study were as
follows:-
A. Primary data was generated through:
1. Preparing a general check list of all plants encountered in the study area and lists
all the plants by visual observations.
2. Phytological studies by using list count quadrant method and the quadrate of 100
m2 size was employed for this study.
3. Bird populations were studied by taking random reading at every location, by
naked eye, binoculars and photographs. The droppings, calls, nests also studied for
their identification.
4. Observing mammals, amphibians, and reptiles moulted skins, dropping, burrows,
pugmarks, calls and other signs.
5. Noting the status and quality of plant growth, and any symptoms like defoliation,
deformities, chlorosis, necrosis, warping, reduced vigour and infection by parasites
and insects by visual observation.
6. Aquatic body study of phytoplankton, zooplankton by plankton nets. Fish of the
aquatic bodies were studied by locating local fishermen while netting and local fish
markets.
7. Local inhabitants were interviewed about the plant and animal of the local areas.
Criteria for Site Selection
While selecting the areas for detailed studies on terrestrial and aquatic ecology following
considerations were made-
Location of the plant and the predominant wind directions
Different landscapes and land use patterns viz.
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Natural vegetation
Agri-ecosystems and surrounding areas
Water bodies- lakes and canals, ponds etc
Topography and the geology of the area
Guidelines from Ministry of Environment and Forests, Govt. of India
Based on the above parameters sampling sites were selected and sampling was carried
at different locations.
Selection of Methodology for the study:
To achieve the above objectives a detailed study of the area was undertaken in 10 km
radius area from proposed project site as centre. The flora was categorized using life-
form categories as per Raunkiaer system of Classification, as given below;
Phanerophyte : Trees & Shrubs
Chamaephyte : Herbs (Perennial, bud resting above the ground)
Hemicryptophyte : Grass
Cryptophyte : Herbs
Geophyte : Herbs, roots & shoot are storage organs
Helophyte : Grows in wet soil
Hydrophyte : Aquatic Flora
5) Theophyte : Cereals & Pulses
6) Epiphyte : Grows on another plants
7) Aerophyte : Epiphytes with no functional roots
The vegetation was classified as per Champion & Seth 5B-C Dry Sal"
1. Literature Review, Research & Published Paper
3. Websites of www.bsienvis.nic.in, www.wiienvis.nic.in
3.7.3 Floral Characteristics
The plants were surveyed, identified and taxonomical characters evaluated. The
importance value indexes for identifying the characters were determined. The study
included Quadrate method. Authenticated list is annexed in Table No.
Sampling was done on random basis. Flora like Natural Trees, Introduced Avenue and
Garden trees, Climbers, grasses and bamboos etc. and fauna like insects, butterflies,
mollusks, amphibian, reptiles, birds and mammals etc.
Plankton Analysis
The physical and chemical characteristics of water affect the abundance, species
composition, stability and productivity of the indigenous populations of aquatic
organisms. The biological methods used for assessing water quality include collection,
counting and identification of aquatic organisms; and processing and interpretation of
biological data. The work involving plankton analysis would help in:
Explaining the cause of colour and turbidity and the presence of objectionable
odour, tastes and visible particles in waters.
The interpretation of chemical analyses.
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Identifying the nature, extent and biological effects of pollution.
Providing data on the status of an aquatic system on a regular basis.
Plankton: A microscopic community of plants (phytoplankton) and animals
(zooplankton), found usually free floating, swimming with little or no resistance to water
currents, suspended in water they occur as unicellular, colonial or filamentous forms
and is mostly photosynthetic and is grazed upon by the zooplankton and other
organisms occurring in the same environment. Zooplankton principally comprise of
microscopic protozoans, rotifers, cladocerans and copepods. The species assemblage of
zooplankton also may be useful in assessing water quality.
Plankton, particularly phytoplankton, has long been used as indicators of water quality.
Because of their short life spans, planktons respond quickly to environmental changes.
They flourish both in highly eutrophic waters while a few others are very sensitive to
organic and/or chemical wastes.
Plankton net: The plankton net is a field-equipment used to trap plankton. It has a
polyethylene filter of a defined mesh size and a graduated measuring jar attached to the
other end. A handle holds the net. The mesh size of the net determines the size range of
the plankton trapped
Sampling Procedure: Plankton net number 25 of mesh size 60 µm was used for
collecting samples. 100 litres of water was measured in a graduated bucket and filtered
through the net and concentrated in a 100 ml bottle. Samples were collected as close to
the water surface as possible in the morning hours and preserved for further analysis.
The following parameters were primarily considered in the study and computed
in the following way:
5) Frequency: the degree of dispersion of individual species in an area is called
frequency. It is express as percentage occurrence.
iii) Abundance: This is the study of number of individual of different species in
community per unit area.
iv) Relative Abundance: it is the determination of the percentage of individual of one
general in composition to the total of all individual as a given area.
v) Density: I t is the numerical strength of a species.
(II) Species Diversity Index: species diversity is biological community based on presence
of a wide variety of species. It is expressed by Shannon-Weaver Index (1948) in the
following way:
Number of quadrates in which a species occurs
Frequency (f) = ------------------------------------------------------------x100
Total number of quadrates sampled
Total No. of individuals of a species in all quadrate
Abundance (A) = --------------------------------------------------------------------
Total number of quadrates in which the species occurs
Total No. of individuals species in the sample
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Relative Abundance (A) = ---------------------------------------------------------
Number of quadrat in which a species occurs
Total No. of individuals of a species in all quadrates
Density (D) = ----------------------------------------------------------------
` Total No. of quadrat sampled
Species Diversity Index: species diversity is biological community based on presence
of a wide variety of species. It is expressed by Shannon-Weaver Index (1948) in the
following way:
s
H = Σ-(Pi×lnPi)
I = 1
H = Species diversity index
S = the number of species in a sample
Pi = (ni / N)
N = the total number of individuals of all the species in a
sample
ni = the number of individuals of a species.
Simpson’s Diversity Index: (D) is a composite index, which depends both on the
number of individual species & the total number of all species, and hence, it is logically
in consonance with the definition of bio-diversity, the bigger the value of D, the lower
the diversity
Number of individual Species i
Total Numer of all species N,
(D)=1-[∑ (n i/N) 2]
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Table 3.16 Quantitative Assessment of Natural Plant species & Calculation of Biodiversity Index of Natural Plant Species
in the study area
SL NAME OF TREES
QUADRAT NUMBER
TO
TA
L
FR
EQ
UE
NC
Y %
DEN
SIT
Y
AB
UN
DA
NC
E
Pi
= n
i/N
(P
i)2
Ln
Pi
Sh
an
no
n
Div
ersit
y
In
dex
H=
-
(P
iXLn
Pi)
1 2 3 4 5 6 7 8 9 10
1 Acacia auriculaeformis 2 5 1 3 2 2 1 16 70 1.6 2.3 0.05 0.00 -3.03 0.15
2 Acacia chundra 1 1 3 1 2 8 50 0.8 1.6 0.02 0.00 -3.72 0.09
3 Albizia lebbeck 1 1 2 2 2 8 50 0.8 1.6 0.02 0.00 -3.72 0.09
4 Alianthus grandis 4 1 1 6 30 0.6 2.0 0.02 0.00 -4.01 0.07
5 Alstonia scholaris 2 1 1 4 30 0.4 1.3 0.01 0.00 -4.41 0.05
6 Anacardium occidentale 5 5 10 0.5 5.0 0.02 0.00 -4.19 0.06
7 Anogeissus latifolia 1 1 2 4 30 0.4 1.3 0.01 0.00 -4.41 0.05
8 Aphanamixis polystachya 1 1 2 4 40 0.4 1.0 0.01 0.00 -4.41 0.05
9 Arthocarpus chaplasha 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
10 Artocarpus integrifolia 2 2 10 0.2 2.0 0.01 0.00 -5.11 0.03
11 Azadirachta indica 2 2 1 4 4 3 16 60 1.6 2.7 0.05 0.00 -3.03 0.15
12 Bombax ceiba 2 2 1 5 30 0.5 1.7 0.02 0.00 -4.19 0.06
13 Bridelia retusa 1 1 2 20 0.2 1.0 0.01 0.00 -5.11 0.03
14 Buchanania lanzan 1 3 4 20 0.4 2.0 0.01 0.00 -4.41 0.05
15 Butea monosperma 5 3 11 1 2 6 5 3 36 80 3.6 4.5 0.11 0.01 -2.22 0.24
16 Callicarpa arborea 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
17 Careya arborea 1 2 3 20 0.3 1.5 0.01 0.00 -4.70 0.04
18 Cassia fistula 2 2 4 20 0.4 2.0 0.01 0.00 -4.41 0.05
19 Cassia siamia 3 1 4 20 0.4 2.0 0.01 0.00 -4.41 0.05
20 Chukrasia tabularis 1 1 2 20 0.2 1.0 0.01 0.00 -5.11 0.03
21 Dalbergia sissoo 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
22 Dillenia indica 2 1 3 20 0.3 1.5 0.01 0.00 -4.70 0.04
23 Duabanga sonneratioides 1 1 2 20 0.2 1.0 0.01 0.00 -5.11 0.03
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24 Elaeocarpus floribundus 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
25 Elaeocarpus lanceaefolius 2 2 1 5 30 0.5 1.7 0.02 0.00 -4.19 0.06
26 Emblica officinalis 1 2 1 1 1 1 7 60 0.7 1.2 0.02 0.00 -3.85 0.08
27 Eucalyptus hybrid 3 3 10 0.3 3.0 0.01 0.00 -4.70 0.04
28 Garuga pinnata 1 1 2 20 0.2 1.0 0.01 0.00 -5.11 0.03
29 Gmelina arborea 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
30 Hadina cordifolia 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
31 Heliotropium indicum 1 1 2 4 20 0.4 2.0 0.01 0.00 -4.41 0.05
32 Lagerstroemia 112ulphur 1 1 2 20 0.2 1.0 0.01 0.00 -5.11 0.03
33 Lagerstroemia parviflora 1 1 2 3 7 40 0.7 1.8 0.02 0.00 -3.85 0.08
34 Lannea coromandelica 1 1 2 20 0.2 1.0 0.01 0.00 -5.11 0.03
35 Lgterstroemia parviflora 2 3 6 11 30 1.1 3.7 0.03 0.00 -3.40 0.11
36 Macaranga sp. 2 2 1 1 6 40 0.6 1.5 0.02 0.00 -4.01 0.07
37 Madhuca Indica 2 1 3 1 2 2 3 1 15 80 1.5 1.9 0.05 0.00 -3.09 0.14
38 Mallotus philippensis 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
39 Pongamia pinnata 1 1 1 1 4 40 0.4 1.0 0.01 0.00 -4.41 0.05
40 Premna sp. 3 3 10 0.3 3.0 0.01 0.00 -4.70 0.04
41 Pterocarpus marsupium 2 2 10 0.2 2.0 0.01 0.00 -5.11 0.03
42 Pterygota alata 1 1 1 2 5 40 0.5 1.3 0.02 0.00 -4.19 0.06
43 Sapium sebiferum 1 1 10 0.1 1.0 0.00 0.00 -5.80 0.02
44 Schima wallichii 2 2 1 5 30 0.5 1.7 0.02 0.00 -4.19 0.06
45 Semicarpus anacardium 1 1 1 2 5 2 12 60 1.2 2.0 0.04 0.00 -3.31 0.12
46 Shorea robusta 3 1 2 2 1 1 2 12 70 1.2 1.7 0.04 0.00 -3.31 0.12
47 Sterculia villosa 1 2 3 20 0.3 1.5 0.01 0.00 -4.70 0.04
48 Syzygium cumini 5 2 4 11 30 1.1 3.7 0.03 0.00 -3.40 0.11
49 Syzygium jambolum 1 1 2 6 4 14 50 1.4 2.8 0.04 0.00 -3.16 0.13
50 Tectona grandis 2 3 1 6 30 0.6 2.0 0.02 0.00 -4.01 0.07
51 Terminalia alata 1 1 2 20 0.2 1.0 0.01 0.00 -5.11 0.03
52 Terminalia bellirica 1 2 1 2 2 8 50 0.8 1.6 0.02 0.00 -3.72 0.09
53 Terminalia chebula 1 1 1 1 1 5 50 0.5 1.0 0.02 0.00 -4.19 0.06
54 Terminalia elliptica 1 2 3 1 7 40 0.7 1.8 0.02 0.00 -3.85 0.08
55 Terminilia arjuna 2 2 3 4 5 1 17 60 1.7 2.8 0.05 0.00 -2.97 0.15
56 Tetrameles nudiflora 1 2 3 20 0.3 1.5 0.01 0.00 -4.70 0.04
57 Toona 112ulphur 1 1 20 0.1 0.5 0.00 0.00 -5.80 0.02
∑ 31 37 51 31 33 26 37 28 31 25 330 1750 33 99.4 1 0.04 -252.45 3.67
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Shanon’s Diversity Index H=3.67. Shanon’s Diversity Index was calculated taking 57 species of
trees in the study area with 10 quadrats
Simpson Diversity index D= 0.032624
Simpson Index is moderately nearer to one so the diversty of species in not very rich.
Discussion
78 types of terrestrial angiosperms species were encountered in the study area, 57
species were encountered in quadrat counts. The other species were among herbs 25,
grass 12, climbers 21, cultivated plants including fruit bearing ,ornamental, avenue
plantation 32. In faunal species wild types were 13, reptiles and snakes 10 and avi fauna
47 species were noted.
From the Shanon’s index it is found that the area is moderately rich in species diversity,
as the land mass is in a plain deltaic area, so most of the land is used for paddy
cultivation.
Creation of green belt and promotion of avenue plantation with fruit bearing trees may
attract more birds to increase the aesthetic.
3.8 SOCIO-ECONOMIC ENVIRONMENT
ToR 6(xi) Socio-Economic status of the study area
The growth of industrial sectors and infrastructure developments in and around the
agriculture dominant areas, villages and towns are bound to create its impact on the
socio- economic aspects of the local population. The impacts may be positive or negative
depending upon the developmental activity. To assess the impacts on the socio-
economics of the local people, it is necessary to study the existing socio-economic status
of the local population, which will be helpful for making efforts to further improve the
quality of life in the study area. The section delineates the overall appraisal of the
socially relevant attributes.
The data collection on the impact of industrialization on the socio-economic aspects in
the study area has been done through analysis of various secondary data and also
supplemented by the primary data generated through the process of limited door to door
socio- economic survey. The demographic and socio-economic profiles are collected from
the Primary Census Abstract for the district of Paschim Burdwan, West Bengal.
Methodology
The methodology adopted in the assessment of socio-economic condition is as given
below:
To evaluate the parameters defining the socio-economic conditions of the
people.Analysis of the identified social attributes like population distribution, sex ratio,
literacy rate, occupational structure, availability of public utilities etc through literature
like the census of India, District Census Statistical Handbooks and from records of
National Informatics Centre etc.
3.8.1 OBJECTIVE:
The main objectives are as follows:
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To assess the impact of the project on agricultural situation;
To examine the impact of the project on pattern of demand;
To assess the in impact of the project on consumption pattern;
To examine employment and income effects of the project;
To explore the possibility of local industrialization as an offshoot of the project;
To examine the effect of the project on education status of the people in the
study area
To judge peoples’ perception regarding the project
3.8.2 DEMOGRAPHIC PATTERN
The socioeconomic features around the 10 km radius of the plant site have been
collected through primary and secondary data collection. The study area covers 129
villages and 95622 inhabitants. Out of the total population SC population is 20.1%, ST
31.0% and other 48.9% The demographic and socioeconomic profiles are collected from
the Primary Census Abstract for the study area of district Paschim Burdwan, West
Bengal.
3.8.3 SEX RATIO
The sex ratio (nos. of male per thousand females) is 976 in the study area (based on the
Census 2011. From above representation of number of male and female of different classes
in the society in the study area, indicates that a in about 30% of the villages the population
distribution is very healthy with the ST and SC women numbers standing at par with the
male population. This distribution will give a normalized population distribution when
plotted for individual villages and hence a healthy sign of development.
3.8.4 LITERACY:
The Literacy rate of study area is 65% of the total population. The above data plot
showing the ratio of men to female literate and illeterates in the study area shows that
though the villages lack the facilities for education yet the picture of female literate (57
%) and male literate( 72 %) gives a encouraging picture of the development of the area.
Yet the literacy level is still gloomy with 35 % of the total population being illiterate.
3.8.5 OCCUPATIONAL PATTERN
The workers in the study area comprised of 52.8 % main workers, 47.1% marginal
workers and 0.1% non-workers. The main workers mainly comprise of cultivators and
agricultural labourers.
3.8.6 GAP ANALYSIS
Major source of drinking water in the villages are tube wells, dug wells and hand
pumps. In summer, there is problem of drinking water and the source of water is
handpump.
Sanitation and medical facility:
It has been found that toilet facility is almost absent in the villages and open
defaecation is prevailing. The buffer zone of the project area is ubnder the grip of
malaria.For minor health problems the village depends on Anganwadi. In some
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vill`ages dispensary, maternity home and health camp is available which are not
sufficient.
Discussion
A separate independent SIA study has been conducted to give a strong focus on the
socio-economy of the area along with the implementation of CER and CSR in future if
attracts CSR norms.
Detailed SIA study is given in Annexure VI
3.9 CONCLUSION:
The chapter has given the vivid picture of present environmental conditions of the study
area during study period. Components, like topography, land use pattern,ambient air
quality, water environment,soil characteristics,noise level, flora & fauna,traffic studies,
socio-economic environment has been described.
The ambient environmental conditions monitored has been described in this chapter
All positive and negative impacts are predicted during the construction as well as
operation phase of the project which will result in deterioration of the environment if
proper mitigation measures are not carried out. The details of the impacts and the
measures to reduce the same are addressed in the next chapter.
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CHAPTER-4
ANTICIPATED ENVIRONMENTAL IMPACT & MITIGATION MEASURE
4.1 DETAILS OF INVESTIGATED ENVIRONMENTAL IMPACTS DUE TO PROJECT
LOCATION, POSSIBLE ACCIDENTS, DESIGN, CONSTRUCTION, OPERATION,
DECOMMISSIONING OR REHABILITATION OF A COMPLETED PROJECT
Impact prediction is a way of mapping the environmental consequences of the project
development. Environmental impact can never be predicted with absolute certainty and
this is all the more reason to consider all possible factors and take all possible
precautions for reducing the degree of uncertainty.
4.1.1 Objectives of Impact Prediction
The objective of Impact Prediction for the proposed modification cum expansion project
under consideration is to identify the potential impacts on the specific site prevailing
environmental setting and degree of impacts. This will enable to draw up an appropriate
Environment Management Plan (EMP) to ensure that the proposed project activity does
not impair the present environmental setting. The findings of EIA are drafted in the form
of Environmental Impact Statement (EIS).
The following impacts of the project in general are assessed:
Climatic condition
Changes in present climatic condition such as temperature, atmospheric pressure,
Humidity & rainfall due to the pollutants emitted from the proposed project
Leads to Green house effect & Global Warming
Air
Changes in ambient levels and ground level concentrations due to total emissions
from point, line and area sources
Effects on soils, materials, vegetation, and human health
Noise
Changes in ambient levels due to noise generated from equipment and movement
of vehicle
Effect on fauna and human health
Water
Availability to competing users
Changes in quality
Sediment transport
Land
Changes in land use and drainage pattern
Changes in land quality including effects of waste disposal
Biological
Deforestation/tree-cutting and shrinkage of animal habitat Impact on fauna and
flora (including aquatic species if any) due to contaminants/pollutants
Impact on breeding and nesting grounds
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Socio-Economic
Impact on the local community including demographic changes
Impact on economic status
Impact on human health
Impact of increased traffic
The objective of having an EIA for the proposed plant under consideration is to identify
the potential impacts on the site specific prevailing environmental setting and degree of
impacts. This will enable to draw up an appropriate Environmental Management Plan
(EMP) to consider other alternatives so as to ensure that the proposed activity does not
impair the present environmental setting beyond the assimilative capacity of the region
and ambient and other environmental standards are not exceeded at any point of time.
This is because ambient standards are maintained to protect human health with an
adequate margin of safety.
4.1.2 Impact Prediction & Assessment
The description of the proposed project and the existing baseline status in the core as
well as in the buffer zone has been dealt in detail in the earlier chapters. These
information forms the basis of Environmental Impact Assessment (EIA) of the proposed
project and the same is discussed in this chapter with prediction and evaluation of these
objective of having an EIA for the proposed project under consideration is to identify the
potential impacts on the site specific prevailing environmental setting and degree of
impacts. This will enable to draw up an appropriate Environment Management Plan
(EMP) to consider other alternatives so as to ensure that the proposed project activity
does not impair the present environmental setting.
4.1.3 Pollution Potential
The plant processes like Raw material handling and product handling plant, Coke oven,
DRI kilns, MBF, EAF, IF, Sinter plant & power plant, etc. are sources of air pollution. The
sources and type of pollution in the process operation are presented in the Table 4.2. It
may be observed that heat, dusts, SO2, CO, CO2 and NOXgeneration from process&
emitted to the air environment are the prime pollution parameters from the proposed
project. However, with proper planning and innovative management technique and the
use of suitable pollution control devices, it is possible to run the manufacturing processes
without much endangering the air environment.
4.2 METHODS USED FOR THE STUDY OF ENVIRONMENTAL IMPACTS
After screening and scoping the identification of potentially significant environmental
impacts constitute one of the preliminary steps of Environmental Impact Assessment
(EIA). There are three principal methods for identifying environmental effects and
impacts; these are checklists, matrices and flow diagram.
Checklists
Checklists are comprehensive lists of environmental effects and impact indicators
designed to stimulate the analysts to think broadly about possible consequence of
contemplated action.
Matrices
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Matrices typically employ a list of human action in addition to a list of impact indicators.
The two are related in a matrix, which can be used to identify cause and affect
relationships.
Flow Diagrams (Network method)
Flow diagrams are sometimes used to identify action-effect-impact relationship. The flow
diagram permits the analysts to visualize the connection between action and impact.
This method is best suited to single project assessment and is not recommended for
large regional actions.
The proposed modification cum Expansion steel plant is a brown field project and the
actions have been planned before implementation of the project to minimize any adverse
impact small or large on environment and population. The environmental attributes that
may be affected due to the construction and operation of the proposed project are:
Air Environment
Noise Environment
Surface-water Environment
Groundwater Environment
Land environment
Biological Environment
Socio-Economic and Cultural Environment
Infrastructure
Aesthetics
The construction, operation and future activities are considered to identify the possible
impact. The matrix method has been chosen to list the potential impacts of the proposed
project. The activities have been arranged in columns and the environmental attributes
in the row of the matrix. The impact identification matrix is shown in the Table 4.1.
Introduction to Matrix Method
The identification and prediction of impacts on various environmental parameters is
followed up by quantification of impacts. There are several methods available to quantify
the environmental impacts. The Leopold matrix method is one of the most widely
adopted and has been used for quantification of impacts for this study. The methodology
involves, first, the identification of activities, which occur during the two phases of the
project and second their likely impacts on the environmental parameters.
Matrix Method
In this method, the effect of various activities on the environment is ranked on a scale of
1 to 10 based on the order of increasing importance to arrive at the Parameter
Importance Value (PIV).
The score of each parameter has been converted to a probability value and then
recalculated by multiplying each value by a factor of 1,000 so that the sum of all the
recalculated values becomes 1000. The values thus confirm to the units of the standard
scale, generally used for evaluating the degree of impact on a set of project activities on
total environment.
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The matrix used for EIA consists of project activities on the X-axis and the environmental
components likely to be effected by such activities on the Y-axis. The degree of impact
upon the environmental components due to each anticipated project activity is graded as
per the index scale given below:
SL. NO. DEGREE OF IMPACT IMPACT VALUE
1 Minimal 1-2
2 Moderate 3-4
3 Appreciable 5-6
4 Significant 7-8
5 Extreme 9-10
A (+) or (-) sign has been assigned to each value depending on its beneficial or
detrimental effect. The environment impact has been framed with the four major project
activities as column in X-axis and 14 environmental components as rows in Y-axis. The
PIV values for each row as determined in Table.4.9, is placed at the first column. An
appropriate impact value based on judicious subjective assessment is assigned to each
of the project activity. The impact score for each environmental component (SC1) have
been calculated as under:
n
SCI = (PIV)iIij
J=i
Where is the impact value (on a scale of 1.0 to 10.0 positive or negative) due to the
effect of a project activity (j) on the environmental component (i).
The n= total number of project activities.
The Total Impact Score (TIS) is arrived at as follows:
n
TIS = (PIV)ISci
I=1
Where n= Total number of environmental components.
The Total Impact Score (TIS) is determined as per the procedure outlined above. The
score has been evaluated against the following Assessment Value Index Scale:
Up to (-) 2000 No appreciable impact on environment. Adverse impact minimal.
(-) 2000 to (-) 4000 Appreciable impact on environment but not injurious in general.
Adequate mitigating measures are important.
(-) 4000 to (-) 6000 Significant impact upon the environment. Major environmental
control measures to be taken.
(-) 6000 to (-) 8000 Major injuries impact on environment. Site selection to be
considered
(-) 8000 and above Alternative site to be considered.
Up to (+)2000 Minimally beneficial.
Up to (+)4000 Moderately beneficial.
Up to (+)6000 Appreciably beneficial.
Up to (+)8000 Significantly beneficial.
(+)8000 and above Extremely beneficial.
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Table 4.1: Parameter Impact Value of Environment Components
Environment
Components
Importance
Rank
Weight age
(W)
Parameters
Importance Value
(PIV)= W X 1000
Soil 1 1/38 26
Resource 3 3/38 79
Water 1 1/38 26
Air 2 2/38 53
Terrestrial flora 2 2/38 53
Aquatic Biota 0 0 0
Terrestrial fauna 0 0 0
Economic 9 9/38 237
Education 5 5/38 132
Public Order 3 3/38 79
Infrastructure & services 1 1/38 26
Security & Safety 4 4/38 105
Health 2 2/38 53
Cultural 5 5/38 132
Total 38 1000
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Table 4.2 Impact Identification Matrix for M/s Bengal Energy Ltd
Environment
Component
PIV
Burn
ing of
Waste
s,
Refu
ge &
Cle
are
d V
egeta
tion
Site
Pre
para
tion/
Change
in
Topogra
phy
Civ
il
Work
s
such
as
Eart
h
Movin
g
&
Buildin
g
of
Str
uctu
res
Inclu
din
g
tem
pora
ry S
tructu
res
Heavy E
quip
ment
Opera
tion
Dis
posal
of
Constr
uction
Waste
s
Genera
tion o
f Sew
age
Influx
of
Constr
uction
Work
ers
Defo
resta
tion
Tra
nsport
ation o
f M
ate
rial
Ere
ction o
f Equip
ment
Raw
Mate
rial use &
Handling
Em
issio
n
from
M
eta
llurg
ical
Pro
cesses
Efflu
ent
from
M
eta
llurg
ical
Pro
cess
Solid
Waste
fr
om
Meta
llurg
ical Pro
cess
Wate
r Extr
action
for
Meta
llurg
ical Pro
cess
Em
plo
ym
ent
genera
tion
Energ
y U
se &
Dem
and
To
tal
TIS
Sco
re
Soil 26
-1 -2 -2 -1 -1
-7 -182
Resource 79
-1 -2 -1 -1 -1 -1 -2 -1 -1 -1 -1 -1 -14 -1106
Water 26
-3 -1 -3 -1
-8 -208
Air 53
-1 -2 -1 -3 -1 -8 -424
Terrestrial flora 53
-2 -2 -1 -5 -263
Aquatic Biota 0
0 0
Terrestrial fauna 0
0 0
Economic 237
+1 +1 +1 +1 +2 +2 +2 +1 -2 -1 -1 +2 +4 +10 2370
Education 132
+2 +2 +2 +2 +8 1056
Public Order 79
-2 -2 -2 -2 -2 -10 -790
Infrastructure &
services 26 -1 -1
-2 -52
Project
activity
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From the matrix table Total impact score (TIS) is found to be “-227” which means as there will be no appreciable impact or minimal
adverse impact on the environment. However, with adequate mitigating measures the degree of beneficial impact will be higher.
_ Negative or adverse Impact
+ Positive or beneficial Impact
Security & Safety 105
-1 -1 -1 -2 -1 -1 -1 -1 -2 -11 -1155
Health 53
-1 -1 -1 -1 -1
-5 -265
Cultural 132
+1 +2 +2 +1
+6 792
Total
-227
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4.3 IMPACT PREDICTION & MEASURES FOR MINIMISING AND/OR
OFFSETTING ADVERSE IMPACT IDENTIFIED.
The description of the proposed expansion of the existing Coke oven plant of M/s Bengal
Energy Ltd, Paschim Medinipur, West Bengal and the baseline status in the core as well
as in the buffer zone has been dealt in details in the earlier chapters. These information
forms the basis of impact prediction and assessment component of Environmental
Impact Assessment (EIA) of the proposed project and the same is discussed in this
chapter and the evaluation of these impact is described in subsequent chapter.
4.3.1 IMPACTS DURING CONSTRUCTION PHASE:
Construction activity will constitute excavation, civil construction and mechanical
erection. Transportation of various construction materials and stockpiling them will also
be a major activity. These activities will be of transient nature and its impact on
environment will be of significance during construction phase only. Several temporary
measures will be taken during construction period to minimize the impact.
Site Development:
Site development is one of the prime activities for any project. This activity mainly
involves clearing of the land from all hindrances to bring the site to a condition of
starting construction work. As the expansion project will be carried out in the existing
land of the plant and the site is mostly developed for Industrial purpose, there will be no
significant impact due to site development.
Civil & Structural Work:
This work can be divided into two groups, foundation work and structural work. Certain
foundation work may involve pile-driving rigs etc. these activities may generate noise
pollution. Besides, foundation work will involve excavation and concreting work. Dust
pollution, especially during dry season, will be the major problem unless appropriate
measures are adopted to contain/ minimize the dust nuisance. The structural work will
involve steel, masonry work etc. and will involve use of equipments like hoists, cranes,
mixers, welding machines etc. there may be dust & noise pollution from this work.
During construction stage water will be required for dust suppression, civil construction
and domestic purposes. So the dust emission and noise will pose some impact on
Environment. However, the dust emission will be controlled by water sprinkling. Noise
will be controlled by adoption of adequate preventive measures like acoustic covering
and use of PPE; By taking adequate precautions the impact due to fugitive emission and
noise will be reduced to negligible level.
Mechanical & Electrical Erection:
The mechanical erection work involves extensive use of mechanical equipment for
storage, retrieval and erection, site fabrication etc. leading to considerable noise
pollution and air pollution to some extent. Pollution from Electrical work, however, is
negligible.
Source of construction materials:
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For any project construction, the requirement of cement, stone chips and sand is
inevitable. These Construction materials are available locally and as the volume of civil
construction is less, the impact due to this activity will be less.
Air Environment:
Civil work and erection of structures are undertaken during construction phase. These
construction activities along with transportation of construction material generate
fugitive dust. Welding of different structures also produce gases. But these dusts are
inorganic in nature and are generated at ground level. Due to the heavy nature of these
dusts, these are not expected to be carried over to long distance to cause inconvenience
to surrounding people. The impact on ambient air quality due to fugitive dust generated
during construction period is not permanent in nature, and will cease with the completion
of construction activity. The bulk of civil work is expected to be completed within 12
months. With the completion of construction phases, the impact on air quality due to
fugitive dust will be minimized. However water sprinkling on roads can bring fugitive
emission under control
Water Environment:
The water requirement during construction activity will be met by existing water
supplies. Debris and other solid wastes are expected to be generated during construction
period and during monsoon with the surface runoff, the debris will be washed away
contributing suspended solids in nearby stream. This will be minimized through provision
of temporary garland drains around the dumping site of debris. Again, this is temporary
in nature and will cease with the completion of the construction work. The impact on
water environment during construction phase is also temporary in nature.
Noise Environment:
The general noise levels due to construction activities such as welding, fabrications and
erection of MBF, DRI Kilns, EAF, IF, rolling mill, & Power plant may sometimes go up to
80-90 dB (A) at the work sites during day time for very shot interval. The workers in
general are likely to be exposed to an equivalent noise level of 65 – 75 dB (A) in 8-hour
shift for which statutory precautionary measure as per the law will be taken. No noisy
work will be performed during night time.
Land Environment:
The proposed project site is acquired and converted to industrial premises, so there will
not be any vegetation loss or tree cutting and will also have small impact on the land use
pattern.
Soil Environment & Solid Waste:
During construction phase, solid waste such as excavated soil, debris, metal cutting,
cotton waste, oil and grease from machineries/vehicles used in construction etc. will be
generated. These wastes may contaminate soil at plant site temporarily and would be
restricted to a small area.
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Certain hazardous wastes such as; used oil filter & used oil etc. will be generated during
constructional activities. These are hazardous in nature but their quantity will be very
less. This will be seggrated and stored in shed. The generation of solid waste during
construction phase will be temporary in nature and will be confined to the construction
site only. Hence the impact due to this will be insignificant, reversible and short term in
nature.
Socio-economic environment:
The construction activity will help in infusing a large amount of funds in that area and
thus will generate a lot of employment, both direct and indirect. The socio-economic
conditions will improve during construction phase of the project.
This might also result in a steep rise in agricultural wages in the surrounding villages,
especially at the time of harvesting for short duration. Hence, short-term positive
impacts on socio-economic conditions of the area are anticipated during the construction
phase.
ToR 10 Details regarding infrastructure facilities such as sanitation,
fuel, restroom etc. to be provided to the labor force during
construction as well as to the casual workers including truck drivers
during operation phase.
The overall purposes of sanitation are to provide a healthy living environment for
everyone, to protect the natural resources (such as surface water, groundwater, soil),
and to provide safety, security and dignity for people when they defecate or urinate.
Existing plant has all sanitary infrastructures for its employees, casual workers, truck
drivers transporting raw material and product to and out of the existing running project.
There is a subsidized canteen with hygienic environment to cater tea, snacks and meals
to all concerned including visitors.
Sanitary MSW disposal system, soak pit and STP exist for the existing system. Bath
rooms, latrines separate for gents and ladies with regular cleaning and sanitation exists
for workers and temporary workers. There are rest rooms with attached bath and latrine
for people working in night shift or continuing two shifts.
There is a first aid center with pharmacists for free checkup, free medicine and first-aid
provision for its employees with ambulance facility during emergency
All these existing infrastructure facilities will be extended to additional work force of
expansion project.
There will be no need of burning fossil fuel by contractor workers for cooking purpose as
canteen coupons will be issued to them through registered contractors. If situation so
demands gas cylinders will be provided to them on chargeable basis.
4.3.2 MITIGATING MEASURES DURING CONSTRUCTION PHASE
Mitigating Measures for Site Development:
Site Development for expansion of M/s. BEL. has no significant impact as the proposed
plant has been planned inside the existing plant premises.
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Mitigating Measures for Civil & Structural Work:
During construction stage water will be sprinkled. Noise will be controlled by adoption of
adequate preventive measures. By taking adequate precaution the impact due to fugitive
emission and noise will be reduced to negligible level.
Mitigating Measures for Air Quality:
The impact on ambient air quality due to fugitive dust generated during construction
period is not permanent in nature, and will cease with the completion of construction
activity. However, use of tarpaulin for covering the material being transported in trucks,
sprinkling of water will control the dust emission and proper maintenance of vehicle and
use of Euro/Bharat- III/IV vehicles will reduce emission. With the completion of
construction phase, the impact on air quality due to fugitive dust will be minimized and
this impact is reversible in nature.
Mitigating Measures for Water Environment:
During monsoon with the surface runoff, the debris will be washed away to contribute a
lot of suspended solids in nearby pond. This will be minimized through provision of
temporary garland drains around the dumping site of debris. Water consumption and
discharge of wastewater is not likely to have any significant impact on the water
environment during construction phase. Again, this is temporary in nature and will be
ceased with the completion of the construction process. Moreover, storm water run-offs
will occur only during the monsoon which last for about three months in the study area.
Domestic effluent generated from labour camp will be treated in septic tank and will be
discharged to soak pit.
Mitigating Measures for Noise Pollution:
The workers in general are likely to be exposed to an equivalent noise level of 80-90 dB
(A) in 8-hour shift for which all statutory precautions as per the law will be implemented.
Uses of proper personal protective equipments like earplugs, earmuffs etc shall further
mitigate any adverse impact of noise on the construction workers. By using standard
practice of operation, these impacts can be minimized and made insignificant. Impacts
on the noise levels will be temporary for short duration and reversible in nature. As far
as possible noisy work during night time will be avoided.
Mitigating Measures for Soil Quality & Solid Waste:
The excavated top soil will be stored near boundary and will be used for back filling/road
work/bund preparation/landscaping. The other wastes will be collected and segregated
and will be disposed of properly without causing any public nuisance
The management, handling & disposal of this hazardous waste will be carried out in
accordance with the Hazardous Waste (Management and Handling) Rules, 1989 and
amendment thereof.
Table 4.4: Action Plan for Excavation and Muck Disposal during Construction
Sl.
No.
Solid Waste Generated Action Plan
1. Excavated soil for preparation of
foundation work of buildings and
machineries.
Will be kept aside near the boundary wall
for later use for filling of low-lying areas.
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2. Leveling of Site Top soil removed during leveling of the site
will be kept aside for development of
Green Belt & land scaping.
3 Metal scrap generated due to
fabrication of equipments.
The scrap will be stored in scrap yard for
use/sale.
4 Debris generated during the
Construction.
Will be suitably disposed in low lying areas.
5 Muck or sludge generated due to
piling jobs.
Will be transferred nearer to boundary wall
to be used later as filling material in low
lying areas.
Mitigating Measures for Ecology Impact:
M/s Bengal Energy Ltd has already developed green belt along boundary line and within
its existing premises, which will be further extended. The Greenbelt will be helpful in
constricting the noise & dust.
Mitigating Measures for Socio-Economic Impact:
General health check- up facilities will be provided to the nearby areas from the plant
side and some work facilities will be given to the non-workers that may contribute to
direct or indirect employment.
4.3.3 IMPACTS DURING OPERATIONAL PHASE
With the commissioning of the steel plant with other ancilliary facilities, the impacts both
beneficial and adverse are anticipated on ambient air quality, noise quality, land use,
water quality, soil, ecology and socioeconomic environment. The impact on
environmental components have been discussed below.
Impact on Air Environment
The impact on Air environment of an Integrated Steel Plant depends on various factors
like production capacity, plant configuration, process technology, type of raw materials,
type of fuel, in plant control measures adopted, operation and maintenance of the
various units of the plant. Apart from these, there will be other activities associated e.g.,
transportation of raw material and finished products, storage facilities and material
handling within plant premises which may contribute to air pollution.
The steel plant is likely to have effect on air quality parameters like PM10, PM2.5, SO2,
NOX and CO. The raw material handling plant, metallurgical units and other downstream
ancilliaries will emit dust and fumes. Apart from the above there will be fugitive dust
emissions due to transportation, storage and processing of of ores and minerals as raw
materials. Needless to say, the adequate air pollution control measures will be taken up
both at design and operational stage to confirm the emission parameters within the
prescribed standards.
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A- Fugitive emission
ToR 7(vi) Measures for Fugitive Emission Control
a)Primary Fugitive Emission
During operations, fugitive dust emissions may associate with
Delivery of raw materials to site;
Storage of different minerals;
Processing
Operation of the stockpiles and reclamation;
Transportation of by-products off site;
Vehicle movements Slag processing;
Handling of collected flue dust from APCs
b)Secondary Fugitive Emission
Secondary fugitive emission like dust and fume from DRI kilns, steel melting shop
comprising of IF& MBF, Sinter plant.
The major concern is SO2 for the operation of AFBC. Sulphur is an input to the process
via the coal and is distributed between ash and off gas with the majority of the sulphur
ending up in the off gas, predominantly in the form of H2S under normal operating
conditions. The primary control mechanism is the use of a lime scrubber unit to scrub all
exhaust gas prior to release to atmosphere. With low Sulphur of South African coal or
even blending with Indian coal lime scrubber is not envisaged.
Measures for fugitive emission control
Following mitigation measures will be taken up.
1) Haulage internal roads are black topped. Automatic water sprinklers to be
installed by the side of roads.
2) Mobile water tankers will be deployed to sprinkle water on leading road to plant
outside main gate & railway line side gate.
3) Dry fog system to be provided to material transportation conveyors.
4) Three tire green belt along the boundary wall, by the side of internal roads and
around material handling plant
5) Bag filter with suction swivel hood for control of fugitive emission at material
loading 7 unloading station.
6) Material transportation will be done fully covered with tarpaulin
B Emission from process
Emitting Stacks are major sources of air pollution in the proposed expansion.Particulate
matter, SO2, NOX will be emitted from different unit operations.
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Measures for emission control during operation phase
Emission of particulate matter, SO2,NOx will have adverse effect on human health and
environment as a whole. There fore it is required to take measures to keep emissions
within prescribed standards. Details of proposed measures have been given in Table 4.5
below.
Gen.Tor 3(vi) Details of Emission, Effluents, Hazardous Waste and
their Management.
Gen.Tor 7(v) Details of Stack Emission and Action Plan for Control of
Emission to Meet Standards.
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Table 4.5: Details of predicted stack emission from proposed expansion Project
Facility Stack Height(m)
Top dia (m)
Temp(K) Velocity (m/s)
Flow rate(m3/hr)
PM mg/Nm3
PM gm/s
SO2 mg/Nm3
SO2 gm/s
NOx gm/s
APC equipment
1x500 TPD DRI Kilns
50 2.6 393 9.15 1,75,000 44.24 2.15 286.00 13.9 - DSC, ABC, ESP & high stack
1x500 TPD DRI
Kilns
50 2.6 393 9.15 1,75,000 44.24 2.15 286.00 13.9 DSC, ABC, ESP &
high stack
2x350 TPD DRI Kilns
60 2.8 393 11.05 2,45,000 44.26 3.01 285.88 19.44 - 2 DSC, ABC, ESP & single high stack
1x0.6 MTPA Coke-Oven
60 3.8 413 11.0 4,60,000 20.34 2.6 194.00 24.78 - WHRB & high stack
1x0.6 MTPA Coke-Oven
60 3.8 413 11.0 4,60,000 20.34 2.6 194.00 24.78 WHRB & high stack
2x80T EAF 30 3.6 340 10.0 3,81,650 80.18 8.5 - - - 2 Bag filters & single stack
3x20T IF 30 2.5 340 8.4 1,43,115 88.05 3.5 - - 2 Bag Filter & single stack
1x60m2 Sinter Plant
55 2.0 393 8.6 96,780 37.77 1.02 24.6 16.8 ESP & stack
1x320m3 MBF 30 2.0 313 6.94 78,500 50.00 1.09 - - Dust catcher,
Ventury scrubber, emergency venting flare stack with
water seal
1x320m3 MBF 30 2.0 313 6.94 78,500 50.00 1.09 - - Dust catcher,
Ventury scrubber, emergency venting flare stack with water seal
1x35 MW AFBC 62 2.6 413 11.0 2,12,000 40.00 2.36 38.1 WHRB & ESP
DRI material Handling Plant
30 1.5 310 8.0 50,200 500.00 7.0 - - Bag filter & stack
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A. Model input: Source input parameter
The different point source input parameters in the form of stack and emission data are
considered.
Stack emissions are major sources of air pollution from the proposed plant. The
proposed expansion steel plant is to be provided with necessary air pollution control
devices like Electro Static Precipitators (ESP), bag filters, dust catchers, ABC, ventury
scrubber& lime scrubber etc to control dusts and gases and also limit emission within the
prescribed standard. The emission factors, air handling capacity of the proposed
installation and emission norm has been used to estimate amount of emission from the
proposed plant with the height of emission. Particulate emission is based upon the Air
Pollution Control Device (APCD) with design stack emission limited to norms specified by
CPCB.
Model input parameters: Control options
The options used for short term computations are:
The plume rise is estimated by Briggs formulae, but the final rise is always
limited to that of the mixing layer;
Buoyancy Induced Dispersion is used to describe the increase in plume
dispersion during the ascension phase;
Calms processing routine is used by default;
Wind profile exponents are used by default.
Flat terrain is used for computations;
It is assumed that the pollutants do not undergo any physico-chemical transformation
and that there is no pollutant removal by dry deposition.
Briggs rural dispersion coefficient has been considered 24 hours averaging are taken into
consideration.
Gen.Tor 7(i) Assessment of ground level concentration of pollutants
from the stack emission based on site-specific meteorological
features. In case the project is located on a hilly terrain, the AQIP
Modelling shall be done using inputs of the specific terrain
characteristics for determining the potential impacts of the project on
the AAQ. Cumulative impact of all sources of emissions (including
transportation) on the AAQ of the area shall be well assessed. Details
of the model used and the input data used for modelling shall also be
provided. The air quality contours shall be plotted on a location map
showing the location of project site, habitation nearby, sensitive
receptors, if any.
Year Month Day Hr.(1-24) CL.
Cover DBT RH PR WD WS MH
2017 12 27 1 1 20 58 1010 360 8.2 302
2017 12 27 2 0 19 58 1011 360 9.2 286
2017 12 27 3 0 19 59 1012 360 10.3 210
2017 12 27 4 0 19 59 1012 360 11 137
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2017 12 27 5 0 20 58 1011 360 11.5 91
2017 12 27 6 0 20 57 1010 360 12 80
2017 12 27 7 0 21 56 1011 360 9.3 75
2017 12 27 8 0 21 55 1010 360 8.5 280
2017 12 27 9 0 20 54 1010 135 5.2 460
2017 12 27 10 0 21 53 1009 45 3.1 590
2017 12 27 11 0 22 52 1011 45 1.2 680
2017 12 27 12 0 23 51 1009 45 0.4 810
2017 12 27 13 0 23 50 1008 45 0.4 980
2017 12 27 14 1 22 50 1008 45 0.4 1042
2017 12 27 15 1 22 51 1009 45 0.4 983
2017 12 27 16 0 21 52 1010 90 0.4 835
2017 12 27 17 0 21 53 1010 90 3.6 740
2017 12 27 18 0 20 54 1011 135 7.5 690
2017 12 27 19 0 19 56 1012 180 9.8 652
2017 12 27 20 0 20 56 1011 180 10.6 580
2017 12 27 21 0 19 54 1010 225 11.2 515
2017 12 27 22 0 20 55 1011 270 12 490
2017 12 27 23 0 20 56 1010 315 10.5 420
2017 12 27 24 0 19 57 1011 315 9.4 386
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Table 4.6 Assessment of GLC of pollutants without APC equipments
Location Name
GLC for PM10 (µg/m3) GLC for PM 2.5(µg/m3) GLC for SO2(µg/m3) GLC for Nox(µg/m3)
Monitored
GLC
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Monitore
d
G
LC
at
sam
pling s
ite
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Monitore
d
G
LC
at
sam
pling s
ite
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Monitore
d
G
LC
at
sam
pling s
ite
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Keshuriya 80.2 14.88 95.1
35.2 13.88 49.1
9.6 6.91 16.5
12.6 14.88 27.5
Bargopal 79.7 3.72 83.4 35.5 3.47 39.0 9.4 6.91 16.3 12.6 4.96 17.6
Daharpur 85.8 29.77 115.6 39.5 27.77 67.3 9.5 20.73 30.2 18.2 14.88 33.1
Nutandihi 74.2 26.4 100.6
32.6 24.29 56.9
17.0 48.36 65.4
17.3 39.69 57.0
Silti 77.1 29.77 106.9 36.3 27.77 64.1 8.4 20.73 29.1 16.3 24.81 41.1
Belti 74.8 22.38 97.2 32.9 17.35 50.3 9.0 27.64 36.6 15.6 29.77 45.4
Salkha 76.4 7.44 83.8 33.8 3.47 37.3 8.7 0 8.7 15.0 0 15.0
Mirjapur 75.8 7.44 83.2 33.4 6.97 40.4 8.2 0 8.2 17.5 4.96 22.5
NAAQS STANDARD
100 60 80 80
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B. Impact of Pollutants on human health
CO2 currently forms about 405 parts per million (ppm) of earth’s atmosphere, compared
to about 280 ppm in pre-industrial times, and billions of metric tons of CO2 are emitted
annually by burning of fossil fuels.CO2 increase in earth’s atmosphere has been
accelerating oxidation of SO2, usually in the presence of a catalyst such as NO2, forms
H2SO4, and thus acid rain. This is one of the causes for concern over the environmental
impact of the use of these fuels as power sources.
Nitrogen oxides, particularly nitrogen dioxide, are expelled from high temperature
combustion, and are also produced during thunderstorms by electric discharge. They can
be seen as a brown haze dome above or a plume downwind of cities. Nitrogen dioxide is
a chemical compound with the formula NO2. It is one of several nitrogen oxides. One of
the most prominent air pollutants, this reddish-brown toxic gas has a characteristic
sharp, biting odor. Annual premature European deaths caused by air pollution are
estimated at 430,000. An important cause of these deaths is nitrogen dioxide and other
nitrogen oxides (Nox) emitted by road vehicles. In a 2015 consultation document the UK
government disclosed that nitrogen dioxide is responsible for 23,500 premature UK
deaths per annum. Across the European Union, air pollution is estimated to reduce life
expectancy by almost nine months. Causes of deaths include strokes, heart disease, lung
cancer, and lung infections.
Particulates, alternatively referred to as particulate matter (PM), atmospheric particulate
matter, or fine particles, are tiny particles of solid or liquid suspended in a gas. In
contrast, aerosol refers to combined particles and gas. Some particulates occur naturally,
originating from volcanoes, dust storms, forest and grassland fires, living vegetation,
and sea spray. Human activities, such as the burning of fossil fuels in vehicles, power
plants and various industrial processes also generate significant amounts of aerosols.
Averaged worldwide, anthropogenic aerosols—those made by human activities—currently
account for approximately 10 percent of our atmosphere. Increased levels of fine
particles in the air are linked to health hazards such as heart disease, altered lung
function and lung cancer.
Impact on Water Environment:
ToR 7(ii) Water quality modeling-in case, if the effluent is proposed to
be discharged into the local drain, then water quality modeling should
be conducted for the drain water taking into consideration the
upstream and downstream quality of water of the drain.
Waste water generated from process will be settled, treated, filtered and reused or
recycled where ever applicable. Some waste water will be utilized in green belt watering
and dust suppression through sprinklers. No effluent will be discharged outside plant
boundary. Hence zero discharge norm will be followed and therefore water quality
modeling not done.
ToR 7 (iii) Impact of the transport of the Raw materials and end
products on the surrounding environment shall be assessed and
provided. In this regard, options for transport of raw material and
finished products and wastes (large quantities) by rail or rail cum
road transport or conveyor-cum-rail transport shall be examined.
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Majority of raw material and product shall be transported through rail. The company has
its railway siding inside project boundary and Raw material will be transported through
rail and unloaded at Rly.siding. It is expected that sometimes lime stone and Dolomite
will be transported on road using environmental compatible Euro/Bharat II/III vehicles.
Hence maximum 2 lakh TPA raw material and 1.0 MTPA, billet will be transported
through road, which translate to 3,333 TPD i.e. 200 trucks/day and taking to and from
into consideration 400 additional heavy motor vehicle (1360 PCU)will be on road due to
project.
1 km length of NH 16 was considered for monitoring traffic study starting from Plant
main gate. As because the entrance opens to NH 16.
Impact on Traffic
Road traffic to and from the plant during operation of expanded plant will be heavier
than at present as envisaged mode of transport of the materials is via road.
Traffic density will be increased marginally as a result of expansion. In turn, it will
contribute to noise as well as ambient air quality in term of dust and other gaseous
pollutants. The regular maintenance of vehicles and transport of materials under cover,
will limit the pollution within limits. The present road conditions are reasonably good for
proposed movement of traffic.
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Impact on Ecology:
The proposed expansion unit will be set up in the existing premises. Designated area will
be considered as solid waste dumping site. No waste water will be drained outside plant
boundary. Hence not much of impact on ecology is anticipated.
Socio-economic Impacts:
It is rather obvious that nearby villages will have more impact (adverse or beneficial),
therefore the study area was divided into three zones with 3 km, 7 km & 10 km radius
with central point of the combined project site as the centre to assess the socioeconomic
impact of the project on the surrounding environment.
The manpower requirement for the proposed project will generate some permanent jobs
and secondary jobs for the operation and maintenance of plant. This will increase
direct/indirect employment opportunities and ancillary business development to
appreciable extent for the local population. This phase is expected to create a beneficial
impact on the local socio-economic environment.
Depending on requirements employees are called in different shifts and few employees
are called on duty in national/ festival holidays and off days. The licensed capacity of the
unit is 1000.
Educational Status
The local educational levels will be raised with additional facilities provided to schools
through various CSR programs, such as scholarships, awareness programs, child care
facilities, and cultural events, self help groups and community participation in area
developments.
Impact on Public Health and Safety
Discussion with the medical officers reveals non-existence of major disease in the study
area. Health awareness among the villages may grow especially regarding cleanliness
with the industrial development.
4.3.4 MITIGATION MEASURES DURING OPERATION PHASE
Mitigation measures for Ground water:
Until recently it was a common myth that groundwater is pristine i.e. potential
contaminant percolating through the subsurface would adhere to the soil or be degraded
by natural process and therefore would not enter or greatly affect groundwater quality.
Thus, the groundwater was regarded as a safe and convenient depository for the waste
and non-waste by-products, generated by the society.
However, with the passage of time and increasing number of serious incidences, there is
a growing concern of groundwater pollution. Raw material of the project will be stored on
compact pure clay mixed with Bentonite layer covered with HDPE layer therefore there will be no
seepage from the raw material piles. Again, the material will be stored under shed so as to
prevent the leachate through runoff.
Mitigating Measures for Air Environment:
The impacts of primary air pollutants on air quality due to emission from single source or a
group of sources is evaluated by use of mathematical models. Needless to say, the adequate
air pollution control measures like ESPs, bag filters,dust catchers, Lime scrubber, ventury
scrubber ID Fan and stack will be installed to reduce impact to a larger extent.
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Air pollution control at different point source
The proposed steel plant will emit gases and fumes which will have negligible impact after
pollution control management on human health, animals, vegetation and material. Here
under, action plans are proposed to address the pollution problem to meet the NAAQS 2009
Standard.
Stacks will be provided with porthole and working platform so that stack monitoring can
be done as per norms of statutory authority and proper Air Pollution Control Devices
shall be installed. On line stack monitoring and tripping of process with failure of
pollution control equipment has been proposed to be interlocked.
The isopleths diagrams after providing efficient equipments to arrest particulate matter is
given in Fig below:
Gen. Tor 7 (i) Assesment Of Ground Level Concentration Of Pollutants
Table 4.7 The GLC values after implementation of APC systems are
Location Name
GLC for PM10 (µg/m3) GLC for PM 2.5(µg/m3)
GLC for SO2(µg/m3) GLC for NOx(µg/m3)
Monitored
GLC
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Monitore
d
G
LC
at
sam
pling s
ite
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Monitore
d
G
LC
at
sam
pling s
ite
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Monitore
d
G
LC
at
sam
pling s
ite
Pre
dic
ted
incre
menta
l G
LC
from
isople
th
Maxim
um
Resultant
GLC
Keshuriya 80.2 0.56 80.8 35.2 1.16 36.4 9.6 7.58 17.2 12.6 14.88 27.5
Bargopal 79.7 0.28 80.0 35.5 0.66 36.2 9.4 3.79 13.2 12.6 4.96 17.6
Daharpur 85.8 1.68 87.5 39.5 1.16 40.7 9.5 15.16 24.7 18.2 14.88 33.1
Nutandihi 74.2 1.96 76.2 32.6 1.32 33.9 17.0 22.74 39.7 17.3 39.69 57.0
Silti 77.1 1.41 78.5 36.3 1.32 37.6 8.4 22.74 31.1 16.3 24.81 41.1
Belti 74.8 1.12 75.9 32.9 1.16 34.1 9.0 18.95 28.0 15.6 29.77 45.4
Salkha 76.4 0.28 76.7 33.8 0.99 34.8 8.7 0 8.7 15.0 0 15.0
Mirjapur 75.8 0.28 76.1 33.4 0.99 34.4 8.2 0 8.2 17.5 4.96 22.5
NAAQS STANDARD
100 60 80 80
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ToR-7(vii)Details of hazardous waste generation and their storage,
utilization and disposal. Copies of MOU regarding utilization of solid
and hazardous waste shall also be included. EMP shall include the
concept of waste-minimization, recycle/reuse/recover techniques.
Energy conservation and natural resource conservation.
The various types of solid waste encountered from an Integrated Steel
Plant are:-
A. Municipal Solid Waste
B. Hazardous Waste
C. Industrial Waste
a. A. Municipal Solid Waste
Very small amount of Municipal Solid waste will be generated from canteen& Guest
House which will be converted to compost through Organic Waste converter and will be
utilized as manure in green belt.
b. B. Industrial Waste
Add ToR 8 Plan for slag utilization
Table 4.3 Solid Wastes utilization & disposal measures
Solid waste Quantity in TPA Utilisation measures
EAF & IF slag 1,20,000 Use in construction work
IF flue dust 24.000 Will be sold to Metal recovery Agencies
DRI Dolchar 2,72,000 Use in AFBC to generate steam for power
plant
Fly ash 13,78,050 Sold to Gava Ecocrete Pvt Ltd
BF slag 1,84,760 Sold to ASO Cement Ltd
BF sludge + dust 2,93,670 Sold to ASO Cement Ltd
Power plant Bottom
Ash
1,00,500 Sold to Gava Ecocrete Pvt Ltd
In case of excess BF slag and sludge over sale, this can be used as raw material for iron
ore sinter making.
Fly Ash Management
Total Fly ash generation from CPP has been estimated to be 13,78,050 which will
be supplied to Gava Ecocrete Pvt Ltd as per their greement.
All the request letter are annexed as Annexure VII
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Bottom Ash Management
Total Bottom ash generation from CPP has been estimated to be 1,00,500 TPA which will
be supplied to Gava Ecocrete Pvt Ltd as per their agreement letter.
C. Hazardous Waste
Hazardous Waste Management
Table 4.9 Hazardous Waste Management
Sl.
No.
Type of
Hazardous
Wastes
Schedule Source of
Generation
Unit of
Measurem
ent
Quantity
Generated
/Annum (
approx )
Mode of Disposal
1 Used Grease
5.2
Moving equipments Kg 500
Stored temporarily
and being lifted by
Authorized Vendor.
2 Used Oil
Filters
35.1 Compressors, power
packs, vehicles. Nos. 70
Stored temporarily
and being lifted by
Authorized Vendor.
3
Waste
Jute/Cotton
& Used PPE's
like Gloves,
shoes etc .
5.2
Use for cleaning
machines Kg 200
Stored temporarily
and being lifted by
Authorized Vendor.
4 Used Bag
Filters
Bag houses Nos./Kg. 110/550
Stored temporarily
and being lifted by
Authorized Vendor.
5 Oily Sludge
34.4
Power Pack Rooms Kg 40
Stored temporarily
and being lifted by
Authorized Vendor.
6 Used Oil
5.1
Transformer and all
Mechanical Engines KL 6.2
Being stored in
containers and will
be sold to
Authorized vendors.
ToR-7(viii)Proper utilization of fly ash shall be ensured as per Fly ash
Notification, 2009.
Fly Ash Management
Total Fly ash generation from CPP has been estimated to be 13,78,050 which will
be supplied to Gava Ecocrete Pvt Ltd as per their greement.
Total Bottom ash generation from CPP has been estimated to be 1,00,500 TPA
which will be supplied to Gava Ecocrete Pvt Ltd as per their agreement letter.
4.4 EMP AT DESIGN STAGE
Technological Improvement
For this steel plant the technologically viable, less energy intensive, less polluting route has
been chosen. With advanced technology in emission reduction and energy conservation will
be taken in to consideration, while selecting the suitable design. Some of the important
design considerations at the design & implementation stage are as follows.
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A proper layout plan has been chosen for the optimum utilization of the available
land and resources.
The design aims at minimum use of water.
Conservation of water through waste water treatment, recycling & reuse.
Zero discharge norms proposed with proper planning and its implementation.
Efficient dust extraction, dust suppression and dust collection measures have
been planned in the design of plant equipment to reduce the dust emission
considerably.
Noise emission control.
The noise producing equipments will be designed with dynamic balancing and
vibration dampening by proper grouting so as to produce minimum noise.
The operation control rooms and pulpits would be provided with noise shield
walls.
4.4.1 ENVIRONMENTAL MANAGEMENT PLANT (EMP) AT CONSTRUCTION
STAGE:
Site Preparation:
The project site preparation requires some leveling activities. During dry weather conditions,
dust may be generated by activities like excavation and transportation through un-metallic
roads. The dust will be suppressed using water sprinkling. As soon as construction is over the
surplus earth should be utilized to fill up low-lying areas, the rubbish should be cleared and
all un-built surfaces reinstated. Appropriate vegetation should be planted and all such areas
should be landscaped.
For Maintaining Water quality
During construction, volume of debris & mud will be generated, which during the rainy
season, can contaminate the storm water run-offs with suspended solids. Efforts will be made
to reduce the suspended solids content of storm water run-offs by routing the storm water
drains through catch pits. Moreover, storm water run-offs will occur only during the monsoon
season which lasts for about 2-3 months in the study area. These impacts will be temporary
lasting only during the construction period of the proposed plant. Pathways for pollution via
seepages, evaporation, residual remains are to be studied for surface water will be done after
running of expansion project
For Maintaining Air Quality
During the construction phase, civil work will be carried out to put the units in place. The
construction work leads to generation of fugitive dust. However, the fugitive dust is not
expected to spread too far. Water spraying will be undertaken to suppress dust. Due to
construction activities, impacts on ambient air quality will not be permanent and will cease
once the construction is completed.
To Maintain Noise Level in the Vicinity
The construction equipment will be chosen by criteria of environmental friendly
technology and shall generate less noise level. Noise levels during the limited
construction period are likely to increase initially due to increased movement of trucks
and other diesel-powered material handling equipment. This is unavoidable and limited
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during day time only. The movement of trucks and machinery will be regulated to reduce
the impacts of increased noise. The construction phase will be limited to short period.
Hence it is temporary. Therefore, the impact on ambient noise levels will be insignificant
and ceases once the construction is completed.
Ecological Aspects
The construction activity won’t affect the surrounding ecology of the proposed steel plant
as the construction is well confined within the site premises.
4.4.2 ENVIRONMENTAL MANAGEMENT PLANT (EMP) AT OPERATIONAL
PHASE
Air Environment Management:
There will be dust & Gas Emission from IF and material handling site. With use of Swivel
Hood, Bag Filter & Stack this emission will be appreciably reduced & there by Air
Pollution will be under control.
The dust generated in the material handling system will be extracted through suction
hoods located at various drop points. The hoods will be connected to a common duct
which will be provided with a motorized damper for isolation. An on-line booster fan will
be provided for generating the necessary suction at the suction hoods.
Air pollution Control devices proposed for the project
E S Ps
M/s Bengal Energy Ltd proposes ESPs for control of dust emission for DRI kilns, sinter
plant and captive power plant.
Charged or emitting electrodes will be connected to 66KV DC. 220V AC will be stepped
up to 66KV and converted through rectifier to DC. Dust collecting plates will be earthed.
Emitting electrodes will be placed between collecting electrodes and equidistance from
them.
Inlet duct of ESP will have gradual expansion and perforated diffuser plate to reduce
pressure to facilitate dust separation and equal distribution of gas to all rows. Corona
discharge will create drift or migration velocity by charging dust particles and pushing
them towards collecting electrodes.
Deposited dust over collecting electrodes will be periodically dry cleaned by automatic
hammering process and collected dust from bottom hopper of ESPs will be pneumatically
conveyed to storage bunker for disposal.
Gas outlet duct is gradually narrowed down to inlet duct size and pressure is recovered.
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ESP dust separation efficiency is minimum 99%, the area of collecting plates ‘A’ is
calculated using Anderson-Deutsch equation.
ฑ= 1-e- Vpm A/Q, whereฑis efficiency of ESP
1) ESP for each 500 TPD DRI kiln
A = ln(1-0.99)/-(Vpm /Q) = 4.605/- (Vpm /Q)
Where A = area of ESP plates taken together, Dust migration velocity Vpm= 0.2m/s
(assumed) and Q= volumetric flow in Nm3/sec
Q= 1,10,260Nm3/hr=30.62Nm3/s, Vpm= 0.2m/s, ฑ=99%
Area of collecting plates A= 4.605/0.0065= 708m2&takingdesign safety factor 1.5
times = 1062m2
With plate height of 9m, the total plate length is estimated as 118m
ESP can have 10 rows with plate length of each row =12m
2x500 TPD DRI Kilns will have 2 ESPs, 2 ID fans but single stack
2)ESP for each 350 TPD DRI kiln
Q=21.44 Nm3/s,Vpm /Q =0.0093 & A=495m2 and taking 1.5 times=743m2
So ESP will have plates of 9m height, 9 rows and plate length of each row=10m
2x350 TPD DRI Kilns will have 2 ESPs, 2 ID fans but single stack
3)1x60m2 Sinter plant
Q=27 Nm3/s, Vpm /Q = 0.0074 & A=622m2 and taking 1.5 times=933m2
So ESP will have plates of 9m height, 9 rows and plate length of each row=12m
The sinter plant will have one ESP, one ID fan and one stack.
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4) ESP for 1x35 MW AFBC power plant
Q=59Nm3/s, Vpm /Q =0.0034 & A=1,354m2 and taking 1.5 times=2032m2
So the ESP will have plates of 9m length, 12 rows and each row of 18m length
One ESP, one ID fan and one stack.
Bag filters
Bag filters have been proposed for EAFs and IFs
Bag Filters
Pulse jet bag filter has been proposed with bag material needle felt polyester, hence Air
to cloth ratio i.e. dust migration velocity Vfhas been taken as 5m/min.
1) Bag filter for 1x20T IF
Gas flow rate of each IF, Q=460Nm3/min,
Ac, Area of filter cloth = Q/Vf= 92m2 and taking design safety factor 1.5times the
calculated value, area of cloth comes to 138m2
Filter media cloth will be stitched to cover a cylindrical MS wire cage with circular
bottom. Dimension of each bag diameter=15cm and length 3.6m, Area of cloth for each
cage=1.7m2 with additional margin for folding inside at connection of bag with Ventury.
Number of bags required will be 82 bags. As 2/3 of bags will be under service and 1/3
under cleaning at a time, total bags will be 123. The bag filter will have 9 rows and each
row will have 14nos of bags. There will be two chambers, Dust separation chamber and
plenum chamber. Dust laden flue gas will enter into separation chamber; pass through
needle felt polyester bags due to suction of ID fan. Dust will be retained on surface of
bags and clean gas will enter into plenum chamber and finally vented through stack due
to discharge of ID fan.
Differential pressure gauge between two chambers will give performance of filtering
media. When dp across is high the pulse jet will operate through timer action and clean
bags. During cleaning of bags dust will be deposited in bottom hopper of bag house and
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will be removed through Rotary air lock valve and pneumatically conveyed to storage
bunker or recycled to process.
For 3x20T IF, there will be 3 nos of bag filters, 3nos of ID fans but single stack with two
EAFs.
2)Bag filter for 1x80T IF
Gas flow rate of each EAF, Q=1840Nm3/min,
Ac, Area of filter cloth = Q/Vf= 368m2 and taking design safety factor 1.5times the
calculated value, area of cloth comes to 552m2
Filter media cloth will be stitched to cover a cylindrical MS wire cage with circular
bottom. Dimension of each bag diameter=15cm and length 3.6m, Area of cloth for each
cage=1.7m2 with additional margin for folding inside at connection of bag with Ventury.
Number of bags required will be 326 bags. As 2/3 of bags will be under service and 1/3
under cleaning at a time, total bags will be 489. The bag filter will have 21 rows and
each row will have 23nos of bags. There will be two chambers, Dust separation chamber
and plenum chamber. Dust laden flue gas will enter into separation chamber; pass
through needle felt polyester bags due to suction of ID fan. Dust will be retained on
surface of bags
Additional Tor-6 All Stock Piles Will Have to be on Top ofa Stable Liner
To Avoid Leaching Of Materials To Ground Water.
The raw materials at the RMHP site will be stored on a platform made up of pure clay
mixed with bentonite and covered by HDPE liner to avoid leaching of materials.
Moreover, the raw materials will be stored under a shed to avoid the contact with rain
water.
Water Management
ToR 7(iv) A note on treatment of waste water from different plant
operation, extent recycled and reused for different purposes shall be
included. Complete scheme of effluent treatment, characteristics of
untreated and treated effluent to meet the prescribed standards of
discharge under E(P) Rule.
Waste Water Management
As the plant water system is designed based on maximum recirculation system and
effective discharge from plant will be insignificant. The effluents likely to be generated
from the proposed plant are:
Backwash Waste from Filtration Plant;
Run-off water from Raw Material Storage Yards;
Waste Water from Billet Caster;
Cooling tower blow-down of various shops; and
Plant Sewage & Canteen Effluents.
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The first step towards a healthy waste water management is to separate the waste
stream from the storm water Stream.
The storm water will have a separate route leading to the rain water harvesting pond
with proper pretreatment scheme before entering to the rain water harvesting pond &
the waste water stream will be routed separately to the treatment unit or Effluent
Treatment Plant (ETP).
TREATMENT OF INDUSTRIAL EFFLUENT
The Effluent Treatment Plant is designed on the basis of the following effluent
characteristics.
PARAMETERS UNIT RAW
EFFLUENT
TREATED
EFFLUENT
SPCB
Standard
Flow M3/HR 100 100
pH - 6.00-9.00 7.00-8.5 6.5 – 8.5
Turbidity NTU 60 <15 -
Oil & Grease PPM 31.2-21.9 < 5 10 mg/l
Total Suspended Solids PPM 1000-5000 <30 100 mg/l
Process Description of the Waste Water Treatment
The effluent from the plant will be screened through the mechanical screen & will
pass to the grit chamber for settling of the heavier & big size particles. The grits
will be pumped through a heavy-duty pump to the sludge tank. The overflow
from the Grit Chamber will be pass to the Oil & Grease tank for separation of Oil
& Grease in the initial partition through a oil skimmer. The skimmed oil & grease
will be kept in a separate tank for further disposal / use.
The Oil & Grease separated effluent will be passing to the Equalisation tank,
which is provided with air agitation for further transfer of effluent to the Flash
Mixer. In the flash Mixer the effluent will be added with lime solution for
precipitation of heavy metals if any & Poly electrolyte of appropriate dose will be
added for faster coagulation in the flocculation zone of the clarifloculator provided
after the Flash Mixer. The solids will be settled in the clarifloculator as sludge &
removed as under flow to the sludge tank. The Overflow of the clarifloculator is
clarified clear water & will be transferred to the clear water tank for further reuse
in the plant.
The sludge from the sludge tank will be fed to the filter press for separation of
solid & water.
STORM WATER MANAGEMENT
Storm water is generated during rainy season due to rainfall. The rain water will flow to
the rain water harvesting pond for storage of rain water. As the storm water passes
through different areas so it may collect pollutants like Suspended Solids, oil & Grease
etc. So before entering to the pond the storm water should pass through the screen ,
Grit Chamber & oil & Grease trap. The details of the schematic flow diagram is given
below
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The various control measures are:
Backwash from Filtration Plant will be led to a sludge pond for removing
suspended solids. The overflow from the sludge pond will be used for dust
suppression and irrigation of green cover. The sludge from the sludge pond will
be dried and dumped in low lying area.
Run-off water from the raw material storage yard will be routed through drains to
catch pits to settle out suspended solids. The clear water will be discharged into
natural drainage channels.
Cooling Tower Blow-down and Boiler Blow-down will be utilized for dust
suppression in the raw material handling area and IF slag cooling.
Efforts to be made to reuse most of the water in the plant itself. This water comes
under the category of ‘Waste Liquor’ and has to be treated to render it harmless.
Backwash from Filtration Plant will be led to pits for removing suspended solids.
The overflow from the pits will be reused in the plant water system. The sludge
from the pits will be dried and dumped. Effluents from the SMS are likely to
contain suspended solids and oil & grease. These effluents will be routed to
settling pits fitted with oil & grease trap. The clarified water will be reused in the
plant.
Cooling Tower Blow-down from various recirculation systems will be cascaded for
reuse in other qualitatively compatible systems. Thus, proposed plant will recycle
water to the maximum extent possible. The Blow Down water from various plant
units will be collected along with the drainage water and used for Dust
Suppression by Spraying and for gardening purpose.
All storm water drains from the raw materials and solid waste handling areas will
be routed through garland drains into catch pits of sufficient volume to settle out
suspended solids present in the storm water run-offs. The clear water will be
discharged into natural drainage channels. This type of effluent is anticipated only
in monsoon. The sewage from the Plant and Canteen waste water will be treated
in Sewage Treatment Plant. The treated sewage will be diverted for irrigation of
green cover.
The proposed plants would require industrial water on a continuous basis for
process requirement, cooling purposes, cleaning/scrubbing purposes etc. In order
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to minimize consumption of fresh water from the source, industrial water after treatment
is proposed to be recycled and reused. After cooling and suitable treatment
makeup water will be added to compensate for the losses in closed circuit
circulation system.
The company is following the ZLD for its existing plant and will propose ZLD for
this expansion project. The water will be required in the steel plant for SMS plant:
Roof and panel cooling, Electrode cooling system requirement and Cast mould
cooling.
ToR-7(x) Action plan for rain water harvesting measure at plant site
shall be submitted to harvest rain water from roof top and storm
water drain to recharge the ground water and also to use for the
various activities at the project site to conserve fresh water and
reduce the water requirement from other sources.
4.5 RAIN WATER HARVESTING
Run Off Water Management during Monsoon/ Post Monsoon Period
M/s. BEL plans to have water rain water harvesting ponds to collect the storm water and
rain water particularly during the monsoon and will use the same for plant purposes as
and when required.
Part I construction:
Rain Water Harvesting Tank
Area=20 ha
Intensity of rainfall=60 mm
Runoff quantity=20*0.06*0.50 ham=0.60 ham
60 % of the above=0.6*0.6 ham=0.36 ham=3600 cum
Capacity of each water harvesting tank:
Fort recharge-2350 cum
So, no. of water harvesting tank required=2
Similarly, in Part II, III & IV 3, 2 & 2 nos. of water harvesting tank would be required.
A. Expected quantum of recharge
Sl
No
Structures Qty Recharge capacity Total quantum of
recharge in cum
Remarks
1 Traditional dug
well
4 10% of volume per
day
4X16X12=768 120 days of
monsoon period
considered
2 Recharge pit 20 0.12 cum per rainy
day
20X0.12X70=168 70 days of
monsoon period
considered
3 Rain water
harvesting tank
2 50mX50mX4m 20000cum
4 Recharge tube well 12 5000*cum 60,000 120 days of
monsoon period
considered
80,936 cum
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B. Part II Expected quantum of recharge 1,05,978 cum
C. Part III Expected quantum of recharge 98,294 cum
D. Part IV Expected quantum of recharge 95,894 cum
Total recharge potential of RWH=3,81,102 cum
Rain water harvesting pond
About 5.20 ha of land has been allocated to store rain water for plant use so that make
up water drawl can be reduced.
The discharge water quality will be as per IS: 2296 for surface water discharge standard.
PH - 6.5-8.5
Suspended solid - <100mg/l
BOD <30mg/l
COD <250mg/l
Iron <0.3mg/l
4.6 MAINTENANCE OF POLLUTION CONTROL EQUIPMENTS:
The Pollution Control Equipment will be examined and maintained in annual shutdown.
• As a measure of preventive maintenance sets of ESP plates and filter
bags for bag filters will be kept ready to meet any eventuality of mal
performance of equipment in position.
• Condition based maintenance also will be taken up.
Noise Pollution Management
During normal operations of the plant, noise levels will increase significantly only close to
the turbines/compressor but this will be confined only within plant boundary. However
noise levels will increase during bleeding-off of excess steam. But such incidents are
occasional and will last only for few seconds at a time only. The noise level within the
plant boundary is occupational noise levels and confined within shops. The level will be
further minimized when the noise reaches the plant boundary and the nearest residential
areas beyond the plant boundary, as elaborate green belt development is envisaged for
all along the boundary for attenuation of noise and fugitive emission. All the equipment
in the steel plant will be designed/operated in such a way that the noise level shall not
exceed 85 dB (A) as per the requirement of Standard.
In the proposed plant, the primary sources of the noise pollution are compressors, turbo
generator & crushers. The noise pollution management will be taken up in following
manner
By selecting low noise generating equipment, which would have below 75 dB at
1m distance. This is taken care at the equipment design stage.
By isolating the noise unit from the working personnel’s continuous exposure by
providing acoustic aids for plant personnel.
By administrative & safety measures, providing noise level monitoring, remedial
measures, providing noise safety appliances.
The noise impact on the surrounding environment during the construction phase
will be within acceptable limits. The operation of high noise generating
equipment shall be restricted during the night time.
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Various measures proposed to reduce noise pollution include reduction of noise at
source, provision of acoustic lagging for the equipment and suction side
silencers, selection of low noise equipment and isolation of noisy equipment &
proper maintenance and lubrication. The plant personnel in noisy area will be
provided with PPE such as ear muffler & also the duration of exposure of the
personnel will be limited as per the norms.
Thick green belt development is planned for the attenuation of noise pollution and
to maintain ambient noise quality within the statutory limit.
Raw Material Handling
Solid waste generated in the raw material handling area is particulate matter. This is
collected using de-dusting equipment like Bag Filters and routed back into the process.
Measures For Improvement Of Ecology:
There is no wildlife sanctuary within the 10 km radius of the proposed plant. There will
not be any loss of plantation because of the project. The resultant ambient air and noise
quality levels after the operation of the plant will be within the prescribed limits to have
any impact on surrounding flora and fauna. Moreover there will not be any wastewater
discharge and solid waste disposal to outside the factory premises to cause any impact
on the local ecology. On the other hand the company will provide the comprehensive
green-belt cover in 33 % of the project area as per the MoEF norms to improve the local
ecology. All these steps will considerably improve upon the ecology of the area.
The company in principle shall adhere to
Plantation program will be undertaken in all available areas. This will include
plantation along the plant boundary, in the proposed plant premises, along the
internal and external roads, on solid waste dump yards and along the
administrative building and the stacking yards.
People will be educated and trained in social forestry activities by local
governmental and non-governmental organizations.
Plantation in residential and industrial areas will be done along the narrow and
broad internal roads. This will not only improve the flora in the region but also
add to the aesthetics of the region.
ToR-7(ix) & Specific ToR(vi) Action plan for the green belt
development plan in 33% area i.e. land with not less than 1,500 trees
per ha. Giving details of species, width of plantation, planning
schedule etc. shall be included. The green belt shall be around the
project boundary and a scheme for greening of roads used for the
project shall also be incorporated.
4.8 GREEN BELT DEVELOPMENT
Green vegetation cover is beneficial in many ways leading to conservation of
biodiversity, retention of soil moisture, recharge of ground water and maintaining
pleasant micro climate of the region. In addition, vegetation cover can also absorb
pollutants from the environment and helps in effective pollution control.
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Green belts are planned open spaces safeguarded from developmental activities such as
construction of buildings, factories, dams, etc. Safeguarded in the sense that no
infrastructural development will be allowed on such designated areas and these areas
will only be used for growing vegetation cover on it. Green belts in and around urban
and industrial areas are important to the ecological health of any given region.
As on Date Plantation Status
Sl. No. Year of
Plantation
Type of Trees No.s
Planted
Area of Plantation Ha of Land
for
Plantation
Cost of
Plantation
in Lakhs
1 2009-2010 Debdaru, Akasia,
Krisnachura, Jujuba 18,600
Along boundary wall-Tier I 12 14.88
2 2010-2011 Kadam, Gamhar, Bottle
brush, Jhaun 15,000
Along boundary wall-Tier II 10 12.00
3 2011-2012 Mango, Jack fruit,
Sisoo, 22,500
Internal roads, Raw Material
Handling 15 24.75
4 2012-2013
Sheesum, Neem, Arjun,
Chatim, Debdaru,
Kamini
7,500
Along Conveyor belt
carrying raw material to
Coke oven
5 9.37
5 2013-2014 Chikoo,Mango,
Arjuna,Chatiman 10,500
Along Coke oven plant 7 13.65
6 2014-2015 Debdaru, kadam,Arjun,
Neem 4,500
Around RWH pond, Internal
roads 3 6.52
7 2015-2016 Replenish the dead trees
- 1.25
8 2016-2017
Akasia, Kanchan,
Neem, Pyara, Jamun,
Kamini
6000
Along railway siding
4 15.00
9 2017-2018 Neem, Debdaru,
Jackfruit 2000
Along Coke oven plant - 16.96
10 2018-2019 Replenish the dead trees - 0.75
Total 11216
56.0 115.13
PROPOSED TARGET
Dead plants will be replenished in coming years.
4.9 SOCIO-ECONOMIC DEVELOPMENT
The proposed plant site has been chosen primarily because of its proximity to the raw
material source and infrastructure facilities. The benefits include;
• Generation of employment;
• Establishment of small and medium scale engineering ancillaries, with cascading
employment opportunities;
• Increased revenue to the state by way of taxes and duties;
• Improved green cover;
• Better communication and transport facilities;
• Better educational facility
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• Improvement in health care sector
The proposed project shall enhance the prospects of employment. Recruitment for the
unskilled workers for the proposed plant will be from the nearby villages. The
development of the basic amenities viz. roads, transportation, electricity, drinking water,
proper sanitation, educational institutions, medical facilities, entertainment, etc. will be
developed as far as possible.
The company shall give special emphasis on skill development of unemployed youth of
the surrounding locality. With the help of Govt. agencies and local NGOs they will pursue
the unskilled youth for augmentation of their skill by undergoing onsite training during
construction and operation phase in order to develop skilled workforce pool. The
surrounding Industries will also be persuaded with the help of govt. department to
develop such work force./ Apprentice trainees will be provided with stipend and
encourage to undertake skill development training during construction and operation
phase so that they can get engagement in the company.
4.10 IRREVERSIBLE AND IRRETRIEVABLE COMMITMENTS OF ENVIRONMENTAL
COMPONENTS
A resource commitment is considered irreversible when impacts from its use would limit
future use options and the change cannot be reversed, reclaimed, or repaired.
Irreversible commitments generally occur to nonrenewable resources such as minerals or
cultural resources, and to those resources that are renewable only over long-time spans,
such as soil productivity.
A resource commitment is considered irretrievable when the use or consumption of the
resource is neither renewable nor recoverable for use by future generations until
reclamation is successfully applied. Irretrievable commitments generally apply to the loss
of production, harvest, or natural resources and are not necessarily irreversible
Although not all of the 161.87 ha of M/s BEL plant site would actually be developed, it is
likely that the entire site would be unavailable for other uses, once the project comes
into operation. However, after the operational life of the project is over and the plant
and linear facilities have been decommissioned and reclaimed, the land would again be
available for other uses. Therefore, during the lifespan of the project, land use would
experience an irretrievable impact.
Existing facilities would be cleared, graded, and filled, as needed, to suit construction of
the project. These actions would result in additional impacts that are irreversible and/or
irretrievable. Existing vegetation and soils would be removed, causing mortality of some
wildlife, such as burrow-dwelling species and slow-moving species that are unable to
relocate when ground-disturbance activities begin. In addition, the vegetation and soil
habitats would be lost for future use by wildlife until reclamation could be successfully
implemented. The direct mortality of wildlife would be an irreversible impact and the loss
of habitat would be an irretrievable impact.
The loss of top soil, which requires a very long time to generate would constitute an
irreversible and irretrievable resource commitment; however, reclamation would likely
include replacing any lost topsoil and not relying on natural soil-producing processes.
Therefore, it is likely that the soil removal would ultimately be an irretrievable impact but
not irreversible.
It has been proposed to store this valuable resource which is excavated during
construction stage and reused in green belt etc. Again fly ash generated from the project
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will be used as brick in construction work, so that conventional use of making brick from
topsoil and burning and damaging it can be avoided.
Process water would be used primarily in the cooling towers, which would convert the
water to vapor. Potable water used during construction and operations would be
discharged through a septic system. the project would not directly discharge any of the
process or potable water to source of surface water. Rain water to be harvested and
used in the process or can be charged to ground water table.
4.11 ASSESSMENT OF SIGNIFICANCE OF IMPACTS (CRITERIA FOR
DETERMINING SIGNIFICANCE, ASSIGNING SIGNIFICANCE)
The last step in the impact assessment process is determining the magnitude and
significance of impacts. This determination provides decision makers with the
information needed to determine if a project should be approved or modified in some
way that would make impacts acceptable.
Impact magnitude depends on the degree and extent to which the project changes the
environment and usually varies according to project phase. In general, most project
impacts are associated with construction and operations. Site characterization has fewer
impacts and decommissioning and reclamation impacts are relatively short-lived and
should result in an improvement in conditions relative to the operational period.
Determining the significance of impacts can be one of the most difficult aspects of an
impact assessment. Quantification of impact magnitude is typically an objective,
scientifically based process. But once impact magnitude is determined, the analyst must
decide on the significance of those impacts. Decision makers typically consider only the
significant impacts in deciding among alternatives. Significant impacts will be the focus of mitigation measures and possible adjustment of project features.
Factors to consider in determining impact significance often parallel those factors used to
determine impact magnitude. These factors include but are not limited to:
Area of Influence: Impact significance is often directly related to the size of the
area affected. An example would be the acres of land disturbed.
Percentage of Resource Affected: The greater the percentage of a resource
affected, the more significant the impact.
Persistence of Impacts: Permanent or long-term changes are usually more
significant than temporary ones. The ability of the resource to recover after the
activities are complete is related to this effect.
Sensitivity of Resources: Impacts to sensitive resources are usually more
significant than impacts to those that are relatively resilient to impacts.
Status of Resources: Impacts to rare or limited resources are usually
considered more significant than impacts to common or abundant resources.
Regulatory Status: Impacts to resources that are protected (e.g., endangered
species, wetlands, air quality, cultural resources, water quality) typically are
considered more significant than impacts to those without regulatory status. Note
that many resources with regulatory status are rare or limited.
Societal Value: Some resources have societal value, such as sacred sites,
traditional subsistence resources, and recreational areas. Note that some of these resources also have regulatory status.
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Category of impact
Small Impact: This is an impact that is limited to the immediate project area,
affects a relatively small proportion of the local population (less than 10%), and
does not result in a measurable change in carrying capacity or population size in
the affected area.
Moderate Impact: This is an impact that extends beyond the immediate project
area, affects an intermediate proportion of the local population (10 to 30%), and
results in a measurable but moderate (not destabilizing) change in carrying
capacity or population size in the affected area.
Large Impact: This is an impact that extends beyond the immediate project
area, could affect more than 30% of a local population, and could result in a
large, measurable, and destabilizing change in carrying capacity or population size in the affected area.
Factors to consider in determining impact magnitude include but are not limited
to:
Area of Influence: The impact magnitude is often directly related to the size of
the area affected. In this case 10km radius of BEL project site.
Overlap Between Area of Influence and Resource of Interest: The impact
magnitude is often directly related to the area of overlap between resources and
the overall area of influence for the project.
Deviation from Current or Baseline Conditions: For projects that affect air or
water quality, how much would concentrations of contaminants increase. For
projects that result in a large influx of workers, what is the current capacity of
housing, schools, and other support services?
Project Duration: Magnitude is often directly proportional to the lifespan of the
project, beyond which it is likely to have much less impact.
Sensitivity of the Resources: Some species appear to be very sensitive to
disturbance whereas others are fairly tolerant of disturbance (e.g., many plant
species adapt to disturbance).
Project Timing: Project activities that occur during periods of sensitivity (e.g.,
nesting season, high-precipitation periods) have greater impacts than at other times.
Quantifying Impacts
Impact magnitude is usually quantified on the basis of the factors listed above. Simple
calculations (e.g., summing area of influence, calculating areas of overlap between
resources and area of influence, determining project duration) or complex mathematical
models (e.g., modeling changes in water concentrations or air emission dispersions) are used to quantify impacts.
Often, the magnitude of impacts cannot be readily quantified. This can result from
incomplete data or a poor understanding of the effect the project will have on resources.
In these cases, professional judgment is usually used to describe in qualitative terms
what the magnitude of impacts would be.
When determining impact magnitude, conservative assumptions are often used.
Examples of conservative assumptions include assuming that all plants and animals in
the project footprint will be killed, that the project will result in a fairly high decrease in
property values, and that emission control features will be some percentage below
design levels. Sometimes a “worst-case” situation is assumed. The purpose of using
conservative assumptions is to ensure that impacts are not underestimated.
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Conservative assumptions can sometimes result in unrealistically high estimates of
impact magnitude. The use of professional judgment in identifying assumptions is
essential to ensure that the results are conservative but not unrealistic.
Even with conservative assumptions, impacts that are poorly understood (e.g., the
response of resources to the environmental changes brought about by the project is not
known) can be underestimated or improperly characterized. Conservative assumptions
can result in greatly overestimating impacts and unnecessary costs for a project
if mitigations are not properly directed and scaled to the impact.
Monitoring programs are usually developed to determine or verify the impacts to various
resources. An important component of any monitoring program will specifically address
uncertainties. Resolving uncertainties will be important for future related projects, fine-tuning of operations, and refinement of a mitigation strategy.
For M/s BEL; significance of impact has been taken on 10km radius of project site and
dispersion model of PM10, PM2.5, SO2 and NOx has been made using software and
concentration of these pollutants of different villages have been shown on isopleths in
this chapter and impacts have been found to be within allowable limit, with installation of pollution control equipments.
CONCLUSION
This chapter described details of predicted environmental impacts due to the project,
measures for minimising and offsetting adverse impact identified during construction
phase as well as operational phase along with EMP at design stage and operational
phase.Estimation of APC devices, rain water harvesting structures, green belt
development. If the industry doesn’t fit to the present technology & location related to
environmental and social aspects then there is a need to select a better technology and
alternate site where it will be most suitable for setting the industry.
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CHAPTER-5
ANALYSIS OF ALTERNATIVES (TECHNOLOGY & SITE)
M/s Bengal Energy Limited is running its project on 161.87 ha of land at-Dauka, in
Paschim Medinipur district of WB. At present the unit has a 0.6 MTPA coke oven plant
and 40 MW power plant based on waste heat recovery from its coke oven gas.
The company is proposing its expansion to manufacture 1.0 MTPA steel billet, generate
205 MW power from waste heat recovery and AFBC completely utilizing char from DRI Kilns.
The process route of steel billet production is DRI Kiln-MBF-EAF/IF-LRF. This route is well
established and proven and many steel plands in the country and abroad are successfully
running on this route. No alternative technology/ new technology has been proposed for the project.
No alternative has also been proposed for the project, as the expansion will be carried
out on available vacant space of the existing 161.87 ha of land. The land is adequate for 1.0 MTPA billet manufacturing project.
CONCLUSION
It is well appraised that the technology considered and the location selected fulfils the
criteria for the expansion project, but then follow up action is needed, by
periodic/continuous monitoring of various aspects of environment, finding out deviations
from permissible limit and corrective measure for sustainability of project and
environment. This aspect need to be dealt in next chapter.
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CHAPTER-6
ENVIRONMENTAL MONITORING PROGRAMME
M/s Bengal Energy Ltd is at present running with 0.6 MTPA Non-Recovery Coke Oven
Plant and 40 MW captive Power Plant.
The company is now proposing expansion to become 1.0 MTPA Integrated Steel Plant
with 1.2 MTPA Non-recovery Coke Oven and 205 MW Power Plant within the existing
plant premises.
The company has already chalked out a comprehensive Environmental Monitoring
Program for sustainable targeted production for existing unit and this will be extended to
the expansion units also.
6.1 TECHNICAL ASPECTS OF MONITORING THE EFFECTIVENESS OF
MITIGATION MEASURES
Regular monitoring of environmental parameters like air, water, noise and soil as well as
performance of pollution control facilities and safety measures in the plant are important
for proper environmental management of any project. Therefore, the environment and
safety cell has already been formed to handle monitoring of air and water pollutants as
well as the solid wastes generation & utilisation as per the directiveof State Pollution
Control Board and Central Pollution Control Board. Proposed monitoring schedule for
environmental parameters is given in the table below.
6.2 ADVANTAGES OF MONITORING
Monitoring of various parameters will be carried out regularly to:
Find out pollution level inside the plant and in nearby area in 10km radius buffer
zone, at specified monitoring stations to compile data and know the trend for
remedial measure.
Monitoring data gives clear indication of plant health.
Find out efficiency level of pollution control measures adopted and scope for
improvements.
Laboratory Facilities
The company has an Environmental laboratory to analyze important pollution parameters
like pH & BOD of water, analysis of raw material, product, noise monitoring near various
equipments etc. However, NABL/MoEF Accredited laboratory is being outsourced for
periodic monitoring of stack flue gas, ambient air quality, surface and ground water
quality and other various parameters.
Gen.ToR-7(xii)& Specific ToR(iv) Action plan for post project
environmental monitoring shall be submitted.
Depending upon prevailing predominant wind direction AAQ monitoring stations have
been decided where monitoring instruments shall be installed for measuring polluting
parameters at regular intervals.
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Pollution load is normally high during winter days and predominant wind direction in
project buffer zone is North and North East. Hence following villages in South and South
West direction at different distances from project site and having settlements have been
selected for installing regular monitoring stations.
Infact isopleth of pollutants at these stations show comparatively higher value than
other locations.
6.3 SAMPLING LOCATIONS
Sl.
No.
Locations Distance
(Km)
Direction w.r.t
project
1 Daharpur 5.89 S
2 Nutandih 5.54 SW
All Pollution control equipment will be provided with separate electricity meter
and totalizer for continuous recording of power consumption.
The amperage of the ID fan will also be recorded continuously. Non-functioning of
Pollution control equipment will be recorded in the same logbook along with
reasons for not running the Pollution Control Equipment.
The safety cap/emergency stack of rotary kiln type plant, which is generally
installed above the After-Burner Chamber (ABC) of feed end column will not be
used for discharging untreated emission, bypassing the air pollution control
device.
In order to prevent bypassing of emissions through safety cap and non-operation
of ESP or any other pollution control device, software controlled interlocking
facility has been proposed to be provided on the basis of real time data from the
plant control system, to ensure stoppage of feed conveyor, so that, feed to the
kiln would stop automatically, if safety cap of the rotary kiln is opened or ESP is
not in operation. The system should be able to take care of multiple operating
parameters and their inter relations to prevent any possibility of defeating the
basic objective of the interlock. The system should be foolproof to prevent any
kind of tempering. The software based interlocking system, proposed to be
installed by industry should be get approved by the concerned State Pollution
Control Board, for its adequacy, before installation by the industry.
Stack Emission from de-dusting units All de-dusting units should be connected to
a stack having a minimum stack height of 30 m. Sampling porthole and platform
etc. shall be provided as per CPCB emission regulation to facilitate stack
monitoring. De-dusting units can also be connected to ABC Chamber and finally
emitted through common stack with kiln off-gas emissions. Fugitive Emission The
measurement may be done, preferably on 8-hour basis with high volume
sampler. However, depending upon the prevalent conditions at the site, the
period of measurement can be reduced.
Siting Guideline for Sponge Iron Plants Siting of new sponge iron plants has been
as per State Pollution Control Board guidelines.
i. Residential habitation (residential localities/ village) and ecologically and/or
otherwise sensitive areas: A minimum distance of at least 1000 m (1.0 km)
has been maintained. The location of Sponge Iron Plant is more than 500 m
away from National Highway and State Highway.
ii. Radial distance between two Sponge Iron Plants is more than 5 km for plants
having capacity 1000 TPD or more.
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iii. Sponge Iron Plants can be established in designated industrial areas / Estates
as notified by State Govt.
iv. If any plant/clusters of plants are located within 1 km from any residential
area/ village they may be shifted by State Pollution Control Board/ State Govt.
in a phased manner for which a time bound action plan is to be prepared by
SPCBs.
6.4 DATA ANALYSIS
The Ground water samples are to be analyzed for various parameters as per IS: 10500
and Surface water as IS: 2296 Class-C standards with the specified procedure. The
methodology which will be adopted for monitoring & analysis of PM10, PM2.5 SO2, NOx will
be as per IS: 5182 standards. Samples are to be analyzed for SO2 using improved West-
Gaeke method for air samples using a spectrophotometer at a wavelength of 560 nm.
Samples will be analyzed for NOx using Jacob and hocheiser modified (Na-As) method,
for air samples using a spectrophotometer at wavelength of 400 nm. RPM & SPM in
ambient air can be found by using respirable dust sampler (RDS).
6.5 REPORTING SCHEDULE
After every six months of plant operation six monthly reports covering all the parameters
of study period has to be prepared engaging external accredited agency and after
completion of analysis a copy of all the analysis reports are to be sent to the State
Pollution Control Board. A copy of the reports are to be maintained in the plant and will
be made available to the concerned inspecting authorities. Abnormality to be reported to
Board of Directors to take decision on remedial measure
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Table 6.1 Monitoring Schedule
Sl
No
Environ
ment
particula
rs Description Areas/Locations
Frequency of
Monitoring
Duration of
sampling
Monitoring
Parameters Data Analysis
Reporting
Schedule Action Plan
1
Air AAQ
1. Daharpur
2.Nutandih Twice in a week 24 hrs
PM10,PM2.5,SO
2,NOx, CO,
Ammonia, Lead,
Nickel, Arsenic
West-Gaeke
Method using
Spectroohoto
mer, Jacob
and
Hocheiser
method
After every six
months of plant
operation six
monthly reports
covering all the
parameters of
study period has
to be prepared
engaging
external
accredited
agency and
after completion
of analysis a
copy of all the
analysis reports
are to be sent to
the State
Pollution Control
Board. A copy of
the reports are
to be
maintained in
the plant and
will be made
available to the
concerned
inspecting
authorities.
Abnormality
to be recorded
and intimated
to Head of
Organisation
and corrective
Measures to
be
Implemented
Fugitive 1. RMHP
2. Internal Roads Twice in a Month SPM
Stack
Emissions
1. DRI Kilns
2. CPP
3. IFs
4. EAF
5. Sinter
6.MBF
Online Monitoring Continuous
PM10, PM2.5,
SO2,NOx,CO,
Flow rate,
Temp.
West-Gaeke
Method using
Spectrophoto
mer
2
Water Surface
Water
1. Pond Water of
Nutandih
2. Pond water of
Dauka
Twice in a year
1. Pre-Monsoon
2. Post-Monsson
Heavy Metals will be
monitored Once in a
month.
Grab
Sample
Parameters as per Class"C"
IS:2296
3
Ground
Water 1.Tubewell of
Daharpur
2.Tubewell of
Nutandih
Twice in a year
1. Pre-Monsoon
2. Post-Monsson
Heavy Metals will be
monitored Once in a
month.
Grab
Sample
Parameters as per Class"C"
IS:10500
4
ETP, CT
and Boiler Inside plant Once in a Month
Grab
Sample
pH, COD,
TSS,Oil &
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Blowdowns Grease, BOD
5
STP
Inside plant Once in a Month
Grab
Sample
pH, COD,
TSS,Oil &
Grease, BOD
6 Noise Noise
1. Along the
boundary wall
2. Daharpur
3.Nutandih Once in 6 Months
8 hrs
continuous
with 1 hr
interval
1.Lday
2. Lnight
3. Ldn
7
Occupati
onal
Health
1. Workers in the
plant Once in a year
Chest, Xray,
Vision, ECG,
Spirometry,
Audiometry etc
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6.6 BUDGETORY PROVISIONS FOR EMP
Gen.Tor-7(xi) Total Capital Cost And Recurring Cost/Annum For
Environmental Pollution Control Measures .
ToR 8(iv)Plan and fund allocation to ensure the occupational health &
safety of all contract and casual workers.
The company will invest 155 Crore (about 4 % of total project cost) as capital
investment towards implementation of Environmental Management Plan. The Annual
recurring cost will be about 18 crore details are as follows.
Investment towards EMP Implementation & its yearly maintenance is given in Table 6.3
Table 6.2 Investment towards EMP, Implementation & its yearly
maintenance
Category
Capital Cost
(INR Cr)
Recurring Cost
(INR Cr)
Air pollution Equipments 111.65 8
Water Pollution Control Machinery
& Construction
28 3
Rainwater Harvesting 2.5 0.8
Occupational Health 1.5 1
Green Belt Development 0.10 0.03
Environmental Monitoring 1.1 0.5
Solid Waste management 3.2 1.5
Safety & Disaster Management 5.3 2.5
EMS & Capacity Development 1.75 1
Total 155.1 18.33
Additional ToR. 7 Plan for The Implementation Of The Recommendations Made
For The Steel Plants In The CREP Guidelines
All the charter on corporate responsibility for environmental protection(CREP)
recommendations for integrated steel project will be implemented & followed strictly
which has been stated in table below.
Table 6.3 CREP Compliance
Sl.
No. CREP Conditions Compliance
1 Technology The organization will adopt the latest state of the art
technology with in-built pollution control measures
2 Fugitive emissions
reduction in SMS
Dedusting of Cast house at tap holes, runners, skimmers ladle
and charging points, swivel hood, Fume Extraction Chamber
followed by adequate capacity bag filtration will control
emission within the norms. RMHS-Dust extraction
&suppression using water sprinklers, Dry Fog in closed
conveyors & Bag filters
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3
Direct inject of reducing
agents in MBF. Energy
recovery of top BF gas.
Pulverized coal injection in MBF has been proposed
MBF top pressure to be utilized to run turbine and generate
power to the tune of 35kw/t of hot metal produced
4
To operate pollution
control equipment
efficiently and to keep
proper record of run
hours, failure time and
efficiency with
immediate effect.
Compliance report in
this regard be submitted
to CPCB/SPCB every
three months
Energy meter has been proposed to be installed in ESPs to
keep record of running hours and reported to SPCB, WB. Non-
conformance to be reported to Board of Directors. Sensible
heat BF gas, Non-recovery Coke-oven hot gas shall be used in
WHRB for captive power generation.ESP will control dust
emission.
5
To reduce specific water
consumption to 5 m3/t
for long products and 8
m3/t for flat products
Unit proposes production of billets and water consumption is
proposed with 6448 m3/day water excluding power plant
consumption but including domestic, coke oven etc. hence it
is coming to about 2.3 m3/t, there is no provision of rolling
mill at present to produce long or flats.
6
Reduction Green House
Gases by Reduction in
power consumption, Use
of by products gases for
power generation.
Promotion of Energy
Optimisation technology
including energy/ audit
BF gas has been proposed to be utilized to generate power.
Power reduction measures have been proposed. Power
recovery from DRI kiln flue gas, use of Variable frequency
Drive ID fans, Silicon-controlled rectifier, capacitor Bank, hot
metal charging in LF/IF, selection of medium frequency
coreless IFs and minimization of air consumption in FBCs are
the power saving steps suggested for the unit
7
Installation of
Continuous stack
monitoring system
Continuous stack monitoring system to be implemented and
regular ambient air monitoring will be done as per the
guidelines.
8 L C A
Life Cycle Assessment (LCA) is a decision cum management
tool which provides information on the environmental effects
of various products and processes so as to arrive at necessary
corrective measures to make the entire process efficient with
optimal utilization of resources and minimal wastes
generation. Steps to be taken to minimize pollution from
receiving ore from mines to utilization of end product and in
every intermediate stages.
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9 Solid Waste /Hazardous
Waste Management
There will be generation of fly ash, bottom ash, BF slag, IF
slag, BF dust &sludge from the plant processes. Fly ash will
be fully utilized in brick making by external manufacturing
agencies, utilization of ground granulated BF slag and fly ash
in cement plants and recycle of BF dust &sludge in sinter
plant has been proposed. Small amount of non-process
hazardous waste like used oil and exhausted batteries shall
be handed over to authorized resources.
10 Good house keeping
Green belt along boundary and tree plantation by the side of
internal roads, material handling area, regular water
sprinkling on roads and removal of MSW on regular basis will
help in good housekeeping. Again, scheduled preventive
maintenance and regular lubrication of moving machineries
will losses due to break down and help in good house keeping
and thereby prevent accidents. M/s BEL is a polythene free
Plant. All the employees spare time every week for cleaness
of the plant.
CONCLUSION
It is highly essential to have a regular environmental monitoring to monitor the post
project environment standards, like establishing a laboratory selection of sampling
locations, data analysis and budgetary provision for EMP, so that later it can be assessed
if there is a change in the ambient environmental conditions. After considering the
environment point of view, there will be evaluation on the risk and hazard involved in the
occupation in the next chapter. An industry cannot survive ignoring issues of people
residing in surrounding area of project who contribute for sustainability of project and
also affected by the project, hence there is need to listen people and take their views
before setting up a project. This need to be addressed in next chapter.
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CHAPTER-7 ADDITIONAL STUDIES
7.1 RISK ASSESSMENT & DISASTER MANAGEMENT:
M/s Bengal Energy Ltd, at-Daukais at present running with 0.6 MTPA Non-Recovery/heat
recovery Coke Oven and 40 MW Power Plant. The project has proposed its expansion for
which prior EC is in the process.
After expansion, the facilities will be as follows:
1. 2x0.6 MTPA non-recovery Coke oven Plant with waste heat recovery boiler
2. 4x500 TPD DRI kilns
3. 4x350 TPD DRI Kilns
4. 2x320m3 MBF
5. 1x60m2 Iron Ore Sinter plant
6. 2x80T EAF with CCM
7. 3x20T IF with CCM
8. 35 MW AFBC based Power plant
9. 22 MW BF gas fired based Power Plant
10. 80 MW Coke Oven gas(WHRB) power Plant
11. 68 MW DRI kiln flue gas(WHRB) Power Plant &
12. 120 TPD ASU.
Besides these operating processes, which can cause major hazards due to leakage of
toxic gases and red hot metal liquids; there will be one month’s fuel stock at all the time
of a year. Coal will be stocked under shed and LDO in 150 KL above ground tank; these
are combustible and Fire/ pool fire is anticipated from these materials
It is presumed that the proposed steel plant would be designed and engineered with all
possible safety measures and standard code of practices of engineering. In spite of this,
there may be some design deficiency or due to operation and maintenance fault which
may lead to accidental events causing damage to the life and property. This chapter
presents an overview of environmental risks associated with the production facilities,
suggested remedial measures and a model outline of the emergency preparedness plan.
7.2 OBJECTIVES
The objectives of environmental risk assessment are governed by the following, which
excludes natural calamities:
To identify the potential hazardous areas so that necessary design safety
measures can be adopted to minimize the probability of accidental events.
To identify the potential areas of environmental disaster which can be prevented
by proper design of the installations and its controlled operation
To manage the emergency situation or a disastrous event, if any, from the plant
operation.
Managing a disastrous event will obviously require prompt action by the operators and
the crisis management personnel using all their available resources like alerting the
people and other plant personnel remaining inside, deployment of firefighting equipment,
operation of emergency shut off valves, opening of the escape doors, rescue etc.
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Minimizing the immediate consequences of a hazardous event include cordoning off,
evacuation, medical assistance and giving correct information to the families of the
affected persons and local public for avoiding rumors and panic.
Lastly, an expert committee is required to probe the cause of such events and the losses
encountered and suggest remedial measures for implementation so that in future such
events or similar events do not recur.
7.3 DEFINITION OF ENVIRONMENTAL RISK
The following terms related to environmental risks are defined before reviewing the
environmental risks:
Harm : Damage to the person, property or environment.
Hazard : Something with the potential to cause harm; this could be
a Characteristic of material being processed or malfunctioning
of the equipment. An environmental hazard is thus going to be
a set of circumstances, which leads to the direct or indirect
degradation of environment and damage to the life and
property.
Risk : The probability of the harm or likelihood of harmful
occurrence being released and its severity. Environmental risk
is a measure of the potential threat to the environment, life
and property.
Consequence: Effect due to occurrence of the event, which may endanger the
Environment permanently or temporarily and, or, loss of life and
property.
Environmental The consequence is so severe that it can extensively damage a
Disaster : one or all the four components of the environment, namely, (i)
Physico-chemical, (ii) biological, (iii) human and (iv) aesthetics.
7.4 IDENTIFICATION OF HAZARDS
The hazards are attributable due to raw materials and chemicals used in steel making
and the plant operation. A list of major raw materials used in the plant and the process
units with their hazard potential is presented in Table below.
Gen. ToR 3(x) Hazard Identification and details of proposed safety measures.
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Table 7.1 Hazard Identification of the Proposed Steel Plant
SL NO ACTIVITY CREATING
HAZARD
Rank Risk
potential
Preventive Measures Likelihood of occurrenc
e (A)
RANK
Likelihood
of detection
(B)
RANK
Severity of
consequence
( C )
RANK =
(A+B)XC
Oxygen Plant
1 Handling of Liquid Oxygen HIGH 4 MODERATE 3 LOW 6 42 Leather apron, leather gloves and safety shoes
DRI
1 Cleaning of cooler transfer chute
HIGH 4 VERY LOW 5 MODERATE 8 72 Safety rope and PPE to be used
2 cleaning of dust settling chamber
HIGH 4 VERY LOW 5 MODERATE 8 72
Use of PPE like safety shoes,
helmets, gloves, aprons and goggles
SMS
1 Fall of material due to Excess N2 purging
LOW 2 VERY HIGH 1 HIGH 10 30 Purging to be done with calculated amount of N2
2 Burn injury due to overflow of hot material
LOW 2 VERY HIGH 2 HIGH 10 40 Use of PPE like safety shoes, helmets, gloves, aprons and goggles
3 Burn injury due to broken of wire rope
LOW 2 VERY LOW 5 HIGH 10 70 Cordening of area with hooter arrangement during transportation
4 Fall of ladle due to broken of hanger
LOW 2 VERY LOW 5 HIGH 10 70 Cordening of area with hooter arrangement during transportation
5 Slip and fall due to accumulation of sponge iron on shop floor
MODERATE 3 MODERATE 3 LOW 6 36 Use of PPE like safety shoes, helmets, gloves, aprons and goggles
6 Falling of scrap due to mishandling of scrap during
charging of scrap to SMS
MODERATE 3 MODERATE 3 MODERATE 8 48 Use of helmets and safety shoes
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7
SLIPING OF PERSONS DUE TO Spillage of material on the shop floor during charging of raw material through mobile
equipment
MODERATE 3 MODERATE 3 MODERATE 8 48 Use of PPE like safety shoes, helmets, gloves, aprons and goggles
8 Electrical Flashing / shock during Air cleaning of furnace capacitors and switch gear
LOW 2 LOW 4 HIGH 10 60 Electrical isolation, tagging, spot earthing
9 Electrical Shock during Checking of Capacitor bank
VERY LOW 1 MODERATE 3 MODERATE 8 32 Rubber hand gloves and insulator tools
11 Occurrence of static electricity/electric spark in the Mill Cellar Room
VERY LOW 1 VERY LOW 5 HIGH 10 60 Proper earthing to be ensured
12 Splashing of molten metal and slag
LOW 2 VERY HIGH 1 HIGH 10 30 Face shield, helmet, asbestos appron
Rolling Mill
1 Fall of material during hot slab handling
LOW 2 VERY LOW 5 HIGH 10 70 Sling to be checked from time to time, Use of PPE
2 BODY PART in between slab/chain
LOW 2 VERY LOW 5 MODERATE 8 56 Use of Hand gloves, Stopper switch at short intervals
3 Fire due to Electric short circuit during Firing with Tar
LOW 2 VERY LOW 5 LOW 6 42 Use of MCB
4 Back firing during Firing with Producer gas
LOW 2 VERY LOW 5 LOW 6 42 Use of Face shield
5
Fall of Plate, Cutting set, Fall
on person during Plate/Cobble Cutting
LOW 2 VERY LOW 5 LOW 6 42 Use of helmet
6 Collision of hot coil strips during Shifting of Coil
LOW 2 very low 5 low 6 42 To be mechanically handled
7 Falling of objects from top MODERATE 3 VERY LOW 5 MODERATE 8 64 Use of helmet & Safety Shoe
8 Un safe disposal of oily wastes of Rolling Mills
HIGH 4 Low 4 Moderate 8 64 To be collected in drums and capped
CPP
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1
Furnace oil transfer from tanker to storage tank
LOW 2 HIGH 2 MODERATE 8 32 To be transferred Mechanically and Use of PPE 1.Slip & Fall
2. Fire
2
Operation of Boiler
LOW 2 LOW 4 HIGH 10 60
Periodic NDT to know the thickness of pipe and replacement with thinned down pipes.
Interlocking of ID fan running with LDO firing.
1.EXPLOSION
2.TUBE LEAKAGE
3. BACKFIRE
3 Oil leakage from bearings &
oil line on main steam line LOW 2 LOW 4 LOW 6 36
Shrouding of evaporator coil
4 Chemical handling MODERATE 3 LOW 4 MODERATE 8 56
Use of PPE like safety shoes, helmets, gloves, aprons and goggles 1. ACID / ALKALI SPILLAGE
5 Generation of dust during ash
unloading on trucks VERY HIGH 5 VERY HIGH 1 LOW 6 36 Use of Dusk Mask
6 Fall from height while working in the height
LOW 2 LOW 4 HIGH 10 60 Use of safety belt
7 Oil wastes/oil sludge handling LOW 2 High 2 Mode rate 8 32 Use of PPE like safety shoes, helmets, gloves, aprons and
goggles
8 Collapsing of acid/ alkali storage tanks
VERY LOW 1 High 2 High 10 30 Use of vacuum breaker
9 Leakages of steam line LOW 2 HIGH 2 MODERATE 8 32 NDT of steam line at regular intervals specially at bends and thermal insulation of pipeline
SINTER PLANT
1 Working near moving equipment
HIGH 4 LOW 2 HIGH 10 60 Guards for moving equipment, PPE
2 Generation of dust NOx, SOx & Dioxins
HIGH 4 HIGH 4 MODERATE 8 64 PPE like mask, Good ventilation of Working Place.
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From the Table, it may be observed that the major on-site emergency situation may
occur from the organic coal chemicals storage and handling, fuel gas handling, molten
metal and slag handling, acids and alkali storage and handling and electrical short-
circuit. The off-site environmental disaster may occur if large-scale fire and explosion
occurs, the effect of which extends beyond the plant boundary. The off-site
environmental disaster may occur due to significant environmental degradation for a
sustained period.Off-site environmental disaster not envisaged for this integrated steel
plant. However pool fires from fuel oil storage tanks are not ruled out, and needs
addressal.
7.5 ENVIRONMENTAL RISK EVALUATION
From environmental hazards point of view for the raw materials and consumable
chemicals and processing of the same in various production units, relative risk potential
analysis is made on the following three factors:
Likelihood of occurrence
Likelihood of detection
Severity of consequences
Each of these factors is graded and compiled to determine the risk potential. The factors
governing the determination of relative risk potentials are presented in the Table 7-2.
Table 7.2 – Determination of Risk Potential
Likely hood of
occurrence Likelihood of detection
Severity of
consequences
Criteria (A) Rank Criteria (B) Rank Criteria (C) Rank
Very High 5 Very High 1 None 2
High 4 High 2 Minor 4
Moderate 3 Moderate 3 Low 6
Low 2 Low 4 Moderate 8
Very low 1 Very low 5 High 10
RISK POTENTIAL (RP) = (A+B) X C
Based on the above stated criteria for assessing the risk, each probable event has been
evaluated by addressing several questions on the probability of event occurrence in the
view of the in-built design features detection response, operational practice and its likely
consequence. A summarized list of environmental risk potential for the likely events is
presented in Table 6-3
This evaluation has been done with the presumption of common events as observed
from the past experience in the operation of an integrated iron and steel plant and best
practicable designs for the proposed project. The present risk potential evaluation is
primarily based on human errors or faulty operation or failure of the control systems.
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From the table 7.3, it appears that some events carry risk potential above 50. these
vents will be considered as risk prone hazardous events and need adequate safe design
operation and maintenance in order to reduce the risk.
Risk Management Measures
The Risk management measures for the proposed project activities require adoption of
best safety practice at the respective construction zones within the Works boundary. In
addition, the design and engineering of the proposed facilities would take into
consideration of the proposed protection measures for air and water environment. The
Evaluation is given in the Table No. 7.3.
7.6 DISASTER MANAGEMENT PLAN
Tor-7(xiii) Onsite And Offsite Disaster Preparedness And Emergency
Management Plan Including Risk Assessment And Damage Control.
Manpower
Table 7.3 Manpower to be in position
Department
/ Section
Shifts Total per
week
day
Total on
Pay Roll General I II III
Coke Oven
Plant
20 60 60 60 200 230
Sponge Iron
Plant
15 100 100 100 315 325
BF 10 30 30 30 70 75
EAF & IF 10 75 75 75 235 250
Captive Power
Plant
15 50 50 50 165 175
Sinter Plant 5 20 20 20 65 70
Maintenance
and Services
30 40 40 40 170 175
Quality
Assurance and
Lab
5 15 15 15 50 55
Total 110 390 390 390 1280 1355
From the manpower deployment table, it can be seen that at any point of time in general
shift hours 500 people will be available in plant, and 390 people during night. More over
some contract labors and security guards will be available in the plant. If it is a time of
changeover of shift additional 390 people will also be inside plant premises. Therefore,
planning has to be made for safety of these people during any onsite disaster.
In an integrated steel plant like this one, it is imperative that accidents occurring due to
unforeseen acts and events will not affect the surrounding areas. Therefore, an onsite
emergency plan for prevention and mitigations of accidents will be enough to cater for
unforeseen acts and events that may occur.
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Identification of most credible Hazard Scenarios
All the anticipated hazard scenarios associated with this integrated steel plant are
critically examined and the following scenarios are identified as credible scenarios:
Credible scenario-A : Pool fire in any of 2x200 KL LDO tanks
Credible scenario- B : Pool fire in 1x200 KL FO tank
Credible scenario- C : Toxic release and fire due to CO from MBF
Credible scenario-D : Leakage of liquid Oxygen from ASU
The LDO/FO tanks will be provided with standard auxiliaries such as conservative vent
valve, flame arrestor, drain connection. Oil from these tanks shall be transferred to the
respective consumer units by 2 x 100 per cent fuel oil transfer pumps through filters.
Return oil, if any, shall be discharged back to the storage tank. The tank farm will be
provided with dyke wall and suitable fencing all around according to statutory
requirement. However accidental fire may not be ruled out.
Models done for this scenario show that credible hazard can occur in winter night time.
In this case the significant heat levels of interest(SHL) for the pool fire as predicted by
model shall be as per the following table.
There are three significant “Heat Levels” of interests which are as follows.
S H L Value Experience at
distance pool A
Experience at
Distance pool B
Indication
SHL-1 4.5 KW/m2 10.01m 9.57m Causes pain if unable
to cover the body
within 20 seconds
SHL-2 12.5 KW/m2 6.19m 5.91m Minimum energy for
melting plastic
SHL-3 37.5 KW/m2 3.68m 3.51m Sufficient to cause
damage to equipments
As pool fire can cause damage to equipments within distance estimated, no such
equipments to be constructed within that distance. This hazard is not considered as most
credible scenario.
As to toxic release and fire due to CO release, BF gas contains about 25-30% CO. This
considered as most credible scenario and for that on sight emergency plan has been
made.
Leakage of liquid Oxygen from Oxygen storage tank or ASU will vigorously accelerate the
combustion or initiate explosion of organic or oxidizable material. Many materials that
are not combustible in air(20% Oxygen) can burn in oxygen rich atmosphere. Oxygen
tank may vent rapidly or rupture violently from pressure when involved in a fire
situation.
Toxicological Information
Oxygen is neither combustible nor acutely toxic under normal pressure but helps in
combustion. So associated fire hazard due to leakage of Oxygen is rare and much less in
magnitude as compared to fire from LDO or FO tanks. The coal storage area and LDO/FO
storage tanks to be away from Oxygen storage tank.
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Emergency command structure
7.7 ROLE OF KEY PERSONS
7.7.1 WORKS MAIN CONTROLLER:
He is the Managing Director of the unit and is generally available in the factory or in the
colony nearby except on tours. On emergency, he can reach work site at any odd hour
within 20 minutes time. In his absence, HOD project & co-ordination shall take up his
charge as Works Main Controller (WMC).
On being informed of an incident, he has to:
Rush to the emergency Site, collect all information from SIC.
Decide if emergency is to be declared and advise Site incident Controller
(SIC) accordingly and reach Emergency Control Room (ECR).
Advise Rescue Team Leader (RTL)/ Security Gate to blow the siren with
appropriate code for declaration of emergency.
Two minutes with a pause of five seconds for 3 times for fire hazard.
Three minutes with pause of five seconds for 5 times for Gas leakages.
Advice (Auxiliary Team Leader) ATL for communication to statutory
authorities and for mutual aid as required.
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Through (Auxiliary Team Leader) ATL ensure constant communication to
statutory authorities and to mutual aid partners as required.
Maintain continuous communication with Site Incident Controller (SIC) to
review the situation and assess the possible course of action for emergency
operations.
To declare normalcy at the end of operation and advise Rescue team leader
(RTL)/security Gate to blow “all clear siren” [for 1 minute continuously].
Ensure the record keeping of emergency operations chronologically.
7.7.2 SITE INCIDENT CONTROLLER:
He is available at the factory or in the colony nearby. At any point of time and on being
informed about an accident, he has to:
Intimate the works main Controller (WMC) and proceed to the emergency
site.
Take the necessary instruction from Combat Team Leader (CTL), assess the
situation and call Rescue Team Leader (RTL) and Auxiliary Team Leader
(ATL).
Inform Works Main Controller (WMC) regarding the situation.
Take necessary steps and provide guidance to Combat Team, Rescue Team,
and Auxiliary Team Leaders to mitigate the emergency situation.
Examine for major emergency shut down operation activities, decide safe
escape route and announce for evacuation to Assembly Point.
Inform Works Main Controller (WMC) about the status of the situation at
regular intervals.
7.7.3 COMBAT TEAM LEADER
He is the leader to attend to the emergency and is available in the factory or in the
colony at any instant.
On being informed about an accident, he has to:
Immediately rush to the site and lead the team to control the situation.
Inform Site incident controller (SIC) about the incident and request him to
rush to the spot.
Instruct the rescue Team leader (RTL) for fire fighting and medical assistance.
Co-ordinate the activities of team members and combat the emergency, so as
to eliminate the route cause of the hazard.
Shut-down the plant if necessary to take up repair measures.
To arrest the leakage and spillage from various equipments, shut down the
concerned equipments.
Take necessary action to remove unwanted persons from the site of the
incident.
Keep informed about the developments to Site incident Controller (SIC).
7.7.4 RESCUE TEAM LEADER
He is the person who conducts rescue operations and should be available at any instant.
On receiving the information about the incident he has to:
Rush to site of emergency through safe route.
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Ensure presence of all his team members, availability of fire fighting facilities
and take necessary action to arrest the fires/leakage of gas.
Arrange for safe escape of entrapped persons.
Make necessary arrangements to send the affected persons for immediately
medical attention through the medical officer.
Search for the missing persons on the basis of role call taken by Auxiliary
team leader (ATL).
Give the feedback to the site incident controller (SIC) about the
developments.
7.7.5 AUXILIARY TEAM LEADER
He is the communication manager for the crisis management. On being informed of the
emergency, he should proceed to Emergency Control Room (ECR) and:
Keep in constant touch with works main controller (WMC) and Site Incident
Controller (SIC).
Inform the Statutory Authorities and District Administration.
Communicate to mutual Aid Partners, Fire service stations at Kharagpur.
Send communications to District Hospital Kharagpur Road for rendering
services.
Inform the relatives of causalities and send them to their residence or hospital
as the case may be.
Take care of visit of the authorities to the Emergency site.
Give feed back to work main controller (WMC) about the status with respect
to his areas of activities.
Table 7.4 ACTION PLAN FOR ON-SITE EMERGENCY
STEP
NO
INITIATOR ACTION TO TAKE
1. The person noticing
the emergency
Inform the Security Gate, Combat team leader and the
concerned Shift-in –charge immediately.
2. Combat team Leader
(CTL)
Inform site incident Controller (SIC) and rush to spot and
organize his team.
Take charge of the situation, arrange for fire fighting and
medical first-aid available at site.
To start combating, shut-down equipments, arrest the leakage
of gas/fire.
3. Site Incident
Controller (SIC)
Inform works main controller (WMC) and rush to emergency
site.
Discuss with Combat Team Leader (CTL), assesses the
situation and call the Rescue Team Leader (RTL) & Auxiliary
Team Leader (ATL).
Organize the Rescue Team and Auxiliary Team and send the
rescue Team to site.
Arrange to evacuate the unwanted persons and call for
additional help.
Pass information to the works main controller (WMC)
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periodically about the position at site.
4. Works main
Controller (WMC)
Rush to emergency site and observe the ongoing activities.
Take stock of the situation in consultation with the SIC.
Move to Emergency Control Room.
Take decision on declaration of emergency.
Advise Auxiliary Team Leader to inform the statutory
authorities and seek help of mutual aid from partners as
required.
Decide on declaration of cessation of emergency.
Ensure that the emergency operations are recorded
chronologically.
5. Rescue Team
(RTL)
Consult with Site incident controller (SIC) and organize his
team with amenities to arrest fire fighting and medical
treatment.
Rush to Emergency Site through safe route along with the
team members.
Arrange to set off the fire by fire fighting equipments and
hydrant points to arrest the fire or to evacuate the area.
Shift the injured persons to hospital by ambulance after
providing necessary first aid.
To inform the auxiliary team Leader for necessary help from
mutual aid Partners.
6. Auxiliary Team (ATL) On being directed by works main Controller (WMC) inform
about the emergency to statutory authorities.
Seek help of Mutual Aid partners and Coordinate with Mutual
Aid partners to render their services.
Arrange to inform the relatives of casualties.
Take care of visit of the authorities to the Emergency site.
7. Team members Each of the team members should follow the instruction of
concerned team leader to mitigate the emergency.
7.8 SILENT HOUR COMMAND STRUCTURE
The Senior Officers/ Key Persons of the plant remain during day time i.e. 8am to
8 pm. Hence the timing of 8pm to 8am is considered as silent hour that to 10pm
to 8am is the crucial time. Still each and every unit/section of the plant is
headed by shift in charge in the rank of Officer, Engineer or Sr. Engineer or Asst.
Manager, who shall be responsible for handling the emergency. The other
supporting/services and emergency sections like Fire Service, Ambulance,
Security, Personnel, Water Supply, Transport departments etc. are also running
for 24 hours shift wise with shift in charge and crew to handle emergency during
the silent hour till main command personnel arrive. However, most of the key
persons of the main command structure reside in nearby area and can reach
within minimum time.
The command structure of the silent hour shall be same as during normal hour,
however, during the silent hour, the operation Shift-in charge of the concerned
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area where the fire or leakage of gas has taken place, shall act as SIC-in –
charge, till the arrival of actual designation members.
Since WMC, SIC, CTL, RTL & ATL may not be available inside the plant; they shall
be informed by the SIC-in-charge either by telephone or by sending special
messengers to their residences.
On receiving the information WMC, SIC, CTL, RTL & ATL shall reach the site
immediately & simultaneously take actions to ensure the presence of their
respective team members.
Therefore the action plan as well as the role of key person shall be same as the
normal hour execution of command structure.
7.9 ACTIVATION & CLOSING PROCEDURE FOR ON-SITE EMERGENCY
7.9.1 ACTIVATION PROCEDURE
The person noticing the incident of fire or leakage of gas, shall inform about the location
& nature of fire to the combat team Leader (CTL), security Gate and concerned Shift-in-
charge.
Combat team Leader (CTL) shall inform site incident controller (SIC) and shall rush to
the site immediately. He shall arrange for fire fighting and first aid available at site. He
shall arrange to take necessary steps to eliminate the root cause of fire.
Site incident controller (SIC) on getting information shall inform the WMC and reach the
site at the earliest. He shall take over the charge and shall direct Rescue Team Leader
(RTL)) to carry out rescue operations including fire fighting and medical attention. Site
incident controller (SIC) shall co-ordinate with Combat team leader (CTL) to eliminate
the root cause of fire.
- Work main controller (WMC), on arrival at site shall take stock of the situation
from site incident controller (SIC) and then rush to emergency control room
(ECR) to declare emergency on the basis of assessment made by (Site incident
controller (SIC). He shall give direction to the security gate/ (Rescue team
Leader) RTL to activate siren.
Two Minutes with a pause of five seconds for 3 times for fire Accident.
Three Minutes with a pause of five seconds for 5 times for leakage of gas.
- Rescue Team Leader (RTL) shall mobilize fire fighting and medical resources to
site and shall assist (Site incident Controller) SIC.
- Auxiliary Team Leader (ATL) shall take charge of Emergency Control Room
(ECR), shall ensure smooth operation of ECR and shall inform relatives of
casualties. Informs mutual Aid partners and ensures their arrival at site if
required.
- Auxiliary Team Leader (ATL) informs statutory authorities and district
administration regarding emergency suitably and coordinates their visit at site.
- Works main controller (WMC) coordinates and keeps the track of all the
activities at site and off the site and arranges the recording of the activities in a
chronological manner for review of the Onsite emergency Plan.
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7.9.2 FACILITIES AVAILABLE FOR ON-SITE EMERGENCY PLAN:
(a.) Assembly Point:
In any emergency it will be necessary to evacuate people from affected zones or the
zones likely to be affected, to a safer place. Safer places are identified and designated as
Assembly Points. Taking the area and hazard zones into consideration two assembly
points have been marked in two different areas i.e. one near administrative building
(Assembly Point-1) and other near the SMS Area (Assembly Point-2) Both the points are
well connectable to the plant road and facilities like drinking water, temporary shelter
and first aid is available there. This has been well marked in the lay out map as well as
in the factory.
(b.) Escape routes:
Escape routes are those that, allow reasonably safe passage of persons from the work
area to assembly point during emergency situation. These routes would be different
depending on wind direction, Fire and explosion scenario. Escape routes are ear marked
on the drawings as well as on the routes, showing escape direction in broad arrow marks
on fluorescent paints, which will facilitate all for safe evacuation.
(c.) Emergency Control Room (ECR):
The emergency Control Room is a place from which all emergency management
operation are directed and coordinated. Also it is the place from where all
communication will be established, with outside agencies and district authority also.
Facilities Available at ECR:
a. Plant general Layout, ear marked with hazard zone, Assembly points and escape
routes.
b. List of working personnel in various shifts and general shift.
c. Mobile telephone Nos., of emergency command structure personnel.
d. Emergency command structure.
e. Rhythmical siren code for different emergency situation.
f. Relevant material safety data sheet.
g. Emergency Control Room Register.
h. First Aid Box with antidotes.
i. Required personal protective equipments with self carrying breathing app.
7.10 FACILITIES AVAILABLE
Fire Hydrant System
Fire pumps are to be connected to main fire hydrant to maintain a pressure of
7Kg/cm2. In case of temporary power failure, the fire pumps are to run through
DG. An underground tank supply water to the fire main. A security jeep is
stationed at main gate (main control) to meet the emergency.
Fire Extinguishers
Required types of fire extinguishers are to be provided at different locations of
the plant.
Fire Buckets
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Fire buckets filled with dry sand must be provided in differentlocations of
the plant.
Fire Tender
The company may have a fire tender of its own for major firefighting operations.
Siren
Company must have Siren/ hooter arrangement, which can be activated
manually during fire related emergency.
Communication
Public address system and EPABX telephone is available for effective
communication inside the plant. Telephone directory is available in the entire
department.
Dispensary
A well organized First-aid centre with ambulance, stretchers, oxygen cylinder etc.
shall be located inside the factory. The First-aid centre is manned by one doctor,
4nos. pharmacists, 4 nos. attendants, and one Ambulance with driver. The
first-aid center is manned round the clock. In the event of emergency, the
doctors and staff attend the first-aid centre. The existing first-aid centre is to
be strengthened & well-equipped to meet the emergencies. In case of
requirement outside ambulance services are to be contacted.
First Aid Box
Company has provided First Aid boxes with required first aid medicines at
different locations inside the plant for any injury. First aid boxes are checked by
the pharmacists once in a month & and medicines are filled/replaced. The first aid
boxes are provided in the following locations:
Blast Furnace, DRI, Coke Oven, Ferro Chrome, Power Plant, Electrical Substation,
DG room, Administrative building, SMS, Rolling Mill and Security Office.
7.11 OBJECTIVE OF ONSITE EMERGENCY PLAN
The main objective of the plan is to take immediate actions to meet any emergency
situation for speedy and efficient rescue and relief operations. The main steps in an
onsite emergency plan is described below:
Cordon and isolate the affected area for smooth rescue operation.
Rescue and treat casualties and safeguards the rest.
Minimise damage to persons, property and surroundings.
Contain and ultimately bring the situation under control.
Secure and safe rehabilitation of the affected area.
Identify any dead and provide for the needs of the relatives.
Provide necessary information to statutory agencies.
Provide authoritative information to the news media.
Ward off unsocial elements and prying onlookers.
Counter rumor mongering and panic by relevant accurate information.
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Industrial Safety and Fire Fighting
For protection of working personnel, equipment and machineries from any damage or
loss and to ensure uninterrupted production, adequate safety and firefighting measures
have been planned for the proposed plant. Important provisions are as follows:
Provision of adequate personal safety appliances to workers engaged in hazardous installations
Provision of detection and alarm system to allow a developing fire to be detected
at an early stage.
Provision of water spray fire extinguishing system and portable extinguishers
using carbon dioxide or chemical powder.
Portable Fire Extinguishers
All plant units, office, buildings, stores, laboratories, etc. will be provided with adequate
number of portable fire extinguishers to be used as first aid fire appliances. The
distribution and selection of extinguishers will be done in accordance with the
requirement of fire protection manual.
7.12 OCCUPATIONAL HEALTH
The modern definition of Occupational health is “The promotion and maintenance of the
highest degree of physical, mental and social well-being of workers in all occupations –
total health of all at work”.
Occupational health is concerned with physical, mental and social well-being in humans
in relation to his work and work environment, their adjustment to work and adjustment
of work to humans
ILOs’ Occupational health services recommendation, 1959 (No. 112) aims with following:
Protecting workers against any health hazard, which may arise out of work or condition
in which it is carried on.
Contributing towards workers’ physical and mental adjustment, in particular by
adaptation of work to workers and assignment to jobs in which they are suitable and;
contributing to establishment and maintenance of highest possible degree of physical
and mental social wellbeing of workers.
7.12.1 Occupational Health Hazard
Hazard is defined as “Source or situation with a potential for harm in terms of injury or ill
health, damage to property, damage to the workplace environment, or a combination of
these”
1972 ILO/WHO Conference Recommendations:
Occupational health is a wide field, and during last decade relative importance of its
component parts has changed. This changing concept has been linked with scientific
progress in relation to occupational health and safety and also with changes in evolution
of work and work environment on part of individuals. In past emphasis was on safety,
now it is more on health and job satisfaction.
In 1976, 29th session of World Health Assembly directed Director General to promote
planning and implementation of comprehensive health programs for workers, as an
integral part of National Health Programs.
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Legal Provisions
The Indian Constitution has shown notable concern to workmen in factories and
industries as envisaged in its preamble as Directive Principles of State Policy.
For securing the health and strength of workers, men and women
That the tender age of children is not abused
That the citizens are not forced by economic necessity to enter avocations
unsuited to their age or strength
Just and humane conditions of work and maternity relief are provided and,
That the Government will take steps, by suitable legislation or in any other way,
to secure the participation of workers in the management of undertakings,
establishments or other organizations engaged in any industry
The Factories Act, 1948, the Mines Act, 1952, the Dock Workers (Safety, Health &
Welfare) Act, 1986 are some of the laws, which contain provisions regulating the health
of workers in an establishment. Whereas the Employees State Insurance Act, 1948 and
the Workmen’s Compensation Act, 1923 are compensatory in nature. These various legal
provisions to protect health and safety of the workers are given in Chapter 8. It may be
sufficient to indicate at this stage that metallurgical industries are classified as hazardous
industry and legal provisions must be adhered to avoid any harm to work force and local
residents in the vicinity of the industry.
Occupational health hazard in steel plants are of two types. One occupational health
hazard 1) common to all shops including Raw material/Product handling & 2) Hazards
specific to individual Major Shop.
Gen. Tor 8 (i) Details Of Existing Occupational And Safety Hazards. What Are
The Exposure Levels Of Above Mentioned Hazards And Whether They Are Within
Permissible Exposure Level (PEL). If These Are Not Within PEL, What Measures
The Company Has Adopted To Keep Them Within PEL So That Health Of The
Workers Can Be Preserved.
(A)Existing Health hazards Common to a Steel Plant like M/s BEL are due to dust in
eye contact, skin contact, inhalation of toxic gas, ingestion, coming in contact with
molten metal or high temperature, and unpleasant sound level of running machineries.
Dust
The iron ore and coal are stored in raw material yard. The main health hazard in the
storage yard is uncontrolled fugitive dust emission during loading/un loading and
transportation of material in the stock yard.
Eye Contact:
Airborne dust may cause immediate or delayed irritation or inflammation. Eye contact
with large amounts of dust particles can cause moderate eye irritation, chemical burns
and blindness.. Eye exposures require immediate first aid and medical attention to
prevent significant damage to eye.
Skin Contact:
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Dust of coal, Iron ore and silicon may cause dry skin, discomfort, irritation, severe burns
and dermatitis. These dusts are capable of causing dermatitis by irritation. Skin affected
by dermatitis may include symptoms such as, redness, itching, rash, scaling and
cracking.
Inhalation
Breathing dust may cause nose, throat or lung irritation, including choking, depending on
the degree of exposure. Inhalation of high levels of dust can cause chemical burns to the
nose, throat and lungs. Inhalation of toxic gases beyond TLV can even be fatal.
Ingestion:
Internal discomfort or ill effects are possible if large quantities are swallowed.
Burning
Burning is caused due to coming in contact with hot metal or bodies at high temperature
or corrosive chemicals like acid or alkali. Similarly cold burning and blister formation is
caused in coming contact with liquefied gases.
B)Common safety hazards in an Integrated Steel Plant are - Posture, Excess Load,
Harmful Contact By Cranes : Defective Tackles, Slings, Excess Load, Wrong Signaling,
Working Under Load, Unskilled Operator, Defects in Crane, Improper / Unauthorized
Handling and most important is stress
7.12.2 EXPOSURE LIMITS
The exposure limits for Manganese, Crystalline, silica, Coal Dust are as given in the
following table for awareness.
SR.
NO.
Raw
materials
Chemical
Name
*NIOSH
TLVTWA
(mg/m3)
Factory
Act TLV
(mg/m3)
Target
Organs
Symptoms
1 Manganese Manganese
oxide
(Mn3O4)
1mg/m3 C*05mg/m3 Resp.
System, CNS,
Blood,
Kidneys,
Asthenia,
insomnia,
mental,
confusion, low
back pain,
vomit;
maliase,
blassitude,
kidney
damage;
pneumonitis
2 Silicon Si -
10mg/m3(total)
10600/(% Eyes, Skin, Irritation eyes,
skin, upper
(a)
Crystalline
Quartz+10
mg/m
10/(%
respirable)
Resp sys. respiratory;
cough
(b) Quartz -5mg/m3
(1) In
terms of
dust count
& (2) In
(respiratory) Quartz+2)
mg/mt.
10/(%
respirable)
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terms of
respirable
dust.
3 Coal(Dust) <5%SiO2)2mg/
m3 as the
respirable dust
fraction)
Not
available
Respiratory
system
Chronic
bronchitis,
decreased
pulm function,
emphysema 0.1mg/m3(as
the respirable
quartz fraction)
4 Iron ore Iron oxide
dust
&fume(as
Fe)
(Fe2O3),Iro
n(III) Oxide
5mg/m3 5mg/m3 Respiratory
system
Benign
pneumoconiosi
s( siderosis)
Airborne concentrations of chemical substances and represent conditions under which it
is believed that nearly all workers may be repeatedly exposed, day after day, over a
working lifetime, without adverse health effects are threshold limit values.
Permissible Exposure Level
The expansion project will have Induction Furnace and Rolling mill. The workmen while
handling raw material like sponge iron, pig iron or scrap may be exposed to Iron oxide
Fe2O3 fumes.
Ferric oxide fumes are red brown in color and have a metallic taste. As per OSHA
standard for 8hr working the Possible Exposure Limit is 10mg of Fe2O3 per cubic meter
of air (American standard 5mg/m3. Repeated exposure of iron ore fume over a period of
years may cause x-ray changes of lungs but does not cause the exposed person to
become ill. Exposure for 6 to 10 years is only recognized by X-ray. This may cause
pneumoconiosis and benign of pneumoconiosis is termed siderosis.
If a person breathes a large amount of iron oxide fume must be shifted to fresh air at
once and if breathing found to have stopped, artificial respiration to be given and
affected person to be kept warm and at rest and get medical attention as soon as
possible.
Preventive measure to keep emission within PEL
7.12.3 FIRST AID MEASURES
Following first aid measures shall be taken.
Eye Contact:
Rinse eyes thoroughly with water for at least 15 minutes, including under lids, to remove
all particles. Seek medical attention for abrasions and burns.
Skin Contact:
Wash with cool water and a pH neutral soap or a milk skin detergent. Seek medical
attention for rash, burns, irritation and dermatitis.
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Inhalation:
Move person to fresh air. Seek medical attention for discomfort or if coughing or other
symptoms.
Falling from height
Proper scaffolding to withstand the load, use of safety belt and other PPEs can protect
from injuries.
Ingestion:
Vomiting not to be induced. If conscious, have person drink plenty of water. Seek
medical attention.
7.12.4 EXPOSURE CONTROLS AND PERSONAL PROTECTION
Exposure Controls:
Control of dust through implementation of good housekeeping and maintenance;
The bag filters will be installed to control dust emission.
Use of PPE, as appropriate (e.g. masks and respirators)
Use of mobile vacuum cleaning systems to prevent dust buildup on paved areas;
Personal Protective Equipment (PPE):
Respiratory Protection: When the dust level is beyond exposure limits or when
dust causes irritation or discomfort use Respirator.
Eye Protection: Wear Safety goggles to avoid dust contact with the eyes. Contact
lenses should not be worn when handling the materials.
Skin Protection: Wear impervious abrasion and alkali resistant gloves, boots, long
sleeved shirt, long pants or other protective clothing to prevent skin contact.
Preventive Measures
The storage yards are constructed and maintained as per the guidelines.
Regular weekly inspections of storage yards will be carried out with regard to
proper earthling, adequate firefighting facilities, any combustible materials,
prevention of growth of wild vegetation etc.
No naked fires will be allowed in and around coal storage areas and height of
coal/ coke heap should not be high to prevent auto ignition.
Stress
The process by which we perceive and respond to certain events, called stressors, that
we appraise as threatening or challenging.
Uncertainty at work place cause high level of stress. The cause of uncertainty can be
lack of information or instruction what exactly to do or lack of job knowledge.
No job satisfaction i.e. boss is not happy with or what boss & colleagues think about
his/her ability or receiving vague inconsistent instruction. Sometimes that work place is
not safe and catastrophe anticipated due to wrong operation.
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With increased stress, blood pressure increases, productivity thoughts decrease and
destructive thoughts increase and there is likelihood of taking risky alternatives due to
poor judgment and there may be greater tendency of escape behaviors.
Alcohol & stress in combination are deadly and smoking is not the solution considering
its long-term harmfulness.
Communicating problems at work place to seniors, colleagues; asking in a positive way
and executing their guide lines and giving much importance to each & every job that
comes on the way can remove stress at work place.
Table 7.5 Health Hazard in Major Shops:
Sl.
No.
Group Item Potential
Health hazard
Preventive measures
I Raw materials
and products
handling
Iron ore fines Eye/skin
irritation
Water sprinkling’
Coal, lime stone,
Dolchar
Other fluxing
minerals
Respiratory
track diseases
due to Dust,
Dry fogging in
conveyors, ID fan
bag filter, PPE
Acids/Alkalis Skin & eye
injury
Water jet for eye
washing, first-aid
II Major shops
MBF Hot metal & slag
CO & H2gas
Burn injury
Gas poisoning
Keeping area dry so
that molten Iron Metal
does not come in water
Contact, wearing PPE
Billet caster Hot molten metal Burn injury wearing PPE
Coke-Oven Red Hot Coke Burn injury PPE like safety shoes,
hand gloves & helmet
Sinter Plant Red Hot Sinter Burn injury PPE like safety shoes,
hand gloves & helmet
AFBC High pressure
steam
Burn injury and
exposure to
high level noise
damaging ear
PPE like safety shoes,
hand gloves & ear muff
ASU Liquid O2 & N2 at
very low
temperature
Cold burning of
skin, cold
blisters
PPE like safety shoes,
hand gloves
III Utilities
Fuel gas
Distribution
Gas leaks Fire and gas
Poisoning
Use of PPE
Electric power Short circuit Electric shock Use of PPE
Supply
IV All shops
Falling from
height
Collapse of
scaffoldings
Injury, breaking
of bone
Proper scaffolding to
withstandLoad
Breaking of slings Use of safety belt
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Tested from time to
time.
Falling of heavy
Objects from height
People working over
Head, next floor
Head injury Use of helmet and
safety belt
Gen.Tor-8(ii) Details Of Exposure If The Workers’ Health Is Being Evaluated By
Pre Designed Format, Chest X-Rays, Audiometry, Spirometry, Vision Testing(Far
& Near Vision, Color Vision And Any Other Ocular Defect) ECG, During Pre
Placement And Periodical Examinations Give The Details Of The Same. Details
Regarding Last Month Analyzed Data Of Above Mentioned Parameters As Per
Age, Sex, Duration Of Exposure And Departmental Wise.
From the periodic monitoring and annual health check up of the employee base of M/s
BEL no trend of disease vectors were identified correlating to the type of job, or period
of job for individuals.
Therefore, it may be inferred that the temporary ailments if identified within the
employee are not related to working conditions.
Gen.ToR 8(iv) Plan and Fund Allocation to ensure Occupational health
and Safety of all contract and casual labors.
M/s BEL has proposal for spending Rs 1.5 cr against occupational health and safety.
Medical check up will be carried out once a year for both contract and casual workers.
Gen.ToR 8(iii) Annual report of health status of workers with special
reference to Occupational Health and Safety
Summary of annual report of health status of workers with special reference to
occupational Health and safety is attached as Annexure VIII
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Sp ToR (ii)The issues raised during public hearing and commitment of
the project proponent on the same along with time bound action plan
to implement the commitment and financial allocation thereto should
be clearly provided.
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7.8 PUBLIC HEARING
Public Hearing for proposed expansion from its 0.6 MTPA Non-Recovery Coke Oven and
40 MW Power Plant to 1.0 MTPA Integrated Steel Plant, 1.2 MTPA Non-Recovery Coke
Oven and 205 MW Power Plant at Dauka, PO- Tentulmuri, PS-Narayangarh, Dist-Paschim
Medinipur, West Bengal by M/s Bengal Energy Limited was conducted on 15.05.2018, at
12.00 hrs at the project site , WB. The Proceedings as submitted by WBSPCB are as
follows:
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Summary of Public Hearing report
Notice was given on 13.04.2018 in local daily ‘Ei Samay” and National daily “The Times
of India “for Public hearing of 1.0 MTPA Integrated Steel Plant, 1.2 MTPA Non –Recovery
Coke Oven and 205 MW of M/s BEL at Dauka, PO-Tentulmuri, Narayangarh, Dist-
Paschim Medinipur, West Bengal.
On 15.05.2018, at 12: 00 hrs, PH was conducted at factory site. Sri S K Meena,
Additional District Magisterate (G) & D.L.L.R.O, Paschim Medinipur presided over the
meeting. Sri S.K Mandal Sr, Environment Engineer were also present.
Points raised in hearing by public and reply & commitment of Sri Navin Maheshwari,
Director of M/s BEL, who represented the management have been given below.
Sl.No Name of Public Issues raised by Public Commitment of P P
1 Sri Sarat Pramanik,
Tentulmuri
Source of water for the
plant and concern on
pollution due to expansion
Water requirement will met from
nearby river for which the company
has requisite permission. Pollution
control norms of statutory
authorities will be followed & proper
control measures will be taken for
abatement of pollution. Green belt
will be further strengthened.
2 Sri Subod Dey,
Khorigaria
Sri Sukumar Das,
Khorigaria
Concern on pollution due to
expansion, its control so as
to provide a better
environment for local
village.
Pollution control norms of statutory
authorities will be followed & proper
control measures will be taken for
abatement of pollution. Green belt
will be further strengthened.
3 Sri Mantu Behari
Patra
Enquired about development
of the area due to expansion
CSR activities are being carried out
regularly and will also continue on
regular basis.
4 Sri Anil Singh,
Banspukuria
Sri Dipak Pal,
Tentulmuri
Employment provision for
local people and their safety
aspects.
The issue will be addressed.
5 Sri Badal Patra,
Tentulmuri
Requested the proponent to
assist local people for health
protection and provide food
like gur and channa to the
labours.
CSR activities are being carried out
regularly and will also continue on
regular basis.
6 Sri Durgapada Das,
Khorigaria
Sri Dhananjoy
Bhuiya,
Khorigaria
Provision of training
programs for skill
development to local and
employment opportunities.
CSR activities are being carried out
regularly and will also continue on
regular basis.
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Sri Bhadreswar
Singh, Nangunia
7 Sri Sujit Khara,
Malka
Concern about control of
pollution and employment
opportunities for locals.
Pollution control norms of statutory
authorities will be followed & proper
control measures will be taken for
abatement of pollution. Green belt
will be further strengthened.
General Public and local bodies were in favour of the proposed expansion project of M/s
BEL,Kharagpur.
ToR 11 Adequate funds(at least 2.5% of the project cost) shall be
earmarked towards the Enterprise Social Commitment based on Public
Hearing issues and item wise details along with time bound action
plan shall be included. Social economic development activities need to
be elaborated upon.
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7.8 CORPORATE ENVIRONMENT RESPONSIBILITY
The capital budget for CER purpose is 1810.00 lakhs (1% of 100 cr + 0.75 % of next 500 cr + 0.5 % of 1000 cr + 0.25 % of 3343 cr) of
the project cost which will be spend towards the sustainability of project as well benefit of the public.
S.N0 Item Description Ist Yr (in lacs)
2nd Yr (in lacs)
3rd Yr (in lacs)
Total (in lacs)
1
Refreshers course to technical persons, on
advanced industrial training and practical
exposure to industries, like process, safety,
disaster etc.
Rent Establishment + Training Material + Stipend+
faculty 60 60 60 180
2 Development of water shed and renovation of
water bodies in Banspukuria, Tentulmuri
villages
12 Nos of New &
Existing water
bodies @ 4 Nos/Yr.
@ Rs 400000
Digging, Paving, de-siltation
& removal of Aquatic weeds 16 16 16 48
3 Construction of village community center and
its renovation 3500000/ Village
3 Villages with community
hall, recreational and study
centers
35 35 35 105
4 Strengthening of approach roads
Proposing 4 km CC
Approach & Village
Roads
Rs 1200000./Km for
widening & strengthening 48 48 48 144
5 Adoptation of primary schools and Anganwadi
Centres
3 Schools & 3
Anganwadi centres
Renovation of the school
building, construction of
toilets, provide bench & desk
25 25 25 75
6 Technical and Infrastructural aid to farmers.
Providing deep irigation points with electricity,
supply of high yield seeds, fertilizer to poor
farmers. The villages will be decided in consulattion
with local administration.
35 30 65 130
7 Promote artisans
Hand loom and generic floor mats, bamboo crafts
are famous cottage industries of the area are in
ruined condition to be resumed with modernisation.
15 22 18 55
8 Swatch Bharat Mission Providing Tractors, Back Hoe cum toploader, dust
bins and development of the dump yard 300 300 225 825
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This will be spent along the construction activities of the project and will cover all the issues raised by public during hearing and as
committed by project proponent.
CONCLUSION
In This chapter a study on Identification of hazards, environmental risk evaluation, disaster management plan, Role of key persons during
hazard. On-site emergency plan, occupational health, occupational Health Hazard, exposure Limits, exposure Controls And Personal
Protection, health hazards. Public Consultation/Public hearing and outcome of public hearing is budgeted in corporate environment
responsibility calculating the value as per the capital cost incurred in the project.
After successful commissioning of the project, what will be its benefit to the society to compensate the adverse impact due to the project
need to be elaborated in the next chapter.
9 Energy efficient street light Electrification of the village with energy efficient
LED bulbs. 77 78 76 231
10 Plantation and distribution of saplings in and
around the villages
Adoptation of 5 villages for plantation and
distribution of saplings 5.4 7.2 4.4 17
11 Total expenditure 1810
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CHAPTER-8
PROJECT BENEFIT
For the sustainability of the project and protection of environment the project proponent
has to spend 18.1 cr of its project cost towards CER activities and this has to be spent
along with setup of project.
These are the indicators of benefits that an integrated steel project can give to the
society around it. Making profit should not be the sole aim of setting up an integrated
steel project. Sustainability of project and environment, which include the people in it
also.
8.1 PROJECT BENEFIT
Infrastructure development.
Direct & indirect Employment opportunity
Revenue generation to central & state government.
Spending 18.1 cr against CER activities as per the issues raised by local public
during Public Hearing.
Trickledown effect of enhance profitability to the local populace.
The comprehensive Environmental Management Plan will focus to completely reduce,
recover, recycling/reuse of treated waste water achieving a zero-discharge standard, the
maximum reuse of solid waste, adequate air pollution control measures so as to keep
the resultant of the ground level concentration well within the NAAQS residential norms
and the adequate green belt cover in one third of the project area for enhancement of
the local ecology. M/s BEL has already achieved Zero discharge for its existing unit and
planning to utilize all its waste products to achieve Zero waste and same principle will be
followed for the expansion project also. All these achievements will obviously nullify the
adverse impacts of the pollution problem. Then the beneficial impacts like the
employment opportunity, improvement in infrastructure facilities, improved business
opportunity etc. will obviously improve the socio-economic conditions of the locality.
8.2 INFRASTRUCTURE DEVELOPMENT
PhysicalInfrastructure
The basic physical systems of a business or nation like Transportation, communication,
sewage, water and electric systems are all examples of infrastructure. These systems
tend to be high-cost investments; however, they are vital to a country's economic
development and prosperity.
Infrastructure is also an asset class that tends to be less volatile than equities over the
long term and generally provides a higher yield. As a result, some companies and
individuals like to invest in infrastructure for its defensive characteristics.
The quality and efficiency of infrastructure services play a pivotal role in achieving the
GDP growth target set for the country. The contribution of the private sectors and Public
sectors in development of infrastructure plays vital role in economic growth of India.
Social Infrastructure
Social Infrastructure is a subset of the infrastructure sector and typically includes assets
that accommodate social services.
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Examples of Social Infrastructure Assets
Sector Examples
Health Medical facilities
Education Schools (primary and secondary)
Tertiary facilities
Residential student accommodation
Housing State or Council housing
Civic and Utilities Local government facilities
Water and wastewater treatment
Transport Bus stands
Need-based road construction (excluding demand-risk
toll roads)
Corrections and Justice Prisons
Court houses
8.3 EMPLOYMENT POTENTIAL
There has been direct employment, where local people have been given preference
according to their education and skill and same procedure will be followed for the
expansion projects also.
There will be additional direct and indirect employment for expansion project. Direct
employment will be 1355. Total man power taking existing, expansion and contract
labors under housekeeping, canteen and security will be about 3,000. The breakup of
manpower will be as follows.
Category-wise break-down of manpower
Category Total
Management personnel 65
Technical specialist 150
Supervisory staff 185
Highly skilled staff 225
Skilled 535
Semi-skilled staff 167
Office staff 28
Total 1355
Indirect employment through contractors and ancillary industries like fly ash bricks etc.
will bring economic development of the area. Skilled, semi-skilled and unskilled people
will be get employment.
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8.4 REVENUE GENERATION TO CENTRAL & STATE GOVERNMENT
Both state and central Govt. will earn through various taxes, excise, permit, license and
services and improve their revenue.
CONCLUSION
This chapter has given a description on the project benefit including infrastructural
development, social development including employment generation, revenue for the
country.
The following chapter will have a brief description on environmental cost benefit analysis
of the project,that is by spending on environment protection, a project is gainer in
various ways.
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CHAPTER-9
ENVIRONMENT COST BENEFIT ANALYSIS
Environmental cost benefit analysis has not been recommended at the scope stage. The
expenses made by project proponent to control soil, water, air and noise and bring into
safe limit for sustenance of flora and fauna and more specifically human health, will be
recovered through minimization of expenses to cure diseases, through sustained crop
yield,
The industry can not survive with contaminated water or polluted ambient air. There will
be massive expenses on account of machine break down or process failure due to water
and air. Employees will suffer from diseases caused due to polluted atmosphere and
there will be loss of man days causing production loss to the company. So the expenses
on environmental pollution control although seems to be high at the start up, its
perennial benefit will be enjoyed by present as well as future generations.
CONCLUSION
The expenses made to control environment for sustenance is given in this chapter, after
all the descriptions regarding the project; at the end it should have a well-defined
Environment management plan. The following chapter gives a broad description on EMP.
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CHAPTER-10
ENVIRONMENTAL MANAGEMENT PLAN (ADMINISTARATIVE)
10.1 EMP IMPLEMENTATION AND MONITORING
Various measures have been suggested in the EMP for mitigation of impacts in earlier
chapters of this EIA report. These have to be implemented according to the suggestions
and monitored regularly to prevent any lapse. This chapter deals with administrative
aspect of ensuring that mitigation measures are physically implemented and their
effectiveness monitored for improvement and implementation of corrective measure if
deterioration is observed.
A large part of the sampling and measurement activity will be concerned with long term
monitoring aimed at providing an early warning of any undesirable changes or trends in
the natural environment that could be associated with the steel plant facilities.
10.2 METEOROLOGY
A meteorological station will be set up at a suitable location to monitor wind speed &
direction, air temperature and humidity on a continuous basis. This data will be used to
identify the zones where air pollution levels due to release of pollutants will be more
than the permissible limits levels.
10.3 EMISSIONS AND AIR QUALITY
Work zone air quality shall be monitored once a month, to assess the levels of
particulate matter inside the steel plant complex. To the extent possible, on line
monitoring for PM, SO2, NOx, CO, and CO2 for each stack will be provided. At least 4 no.
of permanent AAQ station will be stationed around the steel plant and monitoring will be
conducted twice a week.
Emissions from other de-dusting stack will also be monitored once a month. However the
frequency of monitoring may be increased if the West Bengal State Pollution Control
Board desires so.
10.4 DRAINAGE SYSTEM
The effectiveness of the drainage system depends on proper cleaning of all drainage
pipes/channels. Regular checking will be done to see that none of the drains are clogged
due to accumulation of sludge/sediments etc. The clogged drains will be cleaned as soon
as possible, preferably the same day. The catch-pits linked to the storm water drainage
system from the coal handling areas will be regularly checked and cleaned to ensure
their effectiveness. This checking and cleaning will be rigorous during the monsoon
season, especially if rains are forecast.
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10.5 WATER QUALITY
Raw water will be monitored daily. Drinking water being supplied inside the plant and the
township will be monitored at least once a week. Although there is no effluent discharge
outside the plant boundary, however bleed off from system either may be utilized for
firefighting or discharge after proper treatment.
Surface water & Ground water quality to be monitored twice in a year. Pre and Post
monsoon and trend to be observed and corrective measures to be taken.
10.6 NOISE LEVEL
Noise level at various equipments is to be measured once in every three months and
greasing, acoustic enclosure repair, foundation bolt tightening etc to be suggested.
10.7 OCCUPATIONAL HEALTH
Routine medical examination of personnel shall be carried out as systematic programs.
10.8 LABORATORY FACILITIES
The plant’s chemical laboratory may be equipped and manned to carry out the necessary
Environmental monitoring work. Alternately other accredited laboratories may be
contracted for carrying out the necessary environmental monitoring.
10.9 UPDATING OF EMP
The periodicity of monitoring will be governed by the directives from statutory
authorities and prevailing regulations. The action plan of EMP will be updated every year
with respect to the results achieved and to plan activities for the next year.
10.10 ORGANISATION AND MANPOWER
M/s Bengal Energy Limited is having Environmental Management Cell working under
Works Main Controller (WMC) who is also Organizational Head/Director. Environment
Pollution Control Cell with Head of Environment Division, Asst. Environment Engineers,
Chemist, laboratory technicians etc. are reporting to him. Again each plant has its
laboratory to take routine analysis.
The teams in co-ordination with each other look after Environmental aspects of the
project.
The routine work of EMC is as follows:
a. Regular monitoring of stack emission & fugitive emission and report any
abnormalities for immediate corrective measures.
b. Regular monitoring of ambient air quality in and around the plant.
c. Regular monitoring of re-circulating water quality, water quality of the storage
ponds, ground water quality and surface water quality.
d. Regular noise monitoring of the work zone and surrounding area.
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e. Green belt plantation, maintenance, development of other forms of greenery
like lawns, nursery, gardens, etc. along the plant boundary and inside the plant
premises, Colony and Guest House.
f. Regular monitoring of solid wastes quantity and ascertaining avenues for
utilization of solid wastes.
g. Development of schemes for water conservation, rain water harvesting and
reuse of treated wastewater.
Various measures have been suggested in the Environmental Management Plan (EMP)
for mitigation of impacts. These have to be implemented according to the suggestions
and will be monitored regularly to prevent any lapse.
In addition to preparing an EMP, this permanent organizational set up also works to
ensure its effective implementation. Hence, proposed plant will create a team consisting
of officers from various departments to co-ordinate the activities concerned with
management and implementation of the environmental control measures. This team will
undertake the activity of monitoring the stack emissions, ambient air quality, noise level
etc. either departmentally or by appointing external agencies wherever necessary. The
department has a sophisticated Environment Laboratory. Regular monitoring of
environmental parameters will be carried out to find out any deterioration in
environmental quality and also to take corrective steps, if required, through respective
internal departments.
The cell will also be responsible for monitoring of the plant safety and safety related
systems which include:
Checking of safety related operating conditions.
Preparation of a maintenance plan and documentation of maintenance work
specifying different maintenance intervals and the type of work to be performed.
Other responsibilities of the cell will include:
Conduct and submit annual Environmental Audit. A SPCB registered agency will be
retained to generate the data in respect of air, water, noise, soil and meteorological
data and prepare the Environmental Audit report. Timely renewal of Consolidated
Consents & Authorization (CC & A) will also be taken care of.
Submitting environmental monitoring report to SPCB. Data monitored by the cell
will be submitted to the Board regularly and as per the requirement of SPCB. The
cell will also take mitigative or corrective measures as required or suggested by the
Board.
Keeping the management updated on regular basis about the conclusions / results
of monitoring activities and proposed measures to improve environment
preservation and protection.
Conducting regular safety drills and training programs to educate employees on
safety practices. A qualified and experienced safety officer will be employed for the
identification of the hazardous conditions and unsafe acts of workers and advice on
corrective actions, organize training programs and provide professional expert
advice on various issues related to occupational safety and health.
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The comprehensive EMP will also include greenbelt development, disaster
management plan and the peripheral socio-economic development plan for the
region. The impact score with EMP is calculated and found to be slightly positive
and hence the project may be implemented. The EMP will implement by the
“Environment Management Department (EMD)” members created by the
management of the plant.
Industrial activity can have harmful effects on ecological systems, climate and
public health. Recognizing this, Proponents are desired to be committed to reducing their
environmental footprint and promoting environmental stewardship at all levels of their
organizations. A company’s goal must be aimed at minimizing its organization’s impact
and maximize future generations’ ability to live, work, play and shared natural
environment, with equal access to clean air, clean water, and natural resources.
Many corporations have established organization-wide environmental policies to define
and advance their environmental goals. An environmental policy sends a clear message
to employees, vendors, and the community at large that their company considers
environmentally intelligent practices an organizational priority. When a company adopts
such a policy, it’s a meaningful first step in any effort to improve environmental
performance.
Gen.ToR-9(i) Does the company have a well laid down environment
policy approved by its board of directors?
M/s BEL has well defined Environment Policy which has been given below as supplied by
Project Proponent.
In the Policy the company has committed to work towards Environment protection,
prevention of Environmental pollution and Environment improvement around its business
unit and adopt sound environment practice to achieve sustainable growth.
Gen.ToR-9(ii) Does the environmental policy prescribes for
standard operating process/procedures to bring into focus any
infringement/ deviation/Violation of the environmental or forest
norms/ conditions?
It can be seen from the Environment policy of M/s BEL given below that the company
commits to comply with all applicable statutory and other norms/requirements for
environmental protection.
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Environmental Policy of Bengal Energy Ltd ( BEL)
BEL recognizes that as a responsible member of society it has an important duty to
operate in harmony with the environment. We also engage in business with the aim of
contributing to ecologically sustainable development of society through production
activities that respect environmental integrity, and by developing environmental
preservation technologies & methods.
Our Action Plan
1. We aim to carry out environmental tasks in an organized way, and to implement
environmental preservation activities continuously.
2. We will set appropriate objectives and targets for reducing the burden our
activities impose on the environment with conserving biodiversity.
3. We aim to provide society with products and services that contribute to the
preservation of the environment.
We endeavor to increase the social value of our products in terms of
environmental protection, safety and hygiene.
We will provide products and services that reduce environmental loads by
obtaining a clear grasp of environmental needs and developing
technologies.
Our policy for business facilities
Taking into consideration respective business activities, local communities and the
surrounding environments by setting out its own environmental policy, objectives and
targets drawing on methods compliant with international standards. Toward such ends,
BEL continually strive:
To respect laws and regulations and agreements we have concluded with external
parties
To prevent pollution and reduce and appropriately treat waste, and to conserve
the ecosystem
To improve “resource productivity” through implementation of energy efficiency,
resource efficiency, and recycling
To inform employees and other companies residing within our facilities of our policies and require their cooperation
With regard to the observance of laws and regulations, we implemented environmental-
related facilities with strict instruction to follow the rules & regulation of State & Central
policies keeping global warming in our mind.
Gen.ToR-9(iii) What is the hierarchical system or Administrative
order of the company to deal with the environmental issues and for
ensuring compliance with the environmental clearance conditions?
Regular monitoring of environmental parameters like air, water, noise and soil as well as
performance of pollution control facilities and safety measures in the plant are important
for proper environmental management of any project. Therefore, the environment and
safety cell has already been formed to handle monitoring of air and water pollutants as
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well as the solid wastes generation as per the requirements of State Pollution Control
Board and Central Pollution Control Board.
The company has an Environmental laboratory to analyze important pollution parameters
like pH & BOD of water, analysis of raw material, product, noise monitoring near various
equipments etc. However NABL/MoEF Accredited laboratory is being outsourced for
periodic monitoring of stack flue gas, ambient air quality, surface and ground water
quality and other various parameters.
The company has well defined budget towards EMP, Implementation & its yearly
maintenance.
Organization, manpower andhierarchical system
M/s BEL is having Environmental Management Cell(EMC) working under Works Main
Controller (WMC) who is also Organizational Head/Director. Environment Pollution
Control Cell with Head of Environment Division, Asst. Environment Engineers, Chemist,
laboratory technicians etc. are reporting to him. Again each plant has its laboratory to
take routine analysis.
The teams in co-ordination with each other look after Environmental aspects of the
project.
The routine work of EMC is as follows:
a. Regular monitoring of stack emission & fugitive emission and report any
abnormalities for immediate corrective measures.
b. Regular monitoring of ambient air quality in and around the plant.
c. Regular monitoring of re-circulating water quality, water quality of the storage
ponds, ground water quality and surface water quality.
d. Regular noise monitoring of the work zone and surrounding area.
e. Green belt plantation, maintenance, development of other forms of greenery like
lawns, nursery, gardens, etc. along the plant boundary and inside the plant
premises, Colony and Guest House.
f. Regular monitoring of solid wastes quantity and ascertaining avenues for
utilization of solid wastes.
g. Development of schemes for water conservation, rain water harvesting and reuse
of treated wastewater.
Various measures have been suggested in the Environmental Management Plan (EMP)
for mitigation of impacts. These have to be implemented according to the suggestions
and will be monitored regularly to prevent any lapse.
In addition to preparing an EMP, this permanent organizational set up also works to
ensure its effective implementation. Hence, proposed plant will create a team consisting
of officers from various departments to co-ordinate the activities concerned with
management and implementation of the environmental control measures. This team will
undertake the activity of monitoring the stack emissions, ambient air quality, noise level
etc. either departmentally or by appointing external agencies wherever necessary. The
department has a sophisticated Environment Laboratory. Regular monitoring of
environmental parameters will be carried out to find out any deterioration in
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environmental quality and also to take corrective steps, if required, through respective
internal departments.
The cell will also be responsible for monitoring of the plant safety and safety related
systems which include:
Checking of safety related operating conditions.
Preparation of a maintenance plan and documentation of maintenance work
specifying different maintenance intervals and the type of work to be performed.
Other responsibilities of the cell will include:
Conduct and submit annual Environmental Audit. A SPCB registered agency will be
retained to generate the data in respect of air, water, noise, soil and meteorological
data and prepare the Environmental Audit report. Timely renewal of Consolidated
Consents & Authorization (CC & A) will also be taken care of.
Submitting environmental monitoring report to SPCB. Data monitored by the cell
will be submitted to the Board regularly and as per the requirement of SPCB. The
cell will also take mitigative or corrective measures as required or suggested by the
Board.
Keeping the management updated on regular basis about the conclusions / results
of monitoring activities and proposes measures to improve environment
preservation and protection.
Conducting regular safety drills and training programs to educate employees on
safety practices. A qualified and experienced safety officer will be responsible for
the identification of the hazardous conditions and unsafe acts of workers and advise
on corrective actions, organize training programs and provide professional expert
advice on various issues related to occupational safety and health.
The comprehensive EMP will also include greenbelt development, disaster
management plan and the peripheral socio-economic development plan for the
region. The impact score with EMP is calculated and found to be slightly negative
and hence the project may be implemented. The EMP will implement by the
“Environment Management Department (EMD)” members created by the
management of the plant.
Gen.ToR-9(iv)Does the company have system of reporting of non-
compliances/violations of environmental norms to the Board of
Directors of the company and/ or share holders or stake holders at
large.
10.11 FUNCTIONS OF EMP CELL
Functions of EMP cell of M/s BEL are as follows:
a) Maintaining Records
In line with the best practice, M/s BEL has established and maintained a system of
records to demonstrate compliance with the environmental management systems and
the extent of achievement of the environmental objectives and targets. In addition the
other records (legislative, audit and review reports), management records also address
the following:
Details of failure in compliance and corrective action;
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Details of indigents and corrective action;
Details of complaints and follow-up action;
Appropriate contractor and supplier information;
Inspection and maintenance reports;
Product identification and composition data;
Monitoring data;
Environmental training records.
b) Audit
As a mandatory requirement under the Environment Protection Rules (1986) as
amended through the Notification issued by the Ministry of Environment and Forests in
April 1993, an Environmental Statement should be prepared annually. This should
include the consumption of total resources (raw material and water per tons of product),
quantity and concentration of pollutants (air and water discharged, quantity of hazardous
and solid waste generation, pollution abatement measures, conservation of natural
resources and cost of production vis-à-vis the investment on pollution abatement. This
may be internal or external audits, but carried out impartially and effectively by a person
properly trained for it. Broad knowledge of the environmental process and expertise in
relevant disciplines is also required.
c) Environmental Monitoring
Regular monitoring programs of the environmental parameters are essential to take into
account the changes in the environment. The objective of monitoring is:
To verify the result of the impact assessment study in particular with regards
to new developments;
To follow the trend of parameters which have been identified as critical;
To check or assess the efficiency of the controlling measures;
To ensure that new parameters, other than those identified in the impact
assessment study, do not become critical through the commissioning of new
installations or through the modification in the operation of existing facilities;
d) Objectives and Targets
The objectives should be set with a view to realizing gradual and steady improvements
in environmental performance through application of best available and economically
viable technology.
e) Reporting
Performance with respect to monitoring results of various parameters is to be reported in
writing to unit Head as well as statutory body like SPCB. Unit head in turn to intimate
share holders and all stake holders.
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CHAPTER-11
SUMMARY & CONCLUSION
ToR 1 Executive Summary
i) Project name and location
Proposed Expansion project of M/s. BEL is located over 161.87 ha of land at village-Dauka, PO-
Tentulmuri, PS- Narayangarh, Dist-Paschim Medinipur, West Bengal, which extends from 220
15’ 22.96’’ N to 220 15’ 27.68’’ N and 870 22’ 53.37’’ E to 870 23’ 34.69’’ N with, with 32
AMSL appearing on Toposheet No-73M/6 (F45J6). The proposed expansion is confined over the
same land of 161.87 ha.
ii) Products & Capacities (existing & proposed)
M/s. BEL, was granted EC vide J-11011/28/2008-IA II (I), 2nd January, 2009for 0.5 MTPA
Integrated steel in MBF,DRI, EAF & CCM route; 1.2 MTPACoke Oven & 140 MW CPP which
included both WHRB & FBC. But the unit could install 0.6 MTPA Coke Oven & 40 MW CPP and
has now applied and granted ToR for 1.0 MTPA integrated steel, 1.2 MTPA Non-Recovery Coke
OVEN & 205 mw POWER Plant. The configuration & capacities are as given in table below.
Facility Existing Configuration
Existing capacity in TPA
Proposed configuration
Proposed capacity in TPA
Final capacity
Product End use
Non.Recovery CO Plant
1x0.6 MTPA 6,00,000 1x0.6 MTPA 6,00,000 12,00,000 Lam Coke MBF
CPP(Coke Oven gas) 1x40 MW 40 MW 1x40 MW 40 MW 80 MW Elec. Power Internal use/Sale
DRI Kiln - Nil 4x500 TPD
6,40,000 4,48,000
10,88,000 Sponge Iron EAF & IF
4x350 TPD
CPP (DRI) - Nil 68 MW 68 MW Elec. Power Internal use/Sale
MBF,2.7T/m3day - Nil 2x320m3 5,96,000 5,96,000 Hot Metal EAF & IF
Sinter Plant 1x60m2 2T/m2.hr, 340days
- Nil 1x60m2 10,00,000 10,00,000 Sinter MBF
EAF with LF, 16H/day, 325days
- Nil 2x80T 8,32,000 8,32,000 Liq. Steel LF
LF - Nil 1x25T Holding Liq. steel CCM
C C M - Nil 2,500 TPD 8,15,000 8,15,000 Steel Billet Sale
IF 15H/day, 325 days
- Nil 3x20T 2,92,500 2,92,500 Liq. Steel CCM
C C M - Nil 1,000 TPD 2,80,000 2,80,000 Steel Billet Sale
CPP (BF gas fired ) - Nil 1x22 MW 22 MW 22 MW Elec. Power Internal use/Sale
AFBC - Nil 1x35 MW 35 MW 35 MW Elec. Power Internal use/Sale
A S U - Nil 120 TPD 1,200 m3/hr 1,200 m3/hr
Oxygen Nitrogen
Use in MBF & EAF
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iii) a. Requirement of land
The project area is located at Vill-Dauka, Po-Tentulmuri, PS-Narayangarh in Paschim Medinipur district of
West Bengal. The company has in its possession 161.87 ha of land. The proposed expansion will be
accommodated in available vacant area of this land. This is an industrial barren land.
b. Requirement of Raw material with source of supply.
Major Raw material inventory for project after modification cum expansion with source and mode of
transportation is estimated and given below.
Material Gross Capacity in TPA Source Mode of Transport
Coking Coal 16,80,000 Imported Ship/Rail/Road
Non-Coking Coal 17,96,780 Talcher Rail
Iron Ore 19,98,800 Barbil, Banspani Rail
Iron Ore fines 7,68,000 Barbil, Banspani Rail
Dolomite 1,36,000 Biramitrapur Rail/Road
Lime stone 1,39,000 Biramitrapur Rail/Road
Other chemicals required for the proposed project is
Sl No Item Description Unit Quantity Per Annum
1 DM plant resins KG 342
2 Hydrochloric acid KL 178
3 Caustic soda KG 287
4 Lubricants KG 3,112
5 Lubricants LTR 10,015
c. Requirement of water
The total water requirement after the expansion project will be 13,165 m3/day, which will be sourced
from river Kangsabati. Two intake wells at the river, one at Jinsar 220 23’ 34.42” N and 870 21’ 49.32” E
and other at Uttershimla 220 23’ 19.30” N and 870 23’ 05.03” E has been set up. Transportation of water
from river to project site will cover a pipe length of 23.7km and cross canal, NH-6, Howrah-Kharagpur
Rly. Line and pass along the length of NH-60, and outfall at 220 14’ 45.48” N and 870 23’ 23.08” E.
Permission has already been from Government of west Bengal, SE Rly etc. This water project is to supply
10 MGD i.e. 40,920 m3/day and part of job has already been completed.
d. Requirement of Power
Power requirement after expansion will be 153 MW. Own Captive Power generation will be 205 MW.
After usage balance power of 52 MW will be supplied to State Grid.
e. Requirement of Fuel
16,80,000 TPA Coking Coal, 17,96,780 TPA Non coking Coal will be used as fuel in project.
iv) Process description in brief
Steel production in proposed expansion will be in DRI/MBF-IF/EAF- route. Lump Iron Ore along with
Coal and dolomite will be fed to Kilns for sponge iron production. Similarly, Iron ore agglomerate sinter
will be manufactured in sinter plant and will be fed to MBFs with coke, Oxygen, dolomite & pulverised
EIA/EMP Report of M/s Bengal Energy Ltd, At: Dauka, P.O: Tentulmuri,
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coal injection for production of hot metal. Hot metal from MBF & Sponge Iron will be used in IFs and EAFs
for production of liquid steel which will be casted in CCM for production of billets..
v) Capital cost of the project, estimated time schedule
The total project cost has been estimated as Rs 4943 crore. This will include pollution control equipments
which will be installed along with process equipments and a CER cost of 18.10 Crore. The plant will be
commissioned and give commercial production in three after obtaining Environmental Clearance.
vi) Site selected for the project
The project is located at Dauka, Tentulmuri, Paschim Medinipur. The expansion has been proposed in the
acquired area on which existing plant is running. It has well developed infrastructure like road network,
railway siding etc. No national park or wildlife sanctuary or eco sensitive zones or places of
archaeological importance are present within 10 km radius around the project and the site does not come
under critical polluted area. Hence alternate site has not been considered.
vii) Baseline Environmental data.
For the preparation of EIA report a monitoring schedule covering winter season of the year was carried
out from 1st Nov 2017 to 31st Jan 2018. The consultant had engaged NABL accreditated laboratory , M/s
Kalyani Laboratories Pvt Ltd for carrying out monitoring under their strict supervision.The impact
identification started with collection of baseline data such as existing ambient air quality, qualities of
ground water, surface water, soil, noise level prevailing in the area and meteorological parameters like
temperature, humidity, wind speed and direction, cloud cover etc.
Land
The general land use/land cover features of the buffer zone include settlements, agricultural land,
vegetation and forest, collieries both in use & disused, wasteland, water bodies, wet land, and industrial
land, infrastructure and others.
Agriculture land of buffer zone is about 66%, followed by 16.5 % rural settlement and about 3.1% dense
forest.
Water
Kangsabati River is of high significance in the region as it caters to the water requirements of most of the
villages and the majority of the industrial units in the region. River is about 20 km away from the project
site. In 1978, the area was affected by flood and there after no flood hazard has been observed since last
40 years. The mean sea level of the river is 26m and the MSL of the plant is 33 m.
Annual avg. Rain fall project area being 1440 mm and project area 20 ha there will be about 3,81,102m3
of rain water harvested per annum and will meet summer supply to plant i.e. lean period of river
Kangsabati.
The analytical results of surface water samples at different location for various parameters reveal that all
the parameters comply with IS: 2296 (Class ‘C’) standards indicating their suitability for drinking and
other purposes after conventional treatment followed by disinfection.
Similarly the analysis results of groundwater samples showed all the parameters are within the
prescribed limits as per IS: 10500 standards for drinking water.
Climate
Climate in the study region is generally dry and hot and is characterized with seasonal variations of temp.,
humidity, rainfall etc.
Summer is from March to June. South West monsoon brings rain to the area from mid June to September.
Post monsoon are October & November. November to February are winter in the area.
The area receives fairly good amount of rainfall from the southwest monsoon during June to September.
Light showers of rain occur during the months of October, November and sometimes in December also
Annual Average rain fall 1440 mm
Meteorological conditions In order to determine the micrometeorological conditions of the study area a temporary micro-
meteorological monitoring observatory was set up near the site from Nov 2017-Jan 2018. The results
EIA/EMP Report of M/s Bengal Energy Ltd, At: Dauka, P.O: Tentulmuri,
P.S: Naraingarh, District: Paschim Medinipur, West-Bengal
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were compared with data of IMD station Midnapore. At the site Overall predominant wind direction has
been from North and the North East direction during study period.
The average wind velocity found to be 3.72 m/s and the calm period is 34.83%.
Ambient air
The study area represents mostly industrial environment. Air quality in the project area is affected by the
presence of polluting industry nearby. The prominent sources of air pollution in the study area are due to
emission from industries, vehicular movement and domestic coal burning as fuel in some parts of the
study area.
During the study period, the concentrations of PM10 measured to vary between 93.6-61.9 g/m3 at
different locations of the study area. The concentrations of PM2.5 varied between 49.8-27.2 g/m3 at
different locations of the study area. During the study period, the average levels of SO2 concentrations at
all location varied from 15.4-6.1 g/m3. The concentrations of NOX values varied between 28.7-10.5
g/m3 at different locations. The concentrations of CO value ranged between 789-342 µg/m3 at different
locations during the study period
Soil analysis
The study area analysis results of the soil parameters show deficiency normal nutrients and micro
nutrients of. The bulk density of the study area ranges from 1.13 to 1.3 gm/cc. The other nutrient content
like nitrogen, potassium and phosphate content of the soil is very low indicating land not suitable for
agriculture purposes. This is to be taken care of in agricultural land as well as growing trees for green
belt.
Flora and Fauna
Flora and Fauna of the study area reveals that no Schedule- I type of fauna found in the study area. In
faunal population; cattle, goats, dogs, rats, insects are common in the study area.
As per IUCN's "Red Data Book", none of the taxa found in this region could be marked as rare or endangered plant species.
Socio Economic
The socioeconomic features around the 10km radius of the plant site have been collected through
primary and secondary data collection. The study area covers 12425 inhabitants. Out of the total
population 53 % are male and 43% are female. SC population is 25%, ST 1.0% and other 74%. 57 % of the
total population is literate.
Priority to be given to local people in employment in proposed expansion project to improve economy of the locality. viii) Identification of Hazard in handling, processing and Storage of material and safety systems
provided.
All the shops will have their own list of hazards, which have been identified and damage to human being
and environment has been discussed with risk management, which can reduce if not mitigated fully. The
major on-site emergency situation may occur from storage and handling, fuel gas, molten metal and slag
handling, acids, alkali storage and handling and electrical short-circuit. Proper safety equipments will be
provided to the workers and proper standard operating procedure will be followed during handling and
processing hazardous material. Hazards in various working area have been identified, its severity has
been estimated and mitigation has been suggested.
Hazard Identification & Risk Analysis for different units has been addressed with identification of most
critical hazard operations.
ix) Likely Impact of the project on air, water, land, flora fauna
Air Environment:
The pollutant emissions from the proposed project will have maximum ground level concentration as
33.48 µg/m3 for PM10, 31.23 µg/m3 for PM2.5, 44.65µg/m3 for NOx and 62.18 µg/m3 for SO2. With
installation of APC systems like bag filters, and ESPs the maximum ground level concentration will come
down to 2.53 µg/m3 for PM10, 1.49 µg/m3 for PM2.5 and 34.11 µg/m3 for SO2.
However there will be occasions when dust venting may be forced due to APC failure although inter
locking provision has been suggested for tripping the unit. Action plan has been suggested to protect
crops of the villagers during such situations. In case of failure of APC immediate action will be taken at
most impact points with water jet mixed system which will be truck mounted.
EIA/EMP Report of M/s Bengal Energy Ltd, At: Dauka, P.O: Tentulmuri,
P.S: Naraingarh, District: Paschim Medinipur, West-Bengal
217 Global Tech Enviro Experts Pvt. Ltd.
Water Management
As the plant water system is designed based on maximum recirculation system. The effluents likely to be
generated from the proposed plant are:
Backwash Waste from Filtration Plant;
Run-off water from Raw Material Storage Yards;
Waste Water from Billet Caster;
Cooling tower blow-down of various shops; and
Plant Sewage & Canteen Effluents.
The effluents will be treated in ETP and will be reused. M/s BEL abides to Zero Discharge Liquid norms
for its existing plant. Rain water harvesting will be done to reduce raw water drawl during lean period of
Damodar.
Noise Pollution Management
The noise level within the plant boundary is occupational noise levels and confined within shops. The
level will be further minimized when the noise reaches the plant boundary and the nearest residential
areas beyond the plant boundary, as elaborate green belt development is envisaged for all along the
boundary for attenuation of noise and fugitive emission. All the equipment in the steel plant will be
designed/operated in such a way that the noise level shall not exceed 85 dB (A) as per the requirement of
Standard.
Solid Waste Management
The comprehensive EMP enlists the management plan for each individual unit.
Solid waste Quantity in
TPA
Utilisation measures
EAF & IF slag 1,20,000 Use in construction work
IF & EAF flue dust 24.000 Will be used in making sinter for use in BF
DRI Dolchar 2,72,000 Use in AFBC to generate steam for power generation
Power plant Fly ash 1,50,750 Supply to Gava Ecocrete Pvt Ltd as per MOU.
DRI ash & dust 5,75,600 Land feel and dump in abandoned coal mines for which
permission to be sought
BF slag 1,84,760 To be used in sinter plant & balance to be Sold to ASO
Cement Ltd as per MOU 20.09.2018
BF sludge + dust 2,93,670 To be used in sinter plant & balance to be Sold to ASO
Cement Ltd as per MOU 29.09.2018
Power plant Bottom Ash 1,00,500 Sold to Gava Ecocrete Pvt Ltd, MOU 30th August, 2018
In case of excess BF slag and sludge over sale, this can be used as raw material for iron ore sinter making.
Measures for Improvement of Ecology:
There is no wildlife sanctuary within the 10 km radius of the proposed plant. The core zone area is devoid
of plantation. There will not be any loss of plantation because of the project. On the other hand, the
company will provide the comprehensive green-belt cover in 33 % of the project area as per the MoEFCC
norms to improve the local ecology. The company plans to acquire the nearby abandoned coal quarries
with deep gorges and holes and will fill the same with the non-hazardous solid waste and will develop
thick green belt cover over the sites. All these steps will considerably improve upon the ecology of the
area.
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P.S: Naraingarh, District: Paschim Medinipur, West-Bengal
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x) Impact Mitigation Measure
Gaseous Emission
e. Hot flue gas with particulate matter, SO2, CO2 and NOx will be generated from DRI kilns, Flue gas
will pass through, DSC, ABC & ESPs for separation of particulate matter and clean gas will be
sucked by ID fans and vented to atmosphere through high stack. Efficiency of ESPs being >99%,
particulate matter emission will come down. In the existing plant 1 no. of ESPs for Cement
rinding units is installed and additional 4 ESPs and 5 Bagfilters will be installed.
f. Fumes generated from Induction Furnace will be cleaned in bag filters and vented to atmosphere
through ID fan and stack. Emission will come down.
g. Sinter plant and FBC will have ESPs to clean gaseous emission which are then sucked by ID fans
and vented to atmosphere.
h. Both DRI Kiln flue gas, Coke Oven gas will have WHRB boiler for removal of heat for generation of
steam for power. Ventury scrubber will be used in MBF to remove particulate matter in the form
of sludge. BF dust and sludge having residual carbon will be used in making sinter.
With this pollution control measure the resultant ground level concentration will come down from
estimated value as follows.
PM10 from 33.48 to 2.53 µg/m3, PM2.5 from 31.23 µg/m3 to 1.49 µg/m3, SO2 from 62.18 to 34.11
µg/m3
Liquid Effluent
d. Industrial waste water from MBFs, DRI kilns and CPP will pass through ETP, where
neutralization and settling will take place. After treatment the turbidity will come down from 60
to <15 NTU, oil & grease from 31 to <5PPM and suspended particle from 1000-5000 to <30 PPM.
e. Domestic waste water will pass through STP having equalization, aeration and settling tank.
Industrial and domestic effluent water after settling tanks will undergo filtration through gravel
& sand bed and will be used for toilet flushing, green belt watering, dust suppression and vehicle
washing.
f. Water quenching will be avoided and dry quenching will be adopted for red hot coke. This will
eliminate waste water generation and treatment from Coke Oven Plant.
Solid and Hazardous Waste
d. Fly ash and bottom ash from CPP will be supplied to Gava Ecocrete Pvt Ltd as per MOU for fly ash
brick manufacturing. Bottom ash , fly ash and kiln accretion from DRI kiln will be used as road
making and land fill material. Possibility of dumping DRI ash & dust in abandoned coal mines to
be explored.
e. BF slag & sludge will be utilized in sinter making and balance will be sold to ASO Cement Ltd as
per MOU. IF slag normally contains about 15% Iron, hence slag will be cooled, crushed and
undergo magnetic separation. Residual iron thus recovered will be recycled to IF for re-melting
and slag which has high silica content and equivalent to river sand will be used as construction
material/land fill.
f. Used oil, DM plant resins and lead batteries like hazardous materials will be handed over to
authorized dealer/suppliers
xi) Hazard Identification & Risk Analysis
It may be observed that the major on-site emergency situation may occur from coal & chemicals storage
and handling; fuel gas handling, molten metal and slag handling, acids and alkali storage and handling and
electrical short-circuit. The off-site environmental disaster may occur if large-scale fire and explosion
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P.S: Naraingarh, District: Paschim Medinipur, West-Bengal
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occurs, the effect of which extends beyond the plant boundary. The off-site environmental disaster may
occur due to significant environmental degradation for a sustained period.
Probable Hazards has been identified through the process of HIRA for major units like ASU, DRI, SMS,
Rolling mill, Sinter & CPP. The respective mitigation majors are also enlisted along with the onsite
emergency Plan. The Environmental management plan includes the environmental Risk mitigation
measures.
BEL has a well-developed Disaster Management Plan consisting of the preparedness plan for onsite and
offsite disasters and the role of key persons during occurrence of any disaster. An emergency cell headed
by Works Main Controller and followed by Site Controller, Combat Leader, Rescue team operates to
prevent any type of disaster. The DMP also states the activation and closing procedure for onsite
emergency along with the responsibilities of each member.
xii) Issues raised during Public Hearing
Public Hearing for proposed expansion from its 0.6 MTPA Non-Recovery Coke Oven and 40 MW Power
Plant to 1.0 MTPA Integrated Steel Plant, 1.2 MTPA Non-Recovery Coke Oven and 205 MW Power Plant at
Dauka, PO- Tentulmuri, PS-Narayangarh, Dist-Paschim Medinipur, West Bengal by M/s Bengal Energy
Limited was conducted on 15.05.2018, at 12.00 hrs at the project site, WB.
Sl.No Name of Public Issues raised by Public Commitment of P P
1 Sri Sarat Pramanik,
Tentulmuri
Source of water for the plant and
concern on pollution due to
expansion
Water requirement will met from nearby
river for which the company has requisite
permission. Pollution control norms of
statutory authorities will be followed &
proper control measures will be taken for
abatement of pollution. Green belt will be
further strengthened.
2 Sri Subod Dey, Khorigaria
Sri Sukumar Das,
Khorigaria
Concern on pollution due to
expansion, its control so as to
provide a better environment for
local village.
Pollution control norms of statutory
authorities will be followed & proper
control measures will be taken for
abatement of pollution. Green belt will be
further strengthened.
3 Sri Mantu Behari Patra Enquired about development of
the area due to expansion
CSR activities are being carried out
regularly and will also continue on regular
basis.
4 Sri Anil Singh, Banspukuria
Sri Dipak Pal, Tentulmuri
Employment provision for local
people and their safety aspects.
The issue will be addressed.
5 Sri Badal Patra, Tentulmuri Requested the proponent to
assist local people for health
protection and provide food like
gur and channa to the labours.
CSR activities are being carried out
regularly and will also continue on regular
basis.
6 Sri Durgapada Das,
Khorigaria
Sri Dhananjoy Bhuiya,
Khorigaria
Sri Bhadreswar Singh,
Nangunia
Provision of training programs
for skill development to local and
employment opportunities.
CSR activities are being carried out
regularly and will also continue on regular
basis.
7 Sri Sujit Khara,
Malka
Concern about control of
pollution and employment
opportunities for locals.
Pollution control norms of statutory
authorities will be followed & proper
control measures will be taken for
abatement of pollution. Green belt will be
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further strengthened.
xiii) CER Plan with proposed expenditure
The company will spend 18.10 crores of its project cost on CER activities based on circular . This will be
spent along the construction activities of the project and cover all the issues raised by public during
Public Hearing and as committed by project proponent.
S.N0 Item Description Ist Yr (in lacs)
2nd Yr (in lacs)
3rd Yr (in lacs)
Total (in lacs)
1
Refreshers course to technical
persons, on advanced
industrial training and
practical exposure to
industries, like process, safety,
disaster etc.
Rent Establishment + Training Material +
Stipend+ faculty 60 60 60 180
2
Development of water shed
and renovation of water bodies
in Banspukuria, Tentulmuri
villages
12 Nos of New &
Existing water
bodies @ 4
Nos/Yr. @ Rs
400000
Digging, Paving, de-
siltation & removal
of Aquatic weeds
16 16 16 48
3
Construction of village
community center and its
renovation
3500000/ Village
3 Villages with
community hall,
recreational and
study centers
35 35 35 105
4 Strengthening of approach
roads
Proposing 4 km CC
Approach &
Village Roads
Rs 1200000./Km for
widening &
strengthening
48 48 48 144
5 Adoptation of primary schools
and Anganwadi Centres
3 Schools & 3
Anganwadi
centres
Renovation of the
school building,
construction of
toilets, provide
bench & desk
25 25 25 75
6 Technical and Infrastructural
aid to farmers.
Providing deep irigation points with
electricity, supply of high yield seeds,
fertilizer to poor farmers. The villages will
be decided in consulattion with local
administration.
35 30 65 130
7 Promote artisans
Hand loom and Dhokra metal casting are
famous cottage industries of the area are
in ruined condition to be resumed with
modernisation
15 22 18 55
8 Swatch Bharat Mission
Providing Tractors, Back Hoe cum
toploader, dust bins and development of
the dump yard
300 300 225 825
9 Energy efficient street light Electrification of the village with energy
efficient LED bulbs. 77 78 76 231
10 Plantation and distribution of
saplings in and around the
Adoptation of 5 villages for plantation and
distribution of saplings 5.4 7.2 4.4 17
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villages
11 Total expenditure 1810
xiv) Occupational Health Measures
Sl. No. Group Item Potential Health hazard Preventive measures
I Raw materials and products handling
Iron ore & Coke, Eye/skin irritation Water sprinkling’ Coal , lime stone/Dolo Respiratory track diseases Dry fogging in
conveyors, ID fan Other fluxing minerals due to Dust, burning due to bag filter, PPE like
safety shoes, Product steel local fire Dust mask and safety
goggles. Acids/Alkalis Water jet for eye
washing II Major shops DRI kiln flue gas CO, dust, heat Pollution Control
Equipments for direct exhaust of the gas
Sinter Plant Dust, heat, Respiratory track diseases, Well ventilation of work place with air ventilating systems
noise Head Ache PPE like gloves, dust mask to prevent dust inhalation
Captive power plant
Fly ash, explosion, noise, vibration, HT, electric equipments, Acid and alkali
Electric shock, injury due to chemicals, burn/ eye injury
Use of PPE, barricading high voltage area.
III Utilities Fuel gas Gas leaks Fire and gas Use of PPE
Distribution Poisoning Electric power
Supply Short circuit Electric shock Use of PPE
IV All shops Falling from
height Collapse of scaffoldings Injury, breaking of bone Proper scaffolding to
withstand Breaking of slings Load and use of safety
belt Tested from time to time.
Falling of heavy People working over Head injury Use of helmet and safety shoes Objects from
height Head, next floor
xv) Post Project Monitoring Plan
Depending upon prevailing predominant wind direction AAQ monitoring stations have been decided
where monitoring instruments shall be installed for measuring polluting parameters at regular intervals.
Similarly Fugitive emission will be monitored twice a month and Stack monitoring will be continuous
with Online monitoring systems. Three locations has been identified for Ground Water and Surface water
monitoring which will be carried out twice in a year. ETP, STP, CT will be monitored once a month or as
per the Standard Operating Procedures.
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P.S: Naraingarh, District: Paschim Medinipur, West-Bengal
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CHAPTER -12
CONSULTANT PROFILE
(A Techno-Enviro Consultant)
(Earlier Named as Global Experts)
NABET Accreditated consultant (Serial No 78) & SPCB, Odisha Empanelled
Consultant.
M/s Global Tech Enviro Experts Pvt. Ltd. (GTEEPL) is a professionally managed quality
conscious organization, which provides environmental solutions to various industrial
organizations with sustainable growth and environmental friendly ecosystem. It is a
competent technical organization providing environmental solutions with latest technical
know how, legal advice, liasioning with various authorities and community at large. More
than 60 industries have engaged Global Experts as their consultant to obtain
environmental & statutory clearances from various statutory bodies and Government
Agencies. Presently more than 10 nos. of Integrated Steel Plants (Signed MoU with Govt.
of Orissa) have engaged Global Experts for carrying out their EIA/ EMP Studies and other
allied environmental clearances. The Global Experts is the first consultant in Orissa to
prepare REIA/ EMP Study report for 1.5 MTPA Integrated Steel Project in Orissa.
Recently Global Experts is been engaged in environmental clearance from MoEF, New
Delhi, VISA Steel Ltd., ACC Bargarh Cement Works, Dungri Limestone Quarry, SPS Steel
and Power Ltd., Maithan Ispat Ltd., various mines of Adhunik Metaliks Ltd. M/s Global
Experts is the first consulting firm in Eastern and North-Eastern region of India to
undertake the EIA/EMP Study along with Liasioning for MoEF clearance for Vedanta
International University Project. Global Experts has a distinct track record in the field of
liasioning with local public in order to carry out Public Hearing jobs for different Steel
Plants to their utmost satisfaction. Our Internal resources and technical acumen blended
with highest degree of Public Relationship has been our strength in providing a total
solution for Environmental aspects of Mines and Industries.
The technical team of Global Experts has wide experience in design, engineering,
erection & commissioning of various pollution control devices, carrying out statutory
Audits, drawing of water pipe line, Water and Air Quality modeling, Mine Plans, designing
of Intake Well and other technical assignment for various industries.
Global Experts is also deeply involved in Hazardous Waste Audits, and Water Harvesting
Projects etc. We are associated with Administrative Staff College of India (ASCI) for the
hazardous waste Inventorisation of all industries in Orissa for their initial preparation.
SERVICES:-
Environmental:
Environment Impact Assessment
Environmental Management Plan
Pollution Prevention & Control (Design, Installation & Maintenance of ETPs, Air
Pollution Control Equipment).
Preparation of Comprehensive EMP mitigation measures, advising on air pollution
control, wastewater treatment.
Municipal Solid Waste Management (Vermin-technology & Bio-Technology),
Industrial Waste, Urban Waste
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Environmental Monitoring & Survey.
Greenery Management (Plantation, Maintenance, Nursery raising & Sailing of
seedling)
Watershed Management
Liasioning with OSPCB, CPCB & MoEF
Environment Auditing, Energy Auditing, Assessing the performance of
environmental systems, environmental liabilities.
Bio-medical Waste Management
Third Party Hazardous Waste Audit
Environmental Monitoring (Air, Water, Soil)
Laboratory Testing of different samples in Laboratory
Techno-Functional:
Site Selection & Procurement of land.
Design, Erection & Commissioning of industrial units, water treatment plant,
Effluent Treatment Plant, Sewage Treatment Plant etc.
Preparation of Mining Plan, Environmental Clearance, Forest Diversion Proposal
Rehabilitation & Reclamation.
Liasioning with statutory authorities.
Mechanical Fabrication.
Engineering Designing
Turnkey Projects
Preparation of DPR for Integrated Steel Plants
Preparation of DPR for MSW Management practices
Preparation of Feasibility Report for Water Pipeline & Intake-well Design,
Supervision & Commissioning
Design, Erection & Commissioning of Dust Suppression Equipments like Sprinkler
System, Dry Fog System & Scrubber etc.
Dust Extraction System like Cyclone & Bag filter.
The list of participatory functionaries in preparation of this EIA is enclosed below
along with the credentials validating the firm for this purpose.
Declaration by Experts contributing to the EIA of M/s. KIC Ltd
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I, hereby, certify that I was a part of the EIA team in the following Capacity
that developed the above EIA.
Declaration by the Head of the accredited consultant organization/ authorized
person
I, Manoranjan Nayak hereby, confirm that the above mentioned experts prepared the
EIA/EMP report of M/s. KIC Metaliks Ltd. I also confirm that the consultant organization
shall be fully accountable for any mis-leading information mentioned in this statement.
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Signature:
Name: Manoranjan Nayak
Designation: Managing Director
Name of the EIA consultant organization: Global Tech Enviro Experts Pvt. Ltd.
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The baseline environment monitoring of M/Bengal Energy Ltd has been carried out by
M/s Kalyani Laboratories Pvt Ltd, MoEF accreditated laboratory. The accreditation
certificated is enclosed herewith:
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NABL Accreditation Certificate