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112th meeting of SEAC-Gujarat, Dated 17.12.2020
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Minutes of the 112th meeting of the State Level Expert Appraisal Committee held on 17th
December 2020 through Video Conference (VC) on National Informatics Centre (NIC).
In the wake of recent crisis of COVID-19, lockdown situation, the agenda of the present meeting
was mailed to expert Committee in advance and a Video conference meeting on NIC was
organised in this regard on 17/12/2020 at 13.30 hrs.
The 112th meeting of the State Level Expert Appraisal Committee (SEAC) was held online by
Video conferencing on 17th December 2020 at 13.30 hrs. Following members joined the meeting:
1. Shri Akshay Kumar Saxena, Chairman, SEAC
2. Dr. S. C. Pant, Vice Chairman, SEAC
3. Dr. M. N. Patel, Member, SEAC
4. Shri D. C. Chaudhari, Member, SEAC
5. Shri J. K. Vyas, Member, SEAC
6. Shri Anand Zinzala, Member, SEAC
7. Shri B. M. Tailor, Member, SEAC
8. Shri A. V. Shah, Secretary, SEAC
The Committee considered the applications made by project proponents, additional details
submitted as required by the SEAC/SEIAA and details furnished in the Form-1, PFR, EMP reports
etc.
1. SIA/GJ/IND2/173344/2020 M/s Hitesh corporation
Plot No. 6504,Near Hoeschst Chowkadi,
GIDC Estate Ankleshwar, Dist-Bharuch
Appraisal
Category of the unit: 5(f)
Project status: New
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173344/2020 on dated
05.10.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
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This is a new unit proposes for manufacturing of synthetic organic chemicals [API and API Intermediates]
as tabulated below,
Sr
.
N
o.
Products API OR
INTERMEDIATE CAS No.
Qty.
(MT/
Mont
h)
End Use
1 BetaMethasone Sodium
Phosphate API 151-73-5
20
Corticosteroid
2 BetaMethasone Valerate API 2240-28-0 Medication-
Corticosteroid
3 BetaMethasone Dipropionate API 5593-20-4 Corticosteroids
4 DexaMethasone Sodium
Phosphate API 2392-39-4 Anti-inflammatory
5 Clobetasol Propionate API 25122-46-
7
Medicine -
corticosteroid to treat
skin conditions such
as eczema, contact
dermatitis, seborrheic
dermatitis, and
psoriasis.
6 Progesterone API 57-83-0
Treating abnormal
uterine bleeding
associated with
hormonal imbalance.
7 Progesterone Acetate API 302-23-8
Tablets are indicated
to treat secondary
amenorrhea, reduce
the incidence of
endometrial
hyperplasia in
postmenopausal
women, and to treat
abnormal uterine
bleeding due to
hormonal imbalance,
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not organic
pathology.
8 Mifepristone API 84371-65-
3 Abortion
9 Pyridoxine HCl API 58-56-0
It is used to prevent
or treat low levels of
vitamin B6 in people
who do not get
enough of the vitamin
from their diets.
10 Nandrolone Decanoate Ip. BP. API 360-70-3
Anemia, chronic renal
failure, osteoporosis
and AIDS.
11 In-house R & D ----- ----- 0.1 ----
TOTAL 20.1
ENDUSE OF PRODUCTS
Sr.
No.
Name of
the
Product
CAS No.
(Product)
Type/
Category of
Product
(API/
Intermediate)
In case of Intermediate stage of
API
Said API is
used for/End
Use of said API
Stage of
Intermediat
e
n-1, n-2,
etc
Name of API
in which
Intermediate
Used/ End
use of said
Intermediate
CA
S
No
.
(A
PI)
1 Beta
Methas
one
Sodium
Phosph
ate
151-73-5 API --- --- ---
Corticosteroid
2. BetaMet 2240-28- API --- --- --- Medication-
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hasone
Valerate
0 Corticosteroid
3. BetaMet
hasone
Dipropio
nate
5593-20-
4
API --- --- ---
Corticosteroid
s
4. DexaMe
thasone
Sodium
Phosph
ate
2392-39-
4
API --- --- ---
Anti-
inflammatory
5. Clobeta
sol
Propion
ate
25122-
46-7
API --- --- --- Medicine -
corticosteroid
to treat skin
conditions
such as
eczema,
contact
dermatitis,
seborrheic
dermatitis, and
psoriasis.
6. Progest
erone
57-83-0 API --- --- --- Treating
abnormal
uterine
bleeding
associated
with hormonal
imbalance.
7. Progest
erone
Acetate
302-23-8 API --- --- --- Tablets are
indicated to
treat
secondary
amenorrhea,
reduce the
incidence of
endometrial
hyperplasia in
postmenopaus
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al women, and
to treat
abnormal
uterine
bleeding due
to hormonal
imbalance, not
organic
pathology.
8. Mifepris
tone
84371-
65-3
API --- --- --- Abortion
9. Pyridoxi
ne HCl
58-56-0 API --- --- --- It is used to
prevent or
treat low levels
of vitamin B6
in people who
do not get
enough of the
vitamin from
their diets.
10
.
Nandrol
one
Decano
ate Ip.
BP.
360-70-3 API --- --- --- Anemia,
chronic renal
failure,
osteoporosis
and AIDS.
The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr.
no.
Particulars Details
A
A-1 Total cost of Proposed Project
(Rs. in Crores):
3.4 Crores
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Break-up of proposed project Cost:
Details Project Cost
(Rs. In Crores)
Land 1.0
Building 0.7
Machinery 0.8
Environment
Protection and
Safety
0.87
A-2 Details of Environmental Management Plan (EMP) As below:
Component Capital Cost of EMP Recurring Cost of EMP
(per Month)
Cost 87 Lakh 8 Lakh
Sr.N
o.
Unit
Detail
Capital Cost
[Rs. in
Crore]
Operating
Cost [Rs.
in Crore]
Maintenan
ce Cost
[Rs. in
Crore]
Total
Recurring
Cost (Rs.
In Crore)
1 Waste Water 8 KLD 0.10 0.06 0.0020 0.06
2 Air - 0.15 0.0034 0.003
3
Hazardous
Management -
0.13 0.01 0.01
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4 Fire & Safety - 0.15 0.0008 0.001
5 AWH Monitoring - 0.02 0.0007 0.001
6
Green Belt
Development 40 %
0.04 0.0002 0.0002
7
Occupational
Health -
0.06 0.0050 0.0050
8 CER Activity 4% of total
Cost 0.136 0.0000 0.00000
9 PLC System - 0.08 0.0002 0.0002
Total 0.87 0.07 0.012 0.085
Summary
Cost of Project in Crores per
Annum:
3.4 Crore
EMP Capital Cost in Crores per
Annum and Percentage:
0.87 Crore[25%]
EMP Recurring Cost in Crores
per Annum and Percentage:
1.0 Crore
A-3 Details of CER as per OM dated 01/05/2018 (In case of project falls under CPA/SPA, CER
fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA
and 2 times for CPA in case of Environmental Clearance as per the mechanism published
vide MoEF&CC‘s OM vide 31.10.2019.)
% as per the OM Rs. in Crores
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4% 0.136 Cr
Brief note on proposed activities:
Unit has planned 4% of the total cost of the proposed project (3.4 Cr.) So unit use
13.6 Lakhs in CER Activities.
CER Budget : 13.6 lakh (for Three Years 2021-2023)
Activity Amount
We will provide required instruments in Civil hospital for
medical treatment and improve facilities in Civil hospitals.
Hospital Bed,Instruments,Laboratory
13.6 Lakh
B Land / Plot ownership details:
B-1 Plot area
Total Plot area
1888 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
➢ Land Area Break-ups
Sr. No. Land Use
Proposed
Area
(Sq. MT)
% First Floor Second
Floor
1 Production plants 160 8.5 160 160
2 Administration 24.91 1.3 24.91
3 OHC 28.62 1.5
4 Lab 25.59 1.4
5 ETP 73.8 3.9
6 Utilities 30 1.6
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7 Raw Material Storage 90 4.8
8 Finished Product Storage 50 2.6
9
Hazardous Waste
Storage Area 81 4.3
10 Solvent Storage Area 72 3.8
11 Under Ground Tank Area 24.38 1.3
12 Green Belt 755 40.0
13 Road & Security cabin 472.7 25.0
Total 1888 100
As per calculation Unit will manufacture capacity of 20.1 MT/Month. So, Adequate Area will
be available to manufacture the proposed product. Production plant area will be 160 Sq. m.
B-3 Green belt area
Total (Sq. meter)
Area in Sq. meter 755
% of total area 40 %
C Employment generation
Total
10 Nos.
D Water
D-1 Source of Water Supply
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(GIDC Bore well, Surface water, Tanker supply etc...)
Status of permission from the concern authority.
➢ we are attached here Annexure.[No.:NTA/ANK/DEE(WS)/1286
D-2 Water consumption (KLD)
Category
Quantity
KLD
Remarks
(A) Domestic 1.0
(B) Gardening 1.0
(C) Industrial
Process 3.2
Washing 1.0
Boiler 3.0
Cooling 2.0
Others 0.3+0.02 Scrubber & R&D
Industrial Total 9.52
Grand Total (A+B+C) 11.52
Brief Note on worst case scenario for water consumption:
➢
Product Water consumption Wastewater
Generation
Betamethason
e Dipropionate
3.2 KLD 3.9 KLD
Summary of Quantity KLD Remarks
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water
requirement
Total water
requirement for
the project (A)
11.52
Quantity to be
recycled (B)
1.5
Total fresh
water
requirement (C)
10.02
Ensure Total water requirement = Fresh water +
Recycled water i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility. [Source of reuse
& application area]
Source
of waste
water for
reuse in
KLD
(From
where it
is
coming)
Application
area with
quantity in
KLD (Where
it is used)
Characteristi
cs of waste
water to be
reused
(COD, BOD,
TDS etc.)
Remarks
regarding
feasibility to
reuse
Boiler
Condens
ate
1.5 KLD
Cooling &
Washing
[1.0KLD+1.5
KLD]
PH:6.5-8.0
COD:100-
200 mg/L
TDS:400-
500 mg/L
In case of no reuse/recycle of waste water, Give brief note on
justification as why no reuse/recycle.
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➢ Not Applicable
D-3 Waste water generation (KLD)
Category Waste water KLD Remarks
(A) Domestic 0.5
(B) Industrial
Process 3.9
Washing 1.0
Boiler 0.5
Cooling 0.5
Others 0.31+0.02 Scrubber & R&D
Total Industrial waste
water
6.23
Total [A + B] 6.73
-
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative):
QUALITATIVE AND QUANTITATIVE ANALYSIS OF EACH WASTE STREAM :-
Sr.
No.
Source of
WasteWater
Generation
Quantity in
KL/Day
Parameter
Quality Final load
at ETP in
Kg/day
1 Boiler 0.5 pH 6.5-8.0 --
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blowdown
COD 200-300 mg/L 0.15
TDS 600-700 mg/L 0.35
2 Cooling Tower
blow down
0.5 pH 6.0-8.5 --
COD 400-500 mg/L 0.2
TDS 700-800 mg/L 0.4
3 Washing 1.0 pH 5.0-6.5 ---
BOD 200-400 mg/L 0.4
COD 600-700 mg/L 0.7
TDS 800-1000 mg/L 1.0
4 Process 3.9 pH 3.0-6.5 ---
BOD 6000-8000 mg/L 31.2
COD 20000-25000 mg/L 97.5
TDS 30000-35000 mg/L 136.5
Total Industrial
Effluent
5.9
CHARACTERISTICS OF WASTEWATER BEFORE & AFTER TREATMENT
(ETP-P+CMEE-BEIL)
Sr.
No. Parameter Unit Before
Treatment
After Primary Treatment
1. pH -- 3.0-6.5 5.0-8.0
2. BOD mg/L 5,000-6,000 4,000-5,000
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3. COD mg/L 15,000-20,000 12,000-17,000
4. TDS mg/L 20,000-25,000 23,000-28,000
Brief justification in case of no process effluent generation or no industrial effluent generation or no
high concentration effluent generation from proposed project (If any applicable to proposal).
-Not Applicable
D-4 Mode of Disposal & Final meeting point
-
Domestic: ● Domestic wastewater will be sent to the primary ETP.
Industrial: ● Industrial waste water will be collected and treated into the primary ETP treatment plant and treated effluent will be sent to BEIL-CMEE for further treatment and disposal.
● Scrubbing water will go along with the product which will be sold to authorized end users registered under rule-9.
-
Clearly mention about final disposal
D-5 Treatment facilities
For Domestic wastewater:
Capacity of STP: Not Applicable [0.5 KLD will be sent to the primary ETP.]
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary,
Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation
at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream
segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
For Proposed, Industrial waste water will be collected and treated into the primary ETP treatment
plant and treated effluent will be send to BEIL-CMEE for further treatment and disposal.
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Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water
(Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
➢ Not Applicable [CMEE-BEIL,Ankleshwar]
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
➢ Applicable
➢ For Proposed new project, Industrial waste water will be collected and treated into the
primary ETP treatment plant and treated effluent will be sent to BEIL-CMEE for further
treatment and disposal.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF
etc. Name of Common facility (CF) (For wastewater treatment)
➢ CMEE-BEIL,Ankleshwar
Membership of Common facility (CF) mentioning total capacity, consented quantity,
occupied capacity and spare capacity and norms of acceptance of effluent from member
units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706
dated 08/01/2020.
➢ We are attached here as Annexure.[Ref.BEIL/ANK/2020].
D-7 Simplified water balance diagram with reuse / recycle of waste water
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E Air
E-1 Brief Note on fuel based heat energy requirement and worst case scenario thereof:
Considering the Calorific Value of the fuel and other parameters, requirement of the heat,
we will use consumption of fuel in MT/Day
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism
published in the MOEFCC‘s OM vide dated 31.10.2019)
-Sr.
no.
Source of
emission
With
Capacity
Stack
Height
(meter)
Type of
Fuel
Quantity
of Fuel
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air Pollution
Control
Measures
(APCM)
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1 Boiler
[1 TPH]
20 m Natural
Gas
1900
Nm3/Day
PM
SO2
NOx
Adequate
Stack
Height
2
Thermic
Fluid
Heater
[Cap. 2
Lac
K.cal/Hr]
20 m Natural
Gas
800
Nm3/Day
PM
SO2
NOx
Adequate
Stack
Height
3 D.G. Set
[250 KVA]
12 m Diesel 500
litre/day
PM
SO2
NOx
Adequate
Stack
Height
-
E-3 Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr.
no.
Specific Source of
emission
(Name of the Product &
Process)
Type of
emission
Stack/Vent
Height
(meter)
Air Pollution
Control
Measures
(APCM)
1 Reaction Vessel
[Product Sr. No.-1,4]
HCl 15 Two Stage
Water Scrubber
Note:
⮚ Details of gaseous raw materials used in proposed project
⮚ Estimation of process gas emission (Product wise and Total)
⮚ Requirement of the scrubbing media (KL per Day) considering solubility (Product
wise and Total)
⮚ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and
its sound management in HW matrix.
Details of scrubbing media are attached as Annexure-I.
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iii Fugitive emission details with its mitigation measures:
As below:
➢ Minimum Joints & flanges
➢ Pumps with mechanical seals
➢ Proper ventilation
➢ Adequate PPEs
F Hazardous wastes
(as per the Hazardous and Other Wastes (Management and Transboundary Movement)
Rules 2016.
Note:
⮚ Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle
within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
⮚ Quantification of hazardous waste shall be based on mass balance and calculations
shall be incorporated in EMP details separately.
⮚ Disposal to scrap vendors/vendors/traders is not allowed
Note:- Details are attached as Annexure-I.
F-1 Hazardous waste management matrix
Sr.
no.
Type/Name of
Hazardous
waste
Specific
Source of
generation
(Name of
the Activity,
Product etc.)
Category
and
Schedule as
per HW
Rules.
Quantity
(MT/Annum
)
Management of HW
1. Empty barrels/
containers/line
rs
contaminated
with
hazardous
chemicals
Raw Material
and
Packaging
33.1 40 Collection, Storage,
Transportation, reuse or
send back to supplier or
sold to Authorized
Vendors.
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/wastes
2. Used Oil From
Machinery
5.1 1 Collection,
Storage,Transportation
and sold to authorized
Recyclers.
3. ETP Sludge ETP 35.3 45 Collection, Storage,
Transportation and sent
to TSDF site- BEIL
Ankleshwar.
4. Distillation
Residue
From
solvent
Distillation
20.3 29 Collection, Storage,
Transportation, Co-
Processing or sent to
CHWIF.
5. Spent Carbon From
Process
Sr.
No.5,9,10
28.3 25 Collection, Storage,
Transportation and
send to Co-Processing
or CHWIF.
6. Spent Catalyst From
Process
Sr. No.2,3,5
28.2 10 Collection, Storage,
Recycle / Regeneration
/ Reuse and/or sent to
CHIWF.
7. Hyflo From
Process Sr.
No.5
35.3 6 Collection, Storage,
Transportation,
CoProcessing or
disposal at CHWIF.
8. Salt
[Lithium Salt
of Methane
Sulphonic
Acid]
From
Process
Sr. No.5
35.3 53 Collection, Storage,
Transportation and sent
to TSDF site
9. HCl Solution
[Hydrochloric
Acid Solution
Scrubber
Sr.
No.1,4,5,10
--- 115 Collection, Storage,
Transportation and sell
to authorized end users
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28%-30%] registered under rule-9.
10. Spent Solvent From
Solvent
Distillation
28.6 687 Collection, Storage,
Recovery and recycle in
process or send
regenerator end user or
sell to authorized end
users registered under
rule-9.
11. Off-
Specification
Products
From
Process
28.4 2 Collection, Storage,
Transportation,
CoProcessing or
disposal at CHWIF.
-
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility.
➢ Membership Certificate No.BEIL/ANK/2020, Dated 03 October 2020.
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Not Applicable
Not Applicable
Sr. no. Type/Name of Other
wastes
Specific Source
of generation
(Name of the
Activity, Product
etc.)
Quantity
(MT/Annum)
Management of
Wastes
1 -------------------------
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered
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Solvents etc.
Sr. No. Product
Name Solvent Name
Solvent
Consumption
[MT/Month]
Solvent
Recover Qty
[MT/Month]
% Rec.
1 BMSP Tetrahydrofuran
(THF) 4.8 4.6 95
Methanol 8.0 7.6 95
Isopropyl Alcohol 4.0 3.8 95
2 BMV MDC 20.0 19.2 96
Acetone 16.0 15.2 95
Methanol 12.0 11.4 95
3 BMD MDC 12.0 11.6 97
Acetone 16.0 15.2 95
Methanol 8.0 7.6 95
4 DMSP TetraHydrofuran
[THF] 4.0 3.8 96
Methanol 4.0 3.8 96
IPA 10.0 9.6 96
5 CP MDC 8.0 7.8 98
Acetone 12.0 11.5 96
Methanol 5.2 5.0 96
6 PS Pyrrolidine 4.8 4.6 96
Methanol 8.0 7.6 95
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Toluene 12.0 11.5 96
7 PSA Acetic Acid 8.0 7.6 95
Vinyl Alcohol 5.2 5.0 96
Chloroform 7.2 6.8 95
8 MP Acetic Acid 20.0 19.0 95
MDC 10.0 9.6 96
9 PDH Methanol 8.0 7.7 96
10 ND Acetone 30.0 28.4 95
n-Pentane 10.0 9.6 96
Pyridine 20.0 19.0 95
A highly efficient and full fledge solvent recovery system is installed to recover maximum possible
solvent and will be reused back in process. Detailed process is as described below:
For the efficient solvent recovery system, chilled water circulation jacketed, chilled water traps will be
installed on the vent for arresting any escape of vapors from the reaction and distillation unit. The
reactors will be connected to water condenser system. The receiver will also be jacketed with
circulation of water. The recovered solvents will then be stored and reused. Proper planning and
maintenance will enable to have an efficient solvent recovery from the system.
The recovery efficiency of every solvent used is approximately 95% - 98%.
● The solvent distillation system shall be designed so as to achieve minimum 95.0 % recovery of solvent.
● Two condensers will install with cooling water and chilled brine to recover the solvent. ● Primary Condenser HE-01: Cooling Tower water or Chilled water (at 10 0C) will be used to
condense the solvents depend on the vapor pressure at its operating conditions and the non-condensed vapours will be condensed in a Secondary Condenser.
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● VOC Trap Condenser HE-02: Chilled Brine at -5 0C will be used to trap any traces of Solvent which is slipped from Secondary condenser
G-2 Brief Note on LDAR proposed:
Leak Detection and Repair (LDAR) for Solvent:
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To prevent losses of these solvents in atmosphere, following infrastructure shall be used in addition
to LDAR program
● Leak Free Pumps & Valve for transfer of solvents
● MSW Gaskets in solvent pipelines to prevent leakage from flanges
● Minimum number of flanges, joints and valves in pipelines.
● To eliminate chances of leakages from glands of pumps, double mechanical seal will be
provided at all solvent pumps.
● All the rotating equipment like pumps will be installed with double Mechanical Seals to arrest
any sort of emissions.
● Condenser post Reactor with cooling arrangement and chilling Arrangement. Flanges will be
sealed so less losses will be there.
● Down the Temperature of Chilling tower to -15°C.
● Closed loop system.
G-3 VOC emission sources and its mitigation measures
● Minimum joints/flanges ● Adequate Condenser ● Brine will be utilised as chilling agent ● Pumps with double mechanical seals ● Proper Ventilation ● PPEs
H SAFETY details
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H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent
acid and spent solvent tanks)
Sr. no Name of
Chemical
Capacity of
Tank
Number of
Tanks
Hazardous Characteristics of
Chemical
1 ------- ------- ------- -------
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags
etc.
➢ Hazardous chemicals bags/drums are stored and handled in Dispensing room for taking out
samples from the container for quality check up purposes or for the partial use. This activity
for Hazardous material handling is carried out by using all PPE with proper ventilation &
under supervision.
➢ Drum handling trolleys is used for transportation of drums up to plant
➢ Materials are transferred by pumping through pipelines or by vacuum from drums.
Safety details of Hazardous Chemicals:
Type of Hazardous
Chemicals
Safety measures
Toluene It is important to keep toluene away from sources of heat or
ignition. This chemical should be stored in a tightly closed
container in a dry, well-ventilated, and secure place, preferably
one designed for the storage of flammable liquids. Toluene should
be kept away from incompatible materials, like oxidizing agents.
Methanol Methanol is a colourless liquid that boils at 64.96 °C (148.93 °F)
and solidifies at −93.9 °C (−137 °F). It forms explosive mixtures
with air and burns with a nonluminous flame. It is completely
miscible in water.
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Do not handle or open near flame, sources of heat, or sources of
ignition. Wear personal protective equipment. Use only in well-
ventilated areas. Provide sufficient air exchange and/or exhaust in
work rooms. Avoid contact with skin, eyes and clothing. Do not
breathe vapors or spray mist. Do not ingest. When using, do not
smoke. To avoid ignition of vapors by static electricity discharge,
all metal parts of the equipment must be grounded. Keep away
from incompatible materials. Handle in accordance with good
industrial hygiene and safety practice. Wash thoroughly after
handling. Containers of this material may be hazardous when
empty since they retain product residues (vapors, liquids).
HCl Wear a chemical-resistant apron, chemical-resistant gloves and
chemical splash goggles at all times when handling HCl to protect
your eyes and skin. Concentrated Hydrochloric acid is toxic if
inhaled, so avoid breathing it in and always handle it while under a
fume hood.
⮚ Applicability of PESO :Not Applicable
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process,
Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of Process Safety measures including Automation
----- ------
● There is no hydrogenation process, Nitration process, Chlorination process, Exothermic
Reaction etc. during our production.
H-3 Details of Fire Load Calculation
Total Plot Area: 1888 Sq. m.
Area utilized for plant activity: 160 Sq. m.(per Floor, total Floors :G+2)
Area utilized for Hazardous Chemicals 90 Sq. m.
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Storage: Number of Floors:
Water requirement for firefighting in
KLD :
5 KLD
Water storage tank provided for
firefighting in KLD:
150 KLD
Details of Hydrant Pumps: 3 Nos.
[1]Main Fire Pump
[2]Diesel Driven Pump
[3]Jockey Pump
Frequency 50/60Hz
Voltage 380 VAC
Phase 3 Phase
Medium
Temperature
-15 deg C to 120 deg C
Max. Working
Pressure
2.5 Mpa
Ambient
Temperature
Less than 40 deg C
Nearest Fire Station : DPMC Fire Station Ankleshwar
Plot No. G/S-3, Near Jayaben Modi Hospital,
GIDC, Ankleshwar, Gujarat 393002
Applicability of Off Site Emergency
Plan:
Not Applicable
-
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H-4 Details of Fire NOC/Certificate:
We will obtain it soon.
H-5 Details of Occupational Health Centre (OHC):
Number of permanent Employee : 10
Number of Contractual
person/Labour :
10
Area provided for OHC: 28.62 Sq. m.
Number of First Aid Boxes : 10 Nos.
Nearest General Hospital : Jayaben Modi Hospital
624/1, Valia Road, Ankleshwar
GIDC, Gujarat 393002
Name of Antidotes to be store in
plant :
Paracetamol
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. Vasundhara Enterprise remains present during
video conference meeting.
Committee noted that the proposal is for Greenfield project in GIDC Ankleshwar. PP submitted details
regarding area adequacy. Source of water is GIDC. Product profile along with end use discussed in
depth. Looking to layout plan, Committee insisted for submit revised layout plan with mentioning
adequate raw material and solvent storage area and its area adequacy with land breakup which is later
on submitted by PP.
Committee noted that PP has submitted waste water management and total industrial effluent will be
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treated in ETP and treated effluent will be sent to CMEE of M/s. BEIL for evaporation. Domestic sewage
will be treated in ETP. Committee discussed regarding stage wise reduction of BOD, COD and TDS in
ETP.
PP submitted that they have proposed boiler and DG set. Fuel used will be Natural gas for boiler and
thermo pack. Two stage scrubbers will be provided as APCM with process reactor stack. Committee
insisted for revised fuel consumption of natural gas as per capacity of boiler for which PP is agreed upon
and later on submitted revised fuel consumption details. PP submitted Hazardous Waste Matrix as per
Hazardous Waste Rules – 2016.
Upon asking regarding provision of fire hydrant network and proposed fire extinguishers details, PP has
addressed the Site Plan/layout plan with provision of fire hydrant network, periphery road with entry and
exit separately, proposed fire extinguishers details, adequate fire water reservoir and fire load
calculation. Committee noted that PP has addressed fire evacuation plan, worker‘s safety and
occupational Health centre (OHC) and process hazard and its safety control measures. Committee
insisted for 150 KL fire water tank and fire trolley pump which details submitted later on by PP.
Committee deliberated on storage and safety aspects of hazardous chemicals, green belt area, EMP,
CER, LDAR and solvent recovery etc. Looking to green belt area mentioned only 36%, Committee
insisted for submit proposal of green belt area as per CEPI mechanism and PP later on submitted
revised green belt area of 40%.
Committee found submission of project proponent satisfactory.
After detailed discussion, Committee unanimously decided to recommend the project to SEIAA,
Gujarat for grant of Environment Clearance
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon‘ble Supreme Court of
India in Civil Appeal no. 8478/2020 regarding operation of the Hon‘ble NGT orders dated 10/07/2019
& 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change in product mix,
after the 30th March 2021, considered as per the provisions in force at that time as mentioned in the
Notification vide S.O. 1223 (E) dated 27/03/2020 and S.O. 3636 (E) dated 15/10/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients (API) as
per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any subsequent
amendments.
4. PP shall submit six monthly compliance report of Environmental Clearance without fail and the same
shall be critically assessed by the regulatory authority.
5. Wastewater shall be sent to CMEE only after providing adequate treatment in such a way that no
pollutant get air borne during evaporation to avoid adverse impact on Human Health & Environment.
6. The PP shall develop green belt within premises (755 Sq. m i.e. 40 % of the total plot area) as per
the undertaking submitted before SEAC. Green belt shall be developed with native plant species that
are significant and used for the pollution abatement as per the CPCB guidelines. It shall be
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implemented within 3 years of operation phase in consultation with GPCB.
7. Domestic wastewater generation shall not exceed 0.3 KL/day for proposed project and it shall be
treated in ETP. It shall not be disposed off in soak pit and septic tank.
8. Close loop solvent recovery system with adequate condenser system shall be provided to recover
solvent vapours in such a manner that recovery shall be maximum and recovered solvent shall be
reused in the process within premises.
9. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB
guidelines. LDAR Logbooks shall be maintained.
10. The unit shall submit the list of authorized end users of hazardous wastes along with MoU signed
with them at least two months in advance prior to the commencement of production. In the absence
of potential buyers of these items, the unit shall restrict the production of the respective items.
11. Unit shall obtain all required permissions from the Narcotics Control Bureau for manufacturing,
storage and handling of Acetic Anhydride & any such chemicals.
12. Safety and Health:
a) PP shall obtain PESO permission for the storage and handling of hazardous chemicals. (If
applicable)
b) PP shall provide Occupational Health Centre (OHC) as per the provisions under the Gujarat
Factories Rule 68-U.
c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the concern
authority as per the prevailing Rules / Gujarat Fire Prevention and Life Safety Measures Act,
2016.
d) Unit shall adopt functional operations/process automation system including emergency
response to eliminate risk associated with the hazardous processes.
e) PP shall carry out mock drill within the premises as per the prevailing guidelines of safety and
display proper evacuation plan in the manufacturing area in case of any emergency or
accident.
f) PP shall install adequate fire hydrant system within premises and separate storage of fire
water and foam for the same shall be ensured by PP. Also PP shall provide alarm system in
nearby fire station for emergency of any fire in plant area.
g) PP shall take all the necessary steps for control of storage hazards within premises ensuring
incompatibility of storage raw material and ensure the storage keeping safe distance as per
the prevailing guidelines of the concerned authority.
h) PP shall take all the necessary steps for human safety within premises to ensure that no any
harm is caused to any worker/employee or labor within premises.
i) Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.
j) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.
k) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam
pouring system etc. to restrict cascade fire emergency in solvent tank farm.
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2. SIA/GJ/IND2/173392/2020 M/s. Anil Synthetics
Plot No. 285/3, GIDC Estate - Ankleshwar,
Dist.: Bharuch
Appraisal
Category of the unit: 5(f)
Project status: New
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173392/2020 on dated
05.10.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
This is a new unit and proposes for manufacturing of synthetic organic chemicals [API and API
Intermediates] as tabulated below,
Sr. No.
Name of the Products
API OR INTERMEDIATE
CAS no. Quantity MT/Month
*End-use of products
1. 1-4-Chloro Benzhydryl Piperazine
Intermediate
303-26-4
30 TPM [Sr No. 1
to 30]
An antihistamine used to relieve allergy symptoms such as watery eyes, runny nose, itching eyes/nose, sneezing, hives, and itching. It works by blocking a certain natural substance that your body makes during an allergic reaction.
2. 1-[2,3 Di Chloro Phenyl] Piperazine Hydrochloride
Intermediate
119532-26-2
An antipsychotic- used in the treatment of schizophrenia and bipolar disorder and other uses include as an add-on treatment in major depressive disorder
3. Dibenzo[b,f][1,4]Thiazepin-11[10H]-One
Intermediate
3159-07-7
30 TPM [Sr No. 1
to 30]
Anti-psychotic -used to treat certain mental/mood conditions.
4. 4 Methyl Acetophenone
Intermediate
122-00-9 Anti-inflammatory-t is used to treat the pain and inflammation in osteoarthritis.
5. Bis (2-Chloroethyl) Amine Hydrochloride
Intermediate
821-48-7 An antifungal- used to treat certain infections caused by fungus
6. 8-Chloro-11-(4-methyl-1-piperazinyl)-5H-dibenzo [b,e][1,4] diazepine
Intermediate
5786-21-0
An antipsychotic medicine. It works by changing the actions of chemicals in the brain.Reduce the risk of suicidal behavior in people
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with schizophrenia or similar disorders.
7. 2-[2-3(S)-3-[2-(7-chloro-2-quinolinyl) -ethyl]phenyl]-3-hydroxypropyl] phenyl-2-propanol
Intermediate
142569-70-8
Used in the treatment of asthma
8. 3,4-dimethoxybenzoyl chloride
Intermediate
3535-37-3
It is used for the treatment of Gastro esophageal Reflux Disease, Functional Dyspepsia, and other associated motility disorders.
9. 5-amino-2,4,6-triiodobenzene-1,3-dicarbonyl chloride
Intermediate
35453-19-1
It contrast agents are used to allow blood vessels, organs, and other non-bony tissues to be seen more clearly on a CT scan or other radiologic (x-ray) examination. it is used to help diagnose certain disorders of the heart, brain, blood vessels, and nervous system.
10. Methyl-5-bromo-2-hydroxy-3-propanoylbenzoate
Intermediate
91983-31-2
It is used to treat certain bladder/urinary tract symptoms. It is a smooth-muscle relaxant. It helps to reduce leaking of urine, feelings of needing to urinate right away, frequent trips to the bathroom, and bladder pain.
11. 5-Amino-2,4,6-triiodoisophthalic acid
Intermediate
37441-29-5
30 TPM [Sr No. 1
to 30]
It contrast agents are used to allow blood vessels, organs, and other non-bony tissues to be seen more clearly on a CT scan or other radiologic (x-ray) examination. it is used to help diagnose certain disorders of the heart, brain, blood vessels, and nervous system.
12. 1-Acetyl-4-(4-hydroxyphenyl) Piperazine
Intermediate
67914-60-7
It is used to treat skin infections such as athlete's foot, jock itch, ringworm, This medication is also used to treat a skin condition known as pityriasis, a fungal infection that causes a lightening or darkening of the skin of the neck, chest,
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arms, or legs.
13. 3-(3-chloropropyl)-7,8-dimethoxy-1,3-dihydro-2H-3-benzazepin-2-one
Intermediate
85175-59-3
It is used to treat heart failure.
14. 2-Butyl-4-Chloro-1H-imidazole-5-carbaldehyde
Intermediate
83857-96-9
It is used to treat high blood pressure (hypertension) and to help protect the kidneys from damage due to diabetes. It is also used to lower the risk of strokes in patients with high blood pressure and an enlarged heart.
15. 4-(4-aminophenyl) morpholin-3-one
Intermediate
438056-69-0
It is used to prevent or treat a type of blood clot called deep vein thrombosis (DVT), which can lead to blood clots in the lungs.
16. 6-Hydroxy-3,4-dihydroquinolin-2(1H)-one
Intermediate
54197-66-9
30 TPM [Sr No. 1
to 30]
It is used to improve the symptoms of a certain blood flow problem in the legs (intermittent claudication). cilostazol can decrease the muscle pain/cramps that occur during exercise/walking.
17. 1-(3-Chlorophenyl)-4-(3-Chloropropyl) Piperazine Hydrochloride
Intermediate
52605-52-4
It is used an antidepressant that increases serotonin activity in the brain. Trazodone is used for depression, anxiety, sleep and pain.
18. 1-(4-Fluorophenyl) Piperazine
Intermediate
2252-63-3
It is used to treat life-threatening low blood pressure that can occur with certain medical conditions or surgical procedures. Norepinephrine is often used during CPR (cardio-pulmonary resuscitation)
19. 2,6-Dimethylphenyl chloroacetamide
Intermediate
1131-01-7
Used to prevent and relieve pain -used to reduce pain or discomfort caused by skin irritations such as sunburn, insect bites, poison ivy, poison oak, poison sumac, and minor cuts, scratches, or burns
20. 4,4'[2-Pyridinylmethylene] Bisphenol
Intermediate
603-41-8 Used as a treatment for constipation or to prepare the large bowel before colonoscopy or surgery.
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21. Trans 4-Amino Cyclohexanol
Intermediate
27489-62-9
used in the treatment of respiratory diseases associated with viscid or excessive mucus
22. 3-[Aminomethyl]-5-Methyl Hexanoic Acid
Intermediate
128013-69-4
Used to treat epilepsy, neuropathic pain, fibromyalgia, restless leg syndrome, and generalized anxiety disorder.
23. 6 chloro-4- hydroxy- 2- methyl- 2H thieno [2,3-e] [1,2] thiazine- 3- carboxylate- 1,1- dioxide
Intermediate
70415-50-8
30 TPM [Sr No. 1
to 30]
Used for the treatment of various types of pain, especially resulting from inflammatory diseases of the joints, osteoarthritis, surgery, sciatica, and other inflammations.
24. 2-Amino 5-Methyl Thiazole
Intermediate
7305-71-7
Anti-inflammatory-used to treat pain and inflammation in rheumatic diseases and osteoarthritis.
25. 1-(3-Chlorophenyl) Piperazine
Intermediate
6640-24-0
It is an antidepressant that increases serotonin activity in the brain. It is used for depression, anxiety, sleep and pain.
26. 2-[2-(piperazin-1-yl)ethoxy]ethanol
Intermediate
13349-82-1
It is used to treat certain mental/mood conditions (such as schizophrenia, bipolar disorder, sudden episodes of mania or depression associated with bipolar disorder). Quetiapine is known as an anti-psychotic drug.
27. 4,4,4-trifluo-1-(4-methylphenyl) butane-1,3-dione
Intermediate
720-94-5 It works by reducing hormones that cause inflammation and pain in the body. it is used to treat pain or inflammation caused by many conditions such as arthritis, ankylosing spondylitis, and menstrual pain
28. 1-(4-methoxyphenyl)piperazine hydrochloride
Intermediate
38869-47-5
It is used in adults to treat infections caused by fungus. This includes infections in any part of the body including the lungs, mouth or throat, toenails, or fingernails. Some brands of itraconazole are not for use
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in treating fungal infections of the fingernails or toenails.
29. 3-(dimethylamino)-1(thiophen-2yl)propan-1-ol
Intermediate
132335-49-0
30 TPM [Sr No. 1
to 30]
Duloxetine is used to treat depression and anxiety. In addition, duloxetine is used to help relieve nerve pain (peripheral neuropathy) in people with diabetes or ongoing pain due to medical conditions such as arthritis, chronic back pain, or fibromyalgia (a condition that causes widespread pain).
30. 1-[2,4-d-Difluorophenyl]-2,3-epoxypropyl-1H-1,2,4-triazole methanesulfonate
Intermediate
86386-77-8
An antifungal medication used for a number of fungal infections.
Total 30 MT/Month
# Brief Note of Product Profile:
1. No of Manufacturing Plants: 1no’s
2. Brief Note regarding number of Products to be manufactured considering plant capacity:
Unit will manufacture any 2 products from above mention product [i.e. 1 to 30] as per
quantity mentioned hence at a time unit will manufacture 2 Products and total
production capacity will not exceed 30.0 MT/ Month.
ENDUSE OF PRODUCTS
Sr. No.
Name of the Product
CAS No. (Product)
Type/ Category of Product (API/ Intermediate)
In case of Intermediate stage of API Said API is used for/End Use of said API
Stage i.e. n-1, n-2, etc.
Name of API in which Intermediate Used/ End use of said Intermediate
CAS no. (API)
1. 1-4-Chloro Benzhydryl Piperazine
303-26-4 Intermediate
(n-1) Cetirizine 83881-51-0
An antihistamine used to relieve allergy symptoms such as watery eyes, runny nose, itching eyes/nose, sneezing, hives, and itching. It
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works by blocking a certain natural substance (histamine)
2. 1-[2,3 Di Chloro Phenyl] Piperazine Hydrochloride
119532-26-2
Intermediate
(n-1) Aripiprazole
HCl
129722-12-9
An antipsychotic- used in the treatment of schizophrenia and bipolar disorder and other uses include as an add-on treatment in major depressive disorder
3. Dibenzo[b,f][1,4]Thiazepin-11[10H]-One
3159-07-7
Intermediate
(n-1) Quetiapine Fumarate
111974-69-7
Anti-psychotic -used to treat certain mental/mood conditions.
4. 4 Methyl Acetophenone
122-00-9 Intermediate
(n-1) celecoxib 169590-42-5
Anti-inflammatory-t is used to treat the pain and inflammation in osteoarthritis.
5. Bis (2-Chloroethyl) Amine Hydrochloride
821-48-7 Intermediate
(n-1) Cyclophosphamide
50-18-0 an antifungal- used to treat certain infections caused by fungus
6. 8-Chloro-11-(4-methyl-1-piperazinyl)-5H-dibenzo[b,e][1,4] diazepine
5786-21-0
Intermediate
(n-1) clozapine 5786-21-0
An antipsychotic medicine. It works by changing the actions of chemicals in the brain. Used to treat schizophrenia after other treatments have failed. Reduce the risk of suicidal behavior in people with schizophrenia or similar disorders.
7. 2-[2-3(S)-3-[2-(7-chloro-2-quinolinyl) -ethyl] phenyl]-3-hydroxypropyl] phenyl-2-propanol
142569-70-8
Intermediate
(n-1) Montelukast
158966-92-8
Used in the treatment of asthma
8. 3,4-dimethoxybenzoyl chloride
3535-37-3
Intermediate
(n-1) Itopride 122898-67-3
It is used for the treatment of Gastroesophageal Reflux Disease, Functional
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Dyspepsia, and other associated motility disorders.
9. 5-amino-2,4,6-triiodobenzene-1,3-dicarbonyl chloride
35453-19-1
Intermediate
(n-1) Lopamidol
60166-93-0
It contrast agents are used to allow blood vessels, organs, and other non-bony tissues to be seen more clearly on a CT scan or other radiologic (x-ray) examination. it is used to help diagnose certain disorders of the heart, brain, blood vessels, and nervous system.
10. Methyl-5-bromo-2-hydroxy-3-propanoylbenzoate
91983-31-2
Intermediate
(n-1) Flovaxate 15301-69-6
It is used to treat certain bladder/urinary tract symptoms. it is a smooth-muscle relaxant. it helps to reduce leaking of urine, feelings of needing to urinate right away, frequent trips to the bathroom, and bladder pain.
11 5-Amino-2,4,6-triiodoisophthalic acid
37441-29-5
Intermediate
(n-1) Lopamidol 60166-93-0
It contrast agents are used to allow blood vessels, organs, and other non-bony tissues to be seen more clearly on a CT scan or other radiologic (x-ray) examination. it is used to help diagnose certain disorders of the heart, brain, blood vessels, and nervous system.
12. 1-Acetyl-4-(4-hydroxyphenyl)Piperazine
67914-60-7
Intermediate
(n-1) Ketoconazole
65277-42-1
It is used to treat skin infections such as athlete's foot, jock itch, ringworm, fungal infection that
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causes a lightening or darkening of the skin of the neck, chest, arms, or legs.
13. 3-(3-chloropropyl)-7,8-dimethoxy-1,3-dihydro-2H-3-benzazepin-2-one
85175-59-3
Intermediate
(n-1) Ivabradine 155974-00-8
It is used to treat heart failure.
14. 2-Butyl-4-Chloro-1H-imidazole-5-carbaldehyde
83857-96-9
Intermediate
(n-1) Losartan 114798-26-4
It is used to treat high blood pressure (hypertension) and to help protect the kidneys from damage due to diabetes. It is also used to lower the risk of strokes in patients with high blood pressure and an enlarged heart. Lowering high blood pressure and kidney problems.
15. 4-(4-aminophenyl)morpholin-3-one
438056-69-0
Intermediate
(n-1) Rivaroxaban
366789-02-8
It is used to prevent or treat a type of blood clot called deep vein thrombosis (DVT), which can lead to blood clots in the lungs (pulmonary embolism
16. 6-Hydroxy-3,4-dihydroquinolin-2(1H)-one
54197-66-9
Intermediate
(n-1) Cilostazol 73963-72-1
It is used to improve the symptoms of a certain blood flow problem in the legs (intermittent claudication). Cilostazol can decrease the muscle pain/cramps that occur during exercise/walking.
17. 1-(3-Chlorophenyl)-4-(3-Chloropropyl) Piperazine Hydrochloride
52605-52-4
Intermediate
(n-1) Trazodone 19794-93-5
It is used an antidepressant that increases serotonin activity in the brain. It is usedforDepression,
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anxiety, sleep and pain.
18. 1-(4-Fluorophenyl) Piperazine
2252-63-3
Intermediate
(n-1) Monatepil 103379-03-9
It is used to treat life-threatening low blood pressure (hypotension) that can occur with certain medical conditions or surgical procedures. Norepinephrine is often used during.
19. 2,6-Dimethylphenyl chloroacetamide
1131-01-7
Intermediate
(n-1) Lidocaine 137-58-6 used to prevent and relieve pain - used to reduce pain or discomfort caused by skin irritations such as sunburn, insect bites, poison ivy, poison oak, poison sumac, and minor cuts, scratches, or burns
20. 4,4'[2-Pyridinylmethylene] Bisphenol
603-41-8 Intermediate
(n-1) Sodium Picosulfate
10040-45-6
used as a treatment for constipation or to prepare the large bowel before colonoscopy or surgery
21. Trans 4-Amino Cyclohexanol
27489-62-9
Intermediate
(n-1) Ambroxol 23828-92-4
used in the treatment of respiratory diseases associated with viscid or excessive mucus
22. 3-[Aminomethyl]-5-Methyl Hexanoic Acid
128013-69-4
Intermediate
(n-1) Pregabalin 148553-50-8
Used to treat epilepsy, neuropathic pain, fibromyalgia, restless leg syndrome, and generalized anxiety disorder.
23 6 chloro-4- hydroxy- 2- methyl- 2H thieno [2,3-e] [1,2] thiazine- 3-
70415-50-8
Intermediate
(n-1) Lornoxicam 70374-39-9
Used for the treatment of various types of pain, especially resulting from
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carboxylate- 1,1- dioxide
inflammatory diseases of the joints, osteoarthritis, surgery, sciatica, and other inflammations.
24. 2-Amino 5-Methyl Thiazole
7305-71-7
Intermediate
(n-1) Meloxicam 71125-38-7
Anti-inflammatory- used to treat pain and inflammation in rheumatic diseases and osteoarthritis.
25 1-(3-Chlorophenyl) Piperazine
6640-24-0
Intermediate
(n-1) Trazodone 19794-93-5
It is an antidepressant that increases serotonin activity in the brain. it is used for depression, anxiety, sleep and pain.
26. 2-[2-(piperazin-1-yl)ethoxy]ethanol
13349-82-1
Intermediate
(n-1) Quetiapine 111974-69-7
It is used to treat certain mental/mood conditions (such as schizophrenia, bipolar disorder, sudden episodes of mania or depression associated with Bipolar disorder).
27. 4,4,4-trifluo-1-(4-methylphenyl) butane-1,3-dione
720-94-5 Intermediate
(n-1) Celecoxib 169590-42-5
It works by reducing hormones that cause inflammation and pain in the body. it is used to treat pain or inflammation caused by many conditions such as arthritis, ankylosing spondylitis, and menstrual pain
28. 1-(4-methoxyphenyl)piperazine hydrochloride
38869-47-5
Intermediate
(n-1) Itraconazole
84625-61-6
It is used in adults to treat infections caused by fungus. This includes infections in any part of the body including the lungs, mouth or throat, toenails, or
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fingernails. Some brands of itraconazole are not for use in treating fungal infections of the fingernails or toenails.
29. 3-(dimethylamino)-1(thiophen-2yl)propan-1-ol
132335-49-0
Intermediates
(n-1) Duloxetine 1165 39-59-4
Duloxetine is used to treat depression and anxiety. In addition, duloxetine is used to help relieve nerve pain (peripheral neuropathy) in people with diabetes or ongoing pain due to medical conditions such as arthritis,
30. 1-[2,4-d-Difluorophenyl]-2,3-epoxypropyl-1H-1,2,4-triazole methanesulfonate
86386-77-8
Intermediate
(n-1) Fluconazole
86386-73-4
An antifungal medication used for a number of fungal infections.
The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr. no. Particulars Details
A-1 Total cost of Proposed Project
(Rs. In Crores):
Total Project
5.0 Crores
Break-up of proposed project Cost:
Details Project Cost
(Rs. In Crores)
Land 0.7
Building 1.0
Machinery 1.5
EMP 1.8
A-2 Details of Environmental Management Plan (EMP) As below:
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Sr. No
Unit Detail Capital Cost (Rs. In Crores)
Operating Cost (Rs. In Crores)
Maintenance Cost (Rs. In Crores)
Total Recurring Cost (Rs. In Crores)
1 Waste Water 20 KLD 0.4 0.088473 0.0528 0.1413
2 Air -- 0.25 --- 0.0046 0.0046
3 Hazardous Management
-- 0.24 0.012068 0.005 0.0171
4. Risk and Safety Audit and Safety Equipment (PPE, Safety Shower, Ventilation, etc.)
-- 0.45 0.00867 -- 0.0125
5. Cost of Fire Extinguisher, Fire hydrant line
-- 0.2 -- 0.0050 0.0083
5 Green Belt Development
-- 0.01 --- 0.0007 0.0007
6. AWH Monitoring
-- 0.2 0.004 0.00225 0.0063
7. Occupational Health
-- 0.05 --- 0.0042 0.0042
Total 1.8 0.1949
Summary
Cost of Project in Crores 5.0
EMP Capital Cost in Crores per Annum and
Percentage:
1.8 (36%)
EMP Recurring Cost in Crores per Annum
and Percentage:
2.34 (46.7%)
A-3 Details of CER as per OM dated 01/05/2018
As per OM no. 22-65/2017 on dated 01/05/2018 regarding ―Corporate Environment Responsibility‖ (CER), Greenfield projects have to contribute 2% of the Additional Capital Investment, the unit has planned to spend 4.0 % of the total cost of the proposed project (Rs.500 Lakhs) over a period of five years towards CER activity. So, as per the project cost Rs. 20 Lakhs used in the CER activities.
% as per the OM
Rs. in Crores
4% 0.2
Brief note on proposed activities:
BUDGETARY ALLOCATION FOR CER ACTIVITIES
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The unit has planned to spend 4.0 % of the total cost of the proposed project (Rs.500 Lakhs) over a period of five years towards CER activity. So, as per the project cost Rs. 20 Lakhs used in the CER activities. Budgetary allocation is given in below table.
Sr. No.
Activity
CER Activities Budget for 2
Years
1 Drinking Water Supply– Common Drinking Water Facility in Temple – Village
Bhadkodra
7.0
2 Electrification Including Solar Power– Motali Installation of Solar Street Light near Gam Panchayat Area
8.0
3 Development of Garden: We will develop a garden with facilities for young
children‘s and seating arrangement. (i.e., Sanjali)
5.0
TOTAL Rs. 20 Lakh
B Land / Plot ownership details:
Details of Land/plot ownership are attached as Annexure-I.
B-1 Plot area
Total Plot area
1048.10 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Sr.No.
Area Ground Floor
First Floor
Second Floor
Sq. M.
%
1 Intermediate Production Area
100 100 100 300 10
2 R.M.Storage 40 40 40 120 4
3 F.G. Storage 15 0 0 15 1
4 Utility Area 30 0 0 30 3
5 ETP Area 50 0 0 50 5
6 Solid waste storage area 5 0 0 5 0
7 Haz waste storage area 10 0 0 10 1
8 Fresh Solvent Storage Area 10 0 0 10 1
9 Recovered Solvent Storage Area
25 0 0 25 2
10 Tank Farm storage area 30 0 0 30 3
11 Green Belt Area 262 0 0 262 25
12 Office Area/OH Centre 30 30 30 90 3
13 Open Area 441.075 0 0 441 42
TOTAL 1048.1 100
So, Adequate Area is available for Storage. As per above table we have
provided sufficient Finish product storage area. For raw material storage area,
we have provided separate storage area for chemicals to prevent Accident and
this area is sufficient to handle Safe products.
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B-3 Green belt area
Total (Sq. meter)
In side Plant Premises Outside Plant Premises (AIA)
Area in Sq. meter 419 320
% of total area 25% 30%
C Employment generation
Total
15
D WATER
D-1
Source of Water Supply
GIDC Notified area Ankleshwar
Status of permission from the concern authority.
Permission letter will provide you soon
D-2
Water consumption (KLD)
Category
Quantity
KLD
Remarks
(A) Domestic 2.0
(B) Gardening 1.0
(C) Industrial
Process 4.5
Washing 2.0
Boiler 4.8
Cooling 4.3
Others[Scrubber] 1.4
Industrial Total 17.0
Total (A + B + C) 20.0
Summary of
water
requirement
Quantity
KLD
Remarks
Total water
requirement for
20.0
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the project (A)
Quantity to be
recycled (B)
4.0 2.0 KLD Steam Condensate + 2.0KLD Cooling Water will be re-use
Total fresh
water
requirement (C)
16.0
Ensure Total water requirement = Fresh
water + Recycled water
i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility.
[Source of reuse & application area]
Source of
waste water
for reuse in
KLD (From
where it is
coming)
Application
area with
quantity in
KLD (Where it is
used)
Characteristics of
waste water to be
reused (COD, BOD,
TDS etc.)
Remarks
regarding
feasibility
to reuse
Not Applicable
D-3 Waste water generation (KLD)
Category Waste water KLD
Remarks
(A) Domestic 1.5
(B) Industrial
Process 3.8
Washing 2.0
Boiler 1.0
Cooling 0.7
Others[Scrubber] 0.0
Total Industrial
waste water 7.5
Total [A + B] 9.0
Brief Note on worst case scenario for waste water generation (Qualitative and
Quantitative):
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We have calculated all the details based on stoichiometric calculation and based on that
considering worst case scenario Total Industrial Water consumption from production
quantity will be 4.5 KLD and waste water generation will be 3.8 KLD. Details of Product
wise water consumption and waste water generation is attached as Annexure II.
QUALITATIVE AND QUANTITATIVE ANALYSIS OF EACH WASTE STREAM
Sr. No.
Source of Waste Water Generation
Quantity [KLD]
Parameter
Quality Final load at ETP in Kg/day
1. Boiler blow down 1.0 pH 6.5-8.0 --
TSS 500-600 mg/L 0.6
COD 200-300 mg/L 0.3
TDS 2500-3000 mg/L 3.0
2. Cooling Tower blow down
0.7 pH 6.0-8.5 --
TSS 600-700 mg/L 0.49
COD 500-800 mg/L 0.56
TDS 3500-4000 mg/L 2.8
3. Washing 2.0 pH 5.0-6.5 --
TSS 1000-1500 mg/L 3.0
COD 1000-1200 mg/L 2.4
TDS 3000-4000 mg/L 8.0
4. Process 3.8 pH 3.0-6.5 --
TSS 800-1000 mg/L 5.7
COD 20000-25000 mg/L
95.0
TDS 35000-40000 mg/L
152
Total Industrial Effluent
7.5 - -
CHARACTERISTICS OF WASTEWATER BEFORE & AFTER TREATMENT:- [PRIMARY + SECONDARY + CMEE-BEIL]
Sr. No.
Parameters
Unit Before
Treatment After Primary
Treatment
After Secondary Treatment effluent
send to CMEE_BEIL
1. pH -- 3.5-5.5 6.5-8.5 6.5-8.5
2. T.S.S. mg/l 1000-1500 250-370 100-150
3. C.O.D. mg/l 20000-25000 17000-21500 5100-6400
4. T.D.S. mg/l 35000-40000 36500-41500 36500-41500
Brief justification in case of no process effluent generation or no industrial effluent
generation or no high concentration effluent generation from proposed project
(Whichever is applicable).
Not Applicable
D-4 Mode of Disposal & Final meeting point
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-
Domestic: Domestic waste water will be collected and will be treated into ETP. Domestic waste water will be used in aeration tank for adequate treatment.
Industrial: Effluent generated from Process, Utilities and Washing section will be mixed with effluent generated from Domestic and treated into ETP [Primary + Secondary] treatment plant and after adequate treatment effluent send to CMEE-BEIL for further disposal.
Scrubbing water will be goes along with by product which will be sell to authorized end users registered under rule-9.
D-5 Treatment facilities
For Domestic waste water:
Capacity of STP: Domestic waste water will be collected and will be treated into ETP.
Domestic waste water will be used in aeration tank for adequate treatment.
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In
case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
Domestic: Domestic waste water will be collected and will be treated into ETP. Domestic waste water will be used in aeration tank for adequate treatment.
Industrial: Effluent generated from Process, Utilities and Washing section will be mixed with effluent generated from Domestic and treated into ETP [Primary + Secondary] treatment plant and after adequate treatment effluent send to CMEE-BEIL for further disposal.
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention
and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
Not Applicable
Generated effluent will be treated into ETP and then send to CMEE_BEIL for further
treatment
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Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
Not Applicable
Generated effluent will be treated into ETP and then send to CMEE_BEIL for further
treatment.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility (CF) (For waste water treatment)
Not Applicable
Membership of Common facility (CF) mentioning total capacity, consented quantity,
occupied capacity and spare capacity and norms of acceptance of effluent from member
units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G
(5)/550706 dated 08/01/2020.
Membership Certificate is attached as Annexure-III.
D-7 Simplified water balance diagram with reuse / recycle of waste water
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario
thereof: \
Considering the Calorific Value of the fuel and other parameters,
requirement of the heat, we have proposed consumption of fuel in m3/day.
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E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the
MOEFCC‘s OM vide dated 31.10.2019)
Sr.
no.
Source
of
emission
With
Capacity
Stack
Height
(meter)
Type
of
Fuel
Quantity
of Fuel
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air
Pollution
Control
Measures
(APCM)
1. Boiler [Cap. 1TPH]
25
Natural Gas
860 Nm3/Day
Adequate Stack Height
PM SO2 NOx
2.
TFH [Cap. 2 Lakh K Cal/Hr.]
20
Natural Gas
300 Nm3/Day
3. DG Set [150 KVA]
15 Diesel 60
Lit/Day
Adequate Stack Height
E-3 Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emissio
n
Stack/Vent
Height (meter)
Air Pollution Control Measures
(APCM)
1. Reaction Vessel-1 [Sr no. 1-4,6,7,810,11,12, 14,15,16,18]
HCl 18 Two Stage Water
Scrubber followed by Alkali Scrubber
2. Reaction Vessel-2 [SO2:-Sr no. 5,8,9,11] [HBr:-Sr no. 7,10,13,17]
SO2
HBr
18 Two Stage Alkali
Scrubber
Note:
Details of gaseous raw materials used in proposed project
Estimation of process gas emission (Product wise and Total)
Requirement of the scrubbing media (KL per Day) considering solubility (Product
wise and Total)
Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and
its sound management in HW matrix.
Details of scrubbing media are attached as Annexure-II.
E-4 Fugitive emission details with its mitigation measures.
Minimum Joints & flanges
Pumps with mechanical seals
Proper ventilation
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Adequate PPEs
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
Note:
Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9
permission, TSDF/CHWIH.
Quantification of hazardous waste shall be based on mass balance and
calculations shall be incorporated in EMP details separately.
Disposal to scrap vendors/vendors/traders is not allowed
Details of Product wise generation of Haz. Waste is attached as Annexure-II.
F-1 Hazardous waste management matrix
-
Sr. no.
Type/Name of Hazardous waste
Specific Source of generation (Name of the Activity, Product etc.)
Category and Schedule as per HW Rules.
Quantity (MT/Annum)
Management of HW
1. Empty barrels/ containers/liners contaminated with hazardous chemicals /wastes
Raw Material
and Packaging
33.1 50 Collection, Storage, Transportation, reuse or send back to supplier or sell to authorize end users registered under rule-9.
2. Used or Spent Oil
From Machinery
5.1 1.0 Collection, Storage, Transportation and sold to authorized Recyclers.
3. ETP Sludge ETP 35.3 79 Collection, Storage, Transportation and sent to Common TSDF site (Ankleshwar/Dahej)
4. Distillation Residue
From Product No. 1,2,3,5-10,
12-28
20.3 72 Collection, Storage, transportation and sent for co-processing in cement industries disposal at CHWIF-Ankleshwar/Dahej. (Through GPS mounted vehicle)
5. Spent Carbon From Product No.
2,3,6,15
28.3 6
6. Spent Catalyst From Product No.
21
28.2 18
7. Acetic Acid From -- 315 Collection, Storage,
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[30-40%] Product No. 12,22
Transportation and sell to authorized end users registered under rule-9.
8. HCl Sol. [28-33%]
Scrubber & From
Product No. 1-
4,6,7,810,11,12,
14,15,16,18
-- 450 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.
9. Sodium bisulfite Sol. [30-40%]
Scrubber & From
Product No. 5,8,9,11
-- 526 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.
10. Sodium Bromide [25-30%]
Scrubber & From
Product No. 7,10,13,17
-- 369 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.
11. Spent Solvent From Product No. 1,2,3,5-10,
12-28
28.6 730 Collection, Storage, Recovery and Recycle for manufacturing of product.
12. Sodium Hypo Chloride
Scrubber -- 10.0 Collection, Storage and reused in ETP as neutralizing agent.
13. Off-Specification Products
Process
28.4 5 Collection, Storage, transportation and sent for co-processing in cement industries disposal at CHWIF-Ankleshwar/Dahej. (Through GPS mounted vehicle)
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility.
Membership certificate will provide you soon.
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Not
Applicable
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the
Quantity (MT/Annum)
Management of Wastes
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Activity, Product etc.)
1 Not Applicable
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of
recovered Solvents etc.
(Details in Table Format)
Sr. No.
Name of Product
Name of Solvent
Boiling Point
Fresh Qty of Solvent
(TPM)
Recovered Qty of
Solvent (TPM)
% Rec.
1 1-4-Chloro Benzhydryl Piperazine Toluene 110.6°C 30 28.8 96.00
2 1-[2,3 Di Chloro Phenyl] Piperazine Hydrochloride
Methanol 64.7 °C 60 58.2 97.00
3 Dibenzo[b,f][1,4]Thiazepin-11[10H]-One
Ethanol 78.37 °C 37.5 36.375 97.00
5 Bis (2-Chloroethyl) Amine Hydrochloride
EDC 83.47°C 51 48.96 96.00
Acetone 56°C 12 11.64 97.00
6 8-Chloro-11-(4-methyl-1-piperazinyl)-5H-dibenzo[b,e][1,4] diazepine
Toluene 110.6°C 27 26.055 96.50
MDC 39.6 °C 21 20.265 96.50
IPA 82.50C 15 14.475 96.50
7 2-[2-3(S)-3-[2-(7-chloro-2-quinolinyl) -ethyl]phenyl]-3-hydroxypropyl] phenyl-2-propanol
Tetra Hydro furan
66 °C 15 14.4 96.00
DMF 153°C 12 11.55 96.25
8 3,4-dimethoxybenzoyl chloride Toluene 110.6°C 13.5 12.96 96.00
10 Methyl-5-bromo-2-hydroxy-3-propanoylbenzoate
EDC 83.47°C 6 5.76 96.00
12 1-Acetyl-4-(4-hydroxyphenyl)Piperazine
Methanol 64.7 °C 9 8.7 96.67
13 3-(3-chloropropyl)-7,8-dimethoxy-1,3-dihydro-2H-3-benzazepin-2-one
Methanol 64.7 °C 6 5.76 96.00
14 2-Butyl-4-Chloro-1H-imidazole-5-carbaldehyde
Methanol 64.7 °C 6 5.76 96.00
15 4-(4-aminophenyl)morpholin-3-one Toluene 110.6°C 6 5.76 96.00
16 6-Hydroxy-3,4-dihydroquinolin-2(1H)-one
Methanol 64.7 °C 6 5.76 96.00
17 1-(3-Chlorophenyl)-4-(3-Chloropropyl) Piperazine Hydrochloride
Toluene 110.6°C 6 5.76 96.00
18 1-(4-Fluorophenyl) Piperazine IPA 82.50C 9 8.76 97.33
19 2,6-Dimethylphenyl chloroacetamide Toluene 110.6°C 9 8.7 96.67
20 4,4'[2-Pyridinylmethylene] Bisphenol Ethyl Acetate 77.1°C 15 14.7 98.00
Methanol 64.7 °C 6 5.76 96.00
21 Trans 4-Amino Cyclohexanol Toluene 110.6°C 15 14.4 96.00
22 3-[Aminomethyl]-5-Methyl Hexanoic Acid
Methanol 64.7 °C 15 14.625 97.50
23 6 chloro-4- hydroxy- 2- methyl- 2H thieno [2,3-e] [1,2] thiazine- 3- carboxylate- 1,1- dioxide
Methanol 64.7 °C 9 8.7 96.67
Toluene 110.6°C 15 14.4 96.00
24 2-Amino 5-Methyl Thiazole Toluene 110.6°C 15 14.4 96.00
25 1-(3-Chlorophenyl) Piperazine Toluene 110.6°C 6 5.76 96.00
26 2-[2-(piperazin-1-yl)ethoxy]ethanol Xylene 139 °C 12 11.7 97.50
27 4,4,4-trifluo-1-(4-methylphenyl) butane-1,3-dione
Ethanol 78.37 °C 6 5.76 96.00
Methanol 64.7 °C 4.2 4.05 96.43
28 1-(4-methoxyphenyl)piperazine hydrochloride
Toluene 110.6°C 9 8.7 96.67
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G-2 Brief Note on LDAR proposed:
Sr.
No.
Source Probable
Pollutant
Emission
Control Measures/ APCM
1. Solvent storage tank Air pollutant (VOC)
i) Carry out work place area
monitoring to find out concentration
level in ambient air.
ii) Provision of breather valve
cum flame arrester.
G-3 VOC emission sources and its mitigation measures
(Details in Table Format)
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
-
Sr. no Name of Chemical Capacity of Tank
Number of Tanks
Hazardous Characteristics of Chemical
1 Methanol 8.0 KL 1 Nos. Flammable
2 Toluene 5.0 KL 1 Nos. Flammable
3 H2SO4 3.0 KL 1 Nos. Corrosive
Brief note on storage of Hazardous chemicals in Tanks
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels,
Carboys, Bags etc.
Other raw materials are store in Drums and Bags.
Safety details of Hazardous Chemicals:
Type of Hazardous Chemicals
Safety measures
HYDROGEN
• CCE approved premises with door having locking arrangement provided.
• Protect cylinders against physical damage. • Store in cool, dry, well-ventilated area, away from sources of heat,
ignition and direct sunlight. • Do not allow area where cylinders are stored to exceed 52°C
(125°F). • Isolate from oxidizers such as oxygen, chlorine, or fluorine. • Use a check valve or trap in the discharge line to prevent hazardous
backflow. • Post ―No Smoking or Open Flame‖ signs in storage and use areas. • Cylinders should be stored upright and be firmly secured to prevent
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falling or being knocked over. • Cylinders can be stored in the open, but in such cases, should be
protected against extremes of weather and from the dampness of the ground to prevent rusting.
• Never tamper with pressure relief devices in valves and cylinders. Electrical equipment should be non-sparking or explosion proof.
• Flammable high-pressure gas. • Use only in a closed system. • Use piping and equipment adequately designed to withstand
pressures and temperatures to be encountered. • Gas can cause rapid suffocation due to oxygen deficiency. • Never work on a pressurized system. • If there is a leak, close the cylinder valve. Blow the system down in
a safe and environmentally sound manner in compliance with all federal, state, and local laws; then repair the leak.
• Never place a compressed gas cylinder where it may become part of an electrical circuit.
• Apron, Hand gloves, gumboot, goggles & helmet provided • ISI Portable fire extinguisher & Hydrant line is provided as per TAC
norms. • Flame proof fitting provided. • Sufficient Nos. of SBA sets & 2 No. of Air line mask.
Hydrogen cylinders
Hydrogen cylinders will be stored in cylinder storage area. Cylinder storage license will be obtained from PESO as per Gas cylinder rules.
Hydrogen cylinder storage area will be made well ventilated and safe distance will be maintained as per gas cylinder rule.
Sprinkler system provision will be made in cylinder storage area.
Gas detectors will be provided in Hydrogen cylinder storage area.
Copper tube will be used for Hydrogen cylinder connection with header. PRV station will be provided for Hydrogen and nitrogen cylinder header.
Non sparking tools will be used for cylinder connection with header.
FLP type area will be provided.
Total enclosed process system.
Instrument & Plant Air System. DCS operational plant.
Nitrogen blanketing in Hydrogenation reactor.
Safety valve and Rupture disc provided on reactor.
Cooling Chilling and power alternative arrangement have been made on reactor.
Hydrogen and Nitrogen Cylinder bank away from the autoclave reactor.
PRV station with shut off valve, safety valve provision will be made for hydrogenation reaction safety.
Before Hydrogen Gas charging into reactor and after completion of reaction Nitrogen flushing will be done.
Flame arrestor will be provided on vent line of reactor and it will be extended up to roof level.
Open well ventilated and fragile roof will be provided to on reactor.
Safe Catalyst charging method will be adopted.
SOP will be prepared and operators will be trained for the same.
Static earthing and electric earthing (Double) provided.
Rector vent extended out side the process area and flame arrestor
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provided on vent line.
Dumping vessel arrangement will be made.
Jumpers for static earthing on pipeline flanges of flammable chemical will be provided.
Ethyl Acetate
Apron, Hand gloves, gumboot, goggles and helmet will be provided.
ISI Portable fire extinguisher & Hydrant line is provided as per TAC norms.
Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.
Level indicator provided. SBA set, Canister mask and airline mask is provided. Vent line dipped in dilute caustic will be provided. RCC foundation will be provided. Transfer material to another empty Vessel.
HCl Valve, pipeline are checked and maintain, in good condition. Apron, Hand gloves, gumboot, goggles and helmet will be provided. ISI Portable fire extinguisher & Hydrant line is provided as per TAC
norms. Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.
Level indicator provided. Vent line dipped in water will be provided. RCC foundation will be provided. Transfer material to another empty Vessel.
DMF/ EDC
All Gaskets are checked periodically & if new one replaces found
defective.
Joints are checked regularly to found any Leakage. Apron, Hand gloves, gumboot, goggles and helmet provided. ISI Portable fire extinguisher & Hydrant line is provided as per
TAC norms. Sufficient amount of sand/soil are kept to control any spillage. Flame proof fitting provided. Eye washer cum shower is provided near storage area.
Level indicator provided. Spark arrester are installed on all vehicles inside the premises. Vent line provided at sufficient height above roof building. Level indicator provided.
Methanol / Toluene/ Acetone/ Butanol
Tank, valve, pipeline are checked and maintain, in good condition through preventive maintenance.
Joints are checked regularly to detect any Leakage. ISI Portable fire extinguisher & Fire Hydrant line is provided as per
TAC norms. Flame proof electrical fittings / installation provided. Proper Earthing, Bonding & flange-to-flange jump ring is provided. Flame arrester provided on vent line. CCE approved Separate Storage area with door having locking
arrangement. Auto & manual sprinkler provided. Spark arrester are installed on all vehicles inside the premises. Apron, Hand gloves, gumboot, goggles and helmet provided. Train operator employed. Eye washer & shower provided. Tank‘s thickness measured on regular interval.
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Good ventilation in the area. Flame arrester with breather valve. Perforated dip pipe in dyke wall will be provided to monitor & detect
any leakage from tank. Sump will be made under dyke to recover leakage material from
dyke. Tanks will be kept under RCC dyke. Tanks will be kept under shed. All tanks will be connected to ETP.
Iso Propyl Alcohol
Valve, pipeline are checked and maintain, in good condition. Apron, Hand gloves, gumboot, goggles and helmet will be provided. ISI Portable fire extinguisher & Hydrant line is provided as per TAC
norms. Flameproof electrical connection will be provided. Separate storage area will be provided. Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.
Level indicator provided. RCC foundation will be provided.
Caustic Soda Lye
Dyke wall with sufficient size is provided. Tank, valve, pipeline are checked and maintain, in good condition. Apron, Hand gloves, gumboot, goggles and helmet provided. ISI Portable fire extinguisher & Hydrant line is provided as per TAC
norms. Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.
Level indicator provided.
AMMONIA (NH3)
• All Gaskets are checked periodically & if new one replaces found defective.
• Joints are checked regularly to found any Leakage. • ADEQUATE PPE is kept to handle the Hazard. • ISI Portable fire extinguisher & Hydrant line is provided as per TAC
norms. • Sufficient amount of sand/soil are kept to control any spillage. • Flame proof fitting provided. • Eye washer cum shower is provided near storage area. • Level indicator provided. • Spark arrester are installed on all vehicles inside the premises. • SBA set, Canister mask and airline mask is provided. • Earthing& bonding on tanks is provided. • Vent line dipped in water will be provided. • RCC foundation will be provided. • Transfer material to another empty Vessel.
Applicability of PESO : Applicable
H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of Process
Safety measures including Automation
Hydrogenation process:-A
For hydrogenation process, hydrogen gas will be used. Unit will allot separate storage area for hydrogen gas cylinder. Hydrogen is a colorless, odorless, tasteless, flammable nontoxic gas which is flammable over a wide range of concentrations.
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Standard Operating procedure shall be made for before Hydrogen Gas charging into reactor and after completion of reaction Nitrogen flushing will be done.
SOP will be prepared and operators will be trained for the same. Nitrogen blanketing will be done in Hydrogenation reactor. Safety
valve and Rupture disc will be provided on reactor. Safe Catalyst charging method will be adopted. Flame arrestor will be provided on vent line of reactor and it will be
extended above the roof level. Static earthing and electric earthing (Double) will be provided. Hydrogen gas detector will be installed for early detection of gas
leak. One RCC wall having thickness 20 cm will be provided on all side of
hydrogenation reactor to protect surrounding and other infrastructure during worst case scenario.
Nitration process
Not applicable
Chlorination process
Not applicable
Exothermic Reaction
Not applicable
H-3 Details of Fire Load Calculation
-
Total Plot Area: 1048.8.00 M2
Area utilized for plant activity: 363.0.00 M2
Area utilized for Hazardous Chemicals Storage:
238.00 M2
Number of Floors: G+2
Water requirement for firefighting in KLD :
0.0
Water storage tank provided for firefighting in KLD:
150 KL
Details of Hydrant Pumps: 5
Nearest Fire Station : 1-2 km
Applicability of Off Site Emergency Plan: Yes
-
H-4 Details of Fire NOC/Certificate:
After Getting EC/NOC we will apply for fire NOC.
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 15
Number of Contractual person/Labour : 10
Area provided for OHC: 30 sq. meter.
Number of First Aid Boxes : 3
Nearest General Hospital : 2 km
Name of Antidotes to be store in plant :
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
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Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. Ecopreneur Incorporate remains present during
video conference meeting.
Committee noted that the proposal is for Greenfield project in GIDC Ankleshwar. PP submitted details
regarding area adequacy. Source of water is GIDC. Product profile along with end use discussed in
depth. Looking to layout plan, Committee insisted for submit revised layout plan with mentioning
adequate separate entry and exit which is later on submitted by PP.
Committee noted that PP has submitted waste water management and total industrial effluent will be
treated in ETP and treated effluent will be sent to CMEE of M/s BEIL for evaporation. Domestic sewage
will be treated in ETP.
PP submitted that they have proposed boiler and DG set. Fuel used will be Natural gas for boiler and
thermo pack. Committee insisted for adequate stack height for thermo pack and PP later on submitted
revised flue gas emission details. Two stage scrubbers will be provided as APCM with each process
reactor stack. PP submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.
Upon asking regarding provision of fire hydrant network and proposed fire extinguishers details, PP has
addressed the Site Plan/layout plan with provision of fire hydrant network, periphery road with entry and
exit separately, proposed fire extinguishers details adequate fire water reservoir and fire load calculation.
Committee insisted for adequate fire water tank of 150 KL and PP later on submitted revised details.
Committee noted that PP has addressed fire evacuation plan, worker‘s safety and occupational Health
centre (OHC) and process hazard and its safety control measures. Committee insisted for auto control
system cost in EMP and PP later on submitted revised EMP.
Committee deliberated on storage and safety aspects of hazardous chemicals, green belt area, EMP,
CER, LDAR and solvent recovery etc. Looking to green belt area and plot size, Committee insisted for
more area of green belt outside premises and PP later on submitted Ankleshwar Industries Association
letter regarding it. Committee insisted for revised CER activity for infrastructure development instead of
general activity looking to cost of CER fund and PP later on submitted revised CER activity.
Committee found submission of project proponent satisfactory.
After detailed discussion, Committee unanimously decided to recommend the project to SEIAA,
Gujarat for grant of Environment Clearance
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon‘ble Supreme Court of
India in Civil Appeal no. 8478/2020 regarding operation of the Hon‘ble NGT orders dated 10/07/2019
& 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change in product mix,
after the 30th March 2021, considered as per the provisions in force at that time as mentioned in the
Notification vide S.O. 1223 (E) dated 27/03/2020 and S.O. 3636 (E) dated 15/10/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients (API) as
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per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any subsequent
amendments.
4. PP shall submit six monthly compliance report of Environmental Clearance without fail and the same
shall be critically assessed by the regulatory authority.
5. PP shall manufacture any two products from product list as per layout submitted by PP.
6. Wastewater shall be fed to CMEE only after providing adequate treatment in such a way that no
pollutant get air borne during evaporation to avoid adverse impact on Human Health & Environment.
7. The PP shall develop green belt [419 m2 inside plant premises + 320 m2 ouside the premises =
Total: 739 Sq. m.) i.e. 55 % of total plot area ] as per the undertaking submitted / committed before
SEAC. Green belt shall be developed with native plant species that are significant and used for the
pollution abatement as per the CPCB guidelines. It shall be implemented within 3 years of operation
phase in consultation with GPCB.
8. Domestic wastewater generation shall not exceed 1.5 KL/day for proposed project and it shall be
treated in ETP. It shall not be disposed off in soak pit and septic tank.
9. Close loop solvent recovery system with adequate condenser system shall be provided to recover
solvent vapours in such a manner that recovery shall be maximum and recovered solvent shall be
reused in the process within premises.
10. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB
guidelines. LDAR Logbooks shall be maintained.
11. The unit shall submit the list of authorized end users of hazardous wastes along with MoU signed
with them at least two months in advance prior to the commencement of production. In the absence
of potential buyers of these items, the unit shall restrict the production of the respective items.
12. Unit shall obtain all required permissions from the Narcotics Control Bureau for manufacturing,
storage and handling of Acetic Anhydride & any such chemicals.
13. Safety and Health:
a) PP shall obtain PESO permission for the storage and handling of hazardous chemicals. (If
applicable)
b) PP shall provide Occupational Health Centre (OHC) as per the provisions under the Gujarat
Factories Rule 68-U.
c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the concern
authority as per the prevailing Rules / Gujarat Fire Prevention and Life Safety Measures Act,
2016.
d) Unit shall adopt functional operations/process automation system including emergency
response to eliminate risk associated with the hazardous processes.
e) PP shall carry out mock drill within the premises as per the prevailing guidelines of safety and
display proper evacuation plan in the manufacturing area in case of any emergency or
accident.
f) PP shall install adequate fire hydrant system within premises and separate storage of fire
water and foam for the same shall be ensured by PP. Also PP shall provide alarm system in
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nearby fire station for emergency of any fire in plant area.
g) PP shall take all the necessary steps for control of storage hazards within premises ensuring
incompatibility of storage raw material and ensure the storage keeping safe distance as per
the prevailing guidelines of the concerned authority.
h) PP shall take all the necessary steps for human safety within premises to ensure that no any
harm is caused to any worker/employee or labor within premises.
i) Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.
j) Unit shall provide water sprinkler in Ammonia storage area.
k) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.
l) Unit shall store Bromine Bottle in cool dry separate area, out of direct sunlight.
m) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam
pouring system etc. to restrict cascade fire emergency in solvent tank farm.
3. SIA/GJ/IND2/173420/2020 M/s. Will Care Pharma
Plot No. 8/7, GIDC- Panoli, Ta-Ankleshwar,
Dist. Bharuch
Appraisal
Category of the unit: 5(f)
Project status: New
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173420/2020 on dated
05.10.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
This is a new unit proposes manufacturing of synthetic organic chemicals [API and API Intermediates] as
tabulated below,
Sr. No.
Name of Product CAS NO. Quantity (MT/Month) End Use Remarks
GROUP-A
1 Oxcarbazepine & it‘s intermediate 28721-07-5
60.0
Anticonvulsants Unit is proposed to mfg either individual or total production of (Product No.- 1 to 23) shall not exceed 60 MT/Month.
10-Methoxy Carbezapine 28721-09-7 Intermediate of Oxcarbazepine
2 Fluconazole & it‘s intermediate 86386-73-4 Anti allergies
DFTA(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl)Acetophenone)
86404-63-9
Intermediates of Fluconazole (1-[2-(2,4- difluorophenyl)-2,3-
epoxypropyl]-1H-1,2,4-Trizole) 86386-76-7
3 Gapapentin & it‘s intermediate Anticonvulsant
2-Azaspiro[4.5]decan-3-one 64744-50-9 Intermediate of Gabapentin
1,1-Cyclohexanediacetic acid monoamide
99189-60-3
4 Quetiapine Fumarate 111974-69-7 anti-psychotic
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5 Fenofibrate 49562-28-9 Antihyperlipidemic
6 Telmisartan & it‘s intermediate 144701-48-4 Antihypertensive
4-Methyl -6-(1-methyl-1H-benzoimidozol-2-yl)-2-propyl-1H-benzo imidazole
152628-02-9
4-Bromomethyl)biphenyl-2-carboxylic acid methyl ester
114772-38-2
Mehtyl -4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]methyl]biphenyl carboxylate
528560-93-2
7 Losartan Potassium & it‘s intermediate
114798-26-4 Antihypertensive
4‘-Bromomethyl-biphenyl-2-carbonitrile
114772-54-2
Intermediate of Losratan
2-butyl-4-chloro-5-formylimidazole 83857-96-9
4‘-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile
11477-55-3
2-Butyl-5-chloro-3-[2‘(2H-tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde
114798-36-6
8 Teneligliptin & it‘s intermediate 760937-92-6 Anti Diabetic
tert-butyl 4-oxo-2-(1,3-thiazolidin-3-ylcarbonyl)pyrrolidine-1-carboxylate OR (2S)-4-Oxo-2-(3-thiazolidinylcarbonyl)-1-pyrrolidinecarboxylic acid tert-butyl ester
401564-36-1 Intermediates of Teneligliptin
9 Aceclofenac Sodium & it‘s intermediate
89796-99-6 Anti Flammatory
Tert Buyl Chloroacetate 107-59-5 Intermediate of Aceclofenac
10 Hyscin Butylbromide & it‘s intermediate
149-64-4 Antimuscarinic
11 Rabeprazole Sodium & it‘s intermediate
117976-89-3 Antiulcer
2-[[[4-(3-methoxypropoxy)-3-methyl-2-pyridinyl] methyl] thio]-1H-benzimidazole
117977-21-6 Intermediates of Rabeprazole Sodium 2-[[4-(3-methoxypropoxy)-3-methyl-
pyridin-2-yl]methylsulfinyl]-1H-benzoimidazole
N/A
12 Etoricoxib & it‘s intermediate 202409-33-4 anti-inflammatory
2-Chloro -3-(dimethylamino)propene-1-iminium
N/A Intermediate of Etoricoxib
13 Tranexamic Acid & it‘s intermediate 1197-18-8 Used to treat heavy bleeding during your menstrual period
4(Aminomethyl)benzoic acid 56-91-7 Intermediate of Tranexamic Acid
4(Aminomethyl)cyclohexanecar boxilic acid
1197-18-8
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14 Pantoprazole & it‘s intermediate 102625-70-7 Used for heartburn, acid reflux and gastro-oesophageal reflux disease
2-Chloromethyl-3,4-dimethoxypyridini hydrochloride 72830-09-2 Intermediates of
Pantoprazole
5-Difluoromethoxy-2-{[(3,4-dimethoxy-2-pyridinyl)methyl]thio}-1H-benzimidazole 102625-64-9
15 Clopidogrel Bisulphate 120202-66-6 Antiplatelet
Methyl (+)-alpha-(2-thienylethylamino)(2-chlorophenyl)acetate
141109-19-5
Intermediate of Clopidogrel Bisulphate
16 2-n-Butyl-3(4-Hydroxy Benzoyl) Benzofuran (n-3)
52490-15-0 Intermediate of Amiodarone HCL
17 4-(2-Methoxy ethyl) Phenol 56718-71-9 Intermediate of Metoprolol succinate
18 P-chloro benzophenone 134-85-0 Intermediate of Cetirizine Dihydrochloride
19 P- chloro Benzhydryl chloride 134-83-8 Intermediate of Cetirizine Dihydrochloride
20 P-chloro benzhydryl piperazine 303-26-4 Intermediate of Cetirizine Dihydrochloride
21 Ketosulfone 221615-75-4 Intermediate of Etoricoxib
22 Thiophene-2-ethanol 5402-55-1 Intermediate of Nebivolol HCI
23 Bis-(2-chloroethyl amine)hydrochloride
821-48-7 Intermediate of Apiprazole
GROUP-B
24 Pregabalin & it‘s intermediate
148553-50-8
20.0
Anti -nervousness
Unit is proposed to mfg either individual or total production of (Product No.- 24 to 32) shall not exceed 20 MT/Month.
R-(-)-3-(Carbomethyl)-5-mehtyl hexonic acid R(+)-Alpha Phenylamine salt
3886-69-9 Intermediate of Pregabalin
25 Rosuvastatin Calcium 147098-20-2 Cardiovascular Disease
N-[4-4-Fluoro-phenyl)5-formyl-6-isopropyl-pyrimidine -2-yl]-N-methyl-methanesulfonamide
147118-37-4
3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid ethyl ester
147118-35-2
7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy-5-oxo-hept-
851443-04-4
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6-enoic acid ethyl ester
26 Atorvastatin Calcium & it‘s intermediate
134523-00-5 Antihypertensive
[6-(2-Aminol-ethyal)-2,2 dimethyl-[1,3]dioxin-4-y]-acetic acid tert-buytl ester
125995-13-3
Intermediate of Atorvastatin
6-[2,[2(-4-fluoro-phenyl)5-isopropyl-3-phenyl-4-phenylcarbomoyl-pyrrol-1-yl-]ethyl}-2,2-lyhtemid-[1,3]dioxin-4-yl)-tret dicaciteca -retse lytub
125971-95-1
7-[2-(4-flouro-phenyl)-5-isopropyl-3-phenyl-4-phentlcarbomyl-pyrrol-1-yl]-3,5 hydroxy-heptanoic acid-tert butyl(
134395-00-9
27 Carvedilol 72956-09-3 Antihypertansive
3-(Phenylhydrazino)cyclohexanone 27385-45-1 Intermediate of Carvedilol 4-Oxo-1,2,3,4-tetrahydrocarbezole 15128-52-6
4-(2,3-Epoxypropoxy)carbazole 51997-51-4
28 Glimipride & it‘s intermediate 93479-97-1 To treat type 2 diabetes
(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1(N—2-phenyl ethyl)-carboxamido]
N/A
Intermediate of Glimipride
4-[2-[(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1-yl) carboxamido] ethyl]benzene sulfonamide
119018-29-0
29 Thiocolchicoside 602-41-5 used as a muscle relaxan
30 Nimesulide & it‘s intermediate 51803-78-2 anti-inflammatory drug
O- Phenoxy Nitrobenzene 2216-12-8 Intermediate of Nimesulide
O- Phenoxy Aniline 2688-84-8
O- Phenoxy Methane N/A
31 Diclofenac Sodium & it‘s intermediate 15307-79-6 Anti Flammatory
(2,6-DICHLORO PHENYLAMINE) 15307-93-4
Intermediate of Diclofenac Sodium
(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)
15308-01-7
(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)
15362-40-0
32 Albendazole 54965-21-8 Anthelmintic
4-Thiocyno-2-Nitro- anilnemol 54029-45-7 Intermediate of Albendazole
2-Nitro-4-propyl thio aniline 54393-89-4
1,2,diamine-5-propyl thio benznene 66608-52-4
33 R&D -- 0.3
Total 80.3
# Brief Note of Product Profile: 3. No of Manufacturing Plants: 15 Reaction Vessel 4. Brief Note regarding number of Products to be manufactured considering plant capacity:
They have applied for (32 + R&D) nos. of product in either & or condition, They will not manufacturing above 80.3 MT/Month. And as per the list of machinery, they will be manufacturing 2 to 3 products at a time as orders received from market.
ENDUSE OF PRODUCTS
Sr. No.
Name of the Product CAS No. (Product)
Type/ Category of
Stage of Intermediat
Name of API in which
CAS No.
Said API is used for/End
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Product (API/
Intermediate)
e n-1, n-2, etc
Intermediate Used/ End use
of said Intermediate
(API) Use of said API
GROUP-A (Unit is proposed to mfg either individual or total production of Group - A (Product No.- 1 to 23) shall not exceed 60 MT/Month.)
1 Oxcarbazepine & it‘s intermediate
28721-07-5 API -- -- -- Anticonvulsants
10-Methoxy Carbezapine
28721-09-7 Intermediate
(n-2) Intermediate of Oxcarbazepine
28721-
07-5
Anticonvulsants
2 Fluconazole & it‘s intermediate
86386-73-4 API -- -- -- Anti allergies
DFTA(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl)Acetophenone)
86404-63-9 Intermediate
(n-2) Intermediates of Fluconazole
86386-
73-4
Anti allergies
(1-[2-(2,4- difluorophenyl)-2,3-epoxypropyl]-1H-1,2,4-Trizole)
86386-76-7 Intermediate
(n-3) Intermediates of Fluconazole
86386-
73-4
Anti allergies
3 Gapapentin & it‘s intermediate
60142-96-3 API -- -- -- Anticonvulsan
t
2-Azaspiro[4.5]decan-3-one
64744-50-9 Intermediate
(n-3) Intermediate of
Gabapentin
60142-
96-3
Anticonvulsan
t
1,1-Cyclohexanediacetic acid monoamide
99189-60-3 Intermediate
(n-2) Intermediate of Gabapentin
60142-
96-3
Anticonvulsan
t
4 Quetiapine Fumarate
111974-69-7
API -- -- -- anti-psychotic
5 Fenofibrate 49562-28-9 API -- -- -- Antihyperlipidemic
6 Telmisartan & it‘s intermediate
144701-48-4
API -- -- -- Antihypertensive
4-Methyl -6-(1-methyl-1H-benzoimidozol-2-yl)-2-propyl-1H-benzo imidazole
152628-02-9
Intermediate
(n-4) Intermediate of Telmisartan
144701-48-4
Antihypertensive
4-Bromomethyl) biphenyl-2-carboxylic acid methyl ester
114772-38-2
Intermediate
(n-3) Intermediate of Telmisartan
144701-48-4
Antihypertensive
Mehtyl -4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]methyl]biphenyl carboxylate
528560-93-2
Intermediate
(n-2) Intermediate of Telmisartan
144701-48-4
Antihypertensive
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7 Losartan Potassium & it‘s intermediate
114798-26-4
API -- -- -- Antihypertensive
4‘-Bromomethyl-biphenyl-2-carbonitrile
114772-54-2
Intermediate
(n-4) Intermediate of
Losratan
11479
8-26-4
Antihypertensi
ve
2-butyl-4-chloro-5-formylimidazole
83857-96-9 Intermediate
(n-3) Intermediate of
Losratan
11479
8-26-4
Antihypertensi
ve
4‘-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile
11477-55-3 Intermediate
(n-3) Intermediate of Losratan
11479
8-26-4
Antihypertensive
2-Butyl-5-chloro-3-[2‘(2H-tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde
114798-36-6
Intermediate
(n-2) Intermediate of Losratan
11479
8-26-4
Antihypertensive
8 Teneligliptin & it‘s intermediate
760937-92-6
API -- -- -- Anti Diabetic
tert-butyl 4-oxo-2-(1,3-thiazolidin-3-ylcarbonyl)pyrrolidine-1-carboxylate OR (2S)-4-Oxo-2-(3-thiazolidinylcarbonyl)-1-pyrrolidinecarboxylic acid tert-butyl ester
401564-36-1
Intermediate
(n-1) Intermediates
of
Teneligliptin
76093
7-92-6
Anti Diabetic
9 Aceclofenac Sodium & it‘s intermediate
89796-99-6 API -- -- -- Anti Flammatory
Tert Buyl Chloroacetate
107-59-5 Intermediate
(n-1) Intermediate of Aceclofenac
89796-99-6
Anti Flammatory
10 Hyscin Butylbromide & it‘s intermediate
149-64-4 API -- -- -- Antimuscarinic
11 Rabeprazole Sodium & it‘s intermediate
117976-89-3
API -- -- -- Antiulcer
2-[[[4-(3-methoxypropoxy)-3-methyl-2-pyridinyl] methyl] thio]-1H-benzimidazole
117977-21-6
Intermediate
(n-2) Intermediates of Rabeprazole Sodium
11797
6-89-3
Antiulcer
2-[[4-(3-methoxypropoxy)-3-methyl-pyridin-2-yl]methylsulfinyl]-1H-benzoimidazole
N/A Intermediate
(n-1) Intermediates
of
Rabeprazole
Sodium
11797
6-89-3
Antiulcer
12 Etoricoxib & it‘s intermediate
202409-33-4
API -- -- -- anti-inflammatory
2-Chloro -3-(dimethylamino)
N/A Intermediate
(n-1) Intermediate of Etoricoxib
202409-33-4
anti-inflammatory
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propene-1-iminium
13 Tranexamic Acid & it‘s intermediate
1197-18-8 API -- -- -- Used to treat heavy bleeding during your menstrual period
4(Aminomethyl)benzoic acid
56-91-7 Intermediate
(n-2) Intermediate of
Tranexamic
Acid
1197-
18-8
Used to treat
heavy
bleeding
during your
menstrual
period
4(Aminomethyl)cyclohexanecar boxilic acid
1197-18-8 Intermediate
(n-1) Intermediate of Tranexamic Acid
1197-
18-8
Used to treat heavy bleeding during your menstrual period
14 Pantoprazole & it‘s intermediate
102625-70-7
API -- -- -- Used for heartburn, acid reflux and gastro-oesophageal reflux disease
2-Chloromethyl-3,4-dimethoxypyridini hydrochloride
72830-09-2 Intermediate
(n-3) Intermediates of Pantoprazole
10262
5-70-7
Used for heartburn, acid reflux and gastro-oesophageal reflux disease
5-Difluoromethoxy-2-{[(3,4-dimethoxy-2-pyridinyl)methyl]thio}-1H-benzimidazole
102625-64-9
Intermediate
(n-1) Intermediates of Pantoprazole
10262
5-70-7
Used
for heartburn,
acid
reflux and
gastro-
oesophageal
reflux disease
15 Clopidogrel Bisulphate
120202-66-6
API -- -- -- Antiplatelet
Methyl (+)-alpha-(2-thienylethylamino)(2-chlorophenyl)acetate
141109-19-5
Intermediate
(n-1) Intermediate of Clopidogrel Bisulphate
12020
2-66-6
Antiplatelet
16 2-n-Butyl-3(4-Hydroxy Benzoyl) Benzofuran
52490-15-0 Intermediate
(n-3) Intermediate of Amiodarone HCL
19774-
82-4
Anti-
arrhythmic
17 4-(2-Methoxy ethyl) Phenol
56718-71-9 Intermediate
(n-3) Intermediate of Metoprolol succinate
98418-
47-4
Antihypertansi
ve
18 P-chloro 134-85-0 Intermediat (n-4) Intermediate of 83881- Antihistamine
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benzophenone e Cetirizine Dihydrochloride
52-1
19 P- chloro Benzhydryl chloride
134-83-8 Intermediate
(n-3) Intermediate of Cetirizine Dihydrochloride
83881-
52-1
Antihistamine
20 P-chloro benzhydryl piperazine
303-26-4 Intermediate
(n-2) Intermediate of
Cetirizine
Dihydrochlorid
e
83881-
52-1
Antihistamine
21 Ketosulfone 221615-75-4
Intermediate
(n-3) Intermediate of Etoricoxib
20240
9-33-4
NSAID
22 Thiophene-2-ethanol 5402-55-1 Intermediate
(n-3) Intermediate of Nebivolol HCI
12020
2-66-6
Antiplatelet
23 Bis-(2-chloroethyl amine)hydrochloride
821-48-7 Intermediate
(n-3) Intermediate of Aripiprazole
12972
2-12-9
Antidepressant
GROUP-B(Unit is proposed to mfg either individual or total production of Group - B (Product No.- 24 to 32) shall not exceed 20 MT/Month.)
24 Pregabalin & it‘s intermediate
148553-50-8
API -- -- -- Anti -nervousness
R-(-)-3-(Carbomethyl)-5-mehtyl hexonic acid R(+)-Alpha Phenylamine salt
3886-69-9
Intermediate
(n-2) Intermediate
of Pregabalin
148553-
50-8
Anti -nervousness
25 Rosuvastatin Calcium
147098-20-2
API -- -- -- Cardiovascular
Disease
N-[4-4-Fluoro-phenyl)5-formyl-6-isopropyl-pyrimidine -2-yl]-N-methyl-methanesulfonamide
147118-37-4
Intermediate
(n-4) Intermediate of Rosuvastatin Calcium
147098-
20-2
Cardiovascular Disease
3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid ethyl ester
147118-35-2
Intermediate
(n-3) Intermediate of Rosuvastatin Calcium
147098-
20-2
Cardiovascular Disease
7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy-5-oxo-hept-6-enoic acid ethyl ester
851443-04-4
Intermediate
(n-2) Intermediate of Rosuvastatin Calcium
147098-
20-2
Cardiovascular Disease
26 Atorvastatin Calcium & it‘s intermediate
134523-00-5
API -- -- -- Antihypertensive
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[6-(2-Aminol-ethyal)-2,2 dimethyl-[1,3]dioxin-4-y]-acetic acid tert-buytl ester
125995-13-3
Intermediate
(n-3) Intermediate of Atorvastatin
134523-
00-5
Antihypertensive
6-[2,[2(-4-fluoro-phenyl)5-isopropyl-3-phenyl-4-phenylcarbomoyl-pyrrol-1-yl-]ethyl}-2,2-lyhtemid-[1,3]dioxin-4-yl)- tret dicaciteca- lytubretse
125971-95-1
Intermediate
(n-2) Intermediate of Atorvastatin
134523-
00-5
Antihypertensive
7-[2-(4-flouro-phenyl)-5-isopropyl-3-phenyl-4-phentlcarbomyl-pyrrol-1-yl]-3,5 hydroxy-heptanoic acid-tert butyl
134395-00-9
Intermediate
(n-1) Intermediate of Atorvastatin
134523-
00-5
Antihypertensive
27 Carvedilol 72956-09-3
API -- -- -- Antihypertansive
3-(Phenylhydrazino) cyclohexanone
27385-45-1
Intermediate
(n-3) Intermediate of Carvedilol
72956-
09-3
Antihypertansive
4-Oxo-1,2,3,4-tetrahydrocarbezole
15128-52-6
Intermediate
(n-2) Intermediate of Carvedilol
72956-
09-3
Antihypertansive
4-(2,3-Epoxypropoxy) carbazole
51997-51-4
Intermediate
(n-1) Intermediate of Carvedilol
72956-
09-3
Antihypertansive
28 Glimipride & it‘s intermediate
93479-97-1
API -- -- -- To treat type 2 diabetes
(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1(N—2-phenyl ethyl)-carboxamido]
N/A Intermediate
(n-2) Intermediate of Glimipride
93479-
97-1
To treat type 2 diabetes
4-[2-[(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1-yl) carboxamido] ethyl]benzene sulfonamide
119018-29-0
Intermediate
(n-1) Intermediate of Glimipride
93479-
97-1
To treat type 2 diabetes
29 Thiocolchicoside 602-41-5 API -- -- -- used as a muscle relaxan
30 Nimesulide & it‘s intermediate
51803-78-2
API -- -- -- anti-inflammatory drug
O- Phenoxy Nitrobenzene
2216-12-8
Intermediate
(n-3) Intermediate of Nimesulide
51803-78-2
anti-inflammatory drug
O- Phenoxy Aniline 2688-84-8
Intermediate
(n-2) Intermediate of Nimesulide
51803-78-2
anti-inflammatory drug
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O- Phenoxy Methane
N/A Intermediate
(n-1) Intermediate of Nimesulide
51803-78-2
anti-inflammatory drug
31 Diclofenac Sodium & it‘s intermediate
15307-79-6
API -- -- -- Anti Flammatory
(2,6-DICHLORO PHENYLAMINE)
15307-93-4
Intermediate
(n-4) Intermediate of Diclofenac Sodium
15307-
79-6
Anti Flammatory
(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)
15308-01-7
Intermediate
(n-3) Intermediate of Diclofenac Sodium
15307-
79-6
Anti Flammatory
(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)
15362-40-0
Intermediate
(n-2) Intermediate of Diclofenac Sodium
15307-
79-6
Anti Flammatory
32 Albendazole 54965-21-8
API -- -- -- Anthelmintic
4-Thiocyno-2-Nitro- anilnemol
54029-45-7
Intermediate
(n-3) Intermediate of Albendazole
54965-
21-8
Anthelmintic
2-Nitro-4-propyl thio aniline
54393-89-4
Intermediate
(n-2) Intermediate of Albendazole
54965-
21-8
Anthelmintic
1,2,diamine-5-propyl thio benznene
66608-52-4
Intermediate
(n-1) Intermediate of Albendazole
54965-
21-8
Anthelmintic
The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 25.11.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr. no.
Particulars Details
A
A-1 Total cost of Proposed Project (Rs. in Crores):
3.90 crores
Break-Up of Project Cost
Particulars Proposed Amount
(Rs. in Crore)
Land Cost & It‘s Development 0.00
Civil Structure & Building 0.75
Plant & Machinery Cost 2.19
Environment protection measures (includes cost of ETP, Tree Plantation, etc.)
0.96
Total Project Cost 3.90
-
A-2 Details of Environmental Management Plan (EMP) As Below
Bifurcation of EMP Cost
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Sr. No
Unit Installed Capacity
(KLD)
Capital Cost (Rs. In Lakhs )
Operating Cost
(Lacs/Year)
Maintenance Cost
(Lacs/Year)
Total Recurring
Cost (Lacs/Year)
1 Waste Water 30 KLD 11.0 291.60 -- 291.60
2 Air -- 27.50 -- 3.40 3.40
3 Hazardous Management
-- 9.0 108.91 -- 108.91
4 Fire & Safety -- 25.0 -- 3.00 3.00
5 AWH Monitoring
-- 1.0 -- 1.00 1.00
6 Green Belt Development
-- 3.46 -- 1.80 1.80
7 Occupational Health
-- 4.0 -- 2.35 2.35
8 Corporate Environment Responsibility
For Year 2021-2024 15.6 -- -- --
Total 96.56 400.51 11.55 412.06
Summary
Cost of Project in Crores per Annum: 3.90 Cr.
EMP Capital Cost in Crores per Annum and Percentage: 0.96 Cr. (24.61%)
EMP Recurring Cost in Crores per Annum and Percentage: 4.12 Cr
--
A-3 Details of CER (As per MoEF&CC OM dated 01/05/2018) As Below
As per OM no. 22-65/2017 on dated 01/05/2018 regarding ―Corporate Environment Responsibility‖ (CER), Greenfield projects have to contribute 2% (Rs. 7.80 Lack) of the Capital Investment (3.90 Cr). But as per New Mechanism of CPCB vide letter no CPCB/IPC-VII/CEPI/NGT/2019 on dated 25/10/2019, we shall commit to do 4% (Rs. 15.60 Lack) of Project Cost as a CER. Our CER activity are as below table…
Component As per Norms Allocation
CER Rs. 7.80 Lakhs (2 %) Rs. 15.6 Lakhs (4 %)
Activities to be carried out under CER:
CER Activities Fund (Rs.)
2021-2022
Provided Solar street light set with battery backup (18W -15 Nos.) in Kharod Village
4,50,000/-
2022-2023
To provide Sports Equipment and stationary in the primary schools of Bakrol Village.
1,60,000/-
Company provide R.O. Plant (2000 Liter) and drinking water storage tank in Bakrol village
4,00,000/-
2023-2024
Company will purchased instrument and renovation of Primary Health center in Bhadkodra Village
5,50,000/-
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TOTAL 15,60,000 /-
-
B Land / Plot ownership details:
B-1 Total Plot area ( sq. meter) 2883 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Sr. No.
Description Gr. Floor
Area Sq. Meter
First Floor B/U Area Sq. Meter
Second Floor B/U Area Sq. Meter
1 Production Building 100 100 100
2 Raw Material Storage Area 200 -- --
3 Finish Product Storage Area 50 -- --
4 Haz. Waste Storage Area 150 -- --
5 Boiler Area 80 -- --
6 ETP 50 -- --
7 Hydrogen Storage Area 20 -- --
8 Gas storage Area 20 -- --
9 Admin & OHC Room 50 50 50
10 Green Belt Area (40%) 1153 -- --
11 Road & Open Area 1000 -- --
12 Security Cabin 10 -- --
TOTAL 2883
Company have store 1056 MT material as per calculations, we require 405 MT storage of material. Hence company has adequate area for storage of the Raw Material / Haz. Chemicals, Hazardous waste and Product. --
B-3 Green belt area ( sq. meter)
1153 Sq. m. (40%)
C Employment generation Direct - 15 Employees Indirect - 10 Employees Total - 25 Employees
D Water
D-1 Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Water Supply
Status of permission from the concern authority. GIDC Water Supply vide letter no NAO/PNK/742 dated 16/09/2020
D-2 Water consumption (KLD)
Category
Quantity KLD
Remarks
(D) Domestic 3.0
(E) Gardening 6.0
(F) Industrial
Process 12.4
Washing 5.0
Boiler 45.0
Cooling 30.0
Scrubber 2.4
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Other (R&D) 0.2
Industrial Total 95.0
Total (A + B + C) 104.0
--
As per our proposed product profile manufacturing process and mass balance, worst case scenario for water consumption is (Product no- 20) (P-chloro benzhydryl piperazine ) (4.80) and (Product no- 27) (Carvedilol) (7.57).
Summary of water requirement Quantity
KLD Remarks
Total water requirement for the project (A) 104.0
Quantity to be recycled (B) 62.5
Total fresh water requirement (C) 41.5
Ensure Total water requirement = Fresh water + Recycled water (104.0 = 41.5 + 62.5)
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]
Source of waste water for reuse in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
2.5 KLD Domestic effluent
Gardening Purposed
BOD-30 --
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. --
D-3 Waste water generation (KLD)
Category
Waste water KLD
Remarks
(A) Domestic 2.5
(B) Industrial
Process 14.3
Washing 5.0
Boiler 4.5
Cooling 3.0
Scrubber 3.2
Other (R&D) 0.2
Industrial Total 30.2
Total (A + B) 32.7
-
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative): As per our proposed product profile manufacturing process and mass balance, worst case scenario for waste water generation is (Product no- 22) (Thiophene-2-ethanol) (5.4) and(Product no- 27) (Carvedilol) (8.99)
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (If any applicable to proposal).
Not Applicable
D-4 Mode of Disposal & Final meeting point
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Domestic: 2.5 KLD domestic effluent will be treated into STP and reused for gardening purposed
Industrial: 27.0 KLD Effluent from process and utility will be treated into primary ETP and primary treated effluent send to common MEE for the final treatment and disposal. 3.2 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9 Permission.
-
D-5 Treatment facility within premises with capacity
For Domestic waste water: Capacity of STP – 3.0 KLD.
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. In-house ETP @ 30 KLD
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.)
CHARACTERISTICS BEFORE & AFTER TREATEMENT OF EFFLUENT
Sr. No.
Parameter
Characteristics(mg/L)
Primary treated Process
Boiler blow down
Cooling Tower blow down
Washing Composite
1 pH 3-9 8 - 8.5 8 - 8.5 5.5 - 8.5 3-9 6.5-7.5
2 TDS 28000 350 250 1000 28000 28700
3 TSS 500 250 350 200 500 75
4 COD 20000 30 100 600 20000 13000
5 BOD3 700 10 30 200 700 490
--
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
Not Applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Total proposed waste water generation from the industry will be 32.7 KLD (Ind. – 30.2 KLD + Dom. –2.5) Industrial:- 27.0 KLD Effluent from process and utility will be treated into primary ETP and primary
treated effluent send to common MEE for the final treatment and disposal. 3.2 KLD Scrubbing media reuse in plant premises & Sell to end user who is having
Rule-9 Permission. Domestic:- 2.5 KLD domestic effluent will be treated into STP and reused for gardening purposed.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
Common MEE Ms/ BEIL, Ankleshwer
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line
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with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
M/s. BEIL, Ankleshwar for Common MEE vide letter no BEIL/ANK/2020 dated 16/09/2020
D-7 Simplified water balance diagram with reuse / recycle of waste water
E Air
E-1 Brief Note on fuel based heat energy requirement and worst case scenario thereof:
SR. NO.
NAME OF FUEL QUANTITY
1. Briquette of Bio Coal 13 MT/Day
2. HSD 50 Lit/hr
Power Requirements: Proposed: Power required from DGVCL is 1000 KVA. Standby power supply from D.G. set (500 KVA) in emergency case. --
E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)
-
SR. NO.
SOURCE OF EMISSION
WITH
STACK HEIGHT (METER)
TYPE OF FUEL
QUANTITY OF FUEL
TYPE OF EMISSIONS
I.E. AIR
AIR POLLUTION CONTROL
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CAPACITY POLLUTANTS MEASURES (APCM)
1
Boiler
(Cap. - 1.5
MT/hr & 4.0
MT/hr) 30 M
Briquette of Bio Coal
10 MT/Day
PM
SO2 NOx
Multicyclone Separator With
Bag Filter
2
Thermic Fluid Heater (Cap. - 1 Lakh Kcal/ Hr)
Briquette of Bio Coal
3 MT/Day
Multicyclone
Separator With
Bag Filter
3
D.G. Sets
(Stand by)
(Cap. – 500 KVA)
18 M HSD 50
Liter/hr
Adequate
Stack Height
-
E-3 Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr. No.
Stack Attached To Stack Height
Air Pollution Control System
Parameter
1 Process Vent -1 (Chlorination/Sulphonation) Product No. 23
11 M
Two stage Scrubber (Water +
Alkali)
HCl SO2
2 Process Vent -2 (Nitrification) Product No. 30
11 M Two stage Alkali
Scrubber NOx
3 Process Vent -3 Product No. 5,32
11 M Two stage Alkali
Scrubber HBr
4 Process Vent -4 (Ammonification) Product No. 27
11 M Two stage
water Scrubber
NH3
5 Process Vent -5 (Chlorination) Product No. 32
11 M Two stage
water Scrubber
Cl2
Note:
Details of gaseous raw materials used in proposed project – Hydrogen gas, Ammonia
gas and Chlorine gas are used
Estimation of process gas emission (Product wise and Total) – process gas emission
for chlorination & Sulphonation – Product No.- 23, process gas emission for
Nitrification – Product No.- 30, process gas emission for Bromination– Product No.-
5,32 process gas emission for Ammonification – Product No.- 27, process gas
emission for Chlorination– Product No.- 32.
Requirement of the scrubbing media (KL per Day) considering solubility (Product wise
and Total).
Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its
sound management in HW matrix. Complied
E-4 Fugitive emission details with its mitigation measures:
Following measures will be adopted to prevent and control fugitive emissions… Solid raw material charging will be done through closed system to avoid fugitive emissions. Airborne dust at all transfers operations/ points will be controlled either by spraying water or
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providing enclosures. Adequate ventilation will be provided. Periodic monitoring of work area will be carried out to check the fugitive emission. Minimum number of flanges, joints and valves in pipelines. Regular inspection of floating roof seals and proper preventive maintenance of roofs and
seals for tanks. Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer
area will be collected through hoods and ducts by induced draft and controlled by scrubber/ dust collector / bad filter.
Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
F Hazardous waste management matrix (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Sr. no.
Type/Name of Hazardous waste
Source of generation
Category and
Schedule as per HW
Rules.
Quantity (MT/Annum)
Disposal Method
1 ETP Sludge ETP SCH-I/35.3 90 Collection, Storage, Transportation and Disposal at common TSDF site.
2 Discarded Drums/Bags/ Liners
Raw Materials/ Products
SCH-I/33.1 35 Collection, Storage, Transportation, Decontamination & Sale to GPCB approved vendors/ reuse /send back to supplier.
3 Used/ Spent Oil Machineries/Utility
SCH-I/5.1 1.4 Collection, Storage, Disposal by reuse in plant machinery as lubricant or transportation & Sale to GPCB registered re-processor.
4 Distillation Residue
Distillation SCH-I/20.3 184 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
5 Spent Solvent Process SCH-I/28.6 7311 Collections, Storage, distillation and reuse in
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plant premises.
6 Spent Carbon Process SCH-I/28.3 76 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
7 Organic Residue Process SCH-I/28.1 159 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.
8 Inorganic residue Process SCH-I/28.1 58 Collection, Storage, Transportation and sent for co-processing in cement industries or Disposal at common TSDF Site .
9 Spent Catalyst Process SCH-I/28.1 25 Collection, Storage, reuse in the plant premises or Transportation and send to regenerator under Rule-9.
10 Iron Sludge Process (Product No. 30)
SCH-I/28.1 277 Collection, Storage, Transportation and sent for co-processing in cement industries (in case of non-operation of co-processing site) Disposal at common incineration site.
11 Aluminum chloride
Process (Product
No. 18,31)
SCH-I/28.1 1193 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
14 Dilute HCl (28%) Process (Product No.- 25)
+ Scrubber (Product
No.- 23, 32)
SCH- II / B 15
10.70 +
468.3 = 479
Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 19 – 849 MT/Year)
15 Sodium bi sulphite (30%)
Scrubber SCH- II / B 15
82 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
16 Sodium Nitrate Scrubber SCH-I/28.1 22 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission
17 Sodium Bromide (25%)
Process (Product No.- 22)
+
SCH- II / B 15
492.12 +
516= 1009
Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.
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-
Scrubber (Product
No.- 5,32)
18 Liq. Ammonia (25%)
Scrubber SCH- II / B 15
159 Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 13 – 593.16 MT/Year)
19 Off Specification Products
From mfg. Process (Batch failure)
SCH-I/28.4 10 Collection, Storage, Transportation and sent for co-processing in cement industries (in case of non-operation of co-processing site) Disposal at common incineration site.
R&D
20 ETP Sludge ETP 35.3 3.0 Collection, Storage, Transportation & disposal in TSDF.
21 Residue from Distillation/ Organic Process Waste
R&D 28.1 4.0 Collection, Storage, Transportation & send to cement industries for co-processing or incineration in CHWIF.
22 Discarded Drum Raw Materials/Pr
oducts
33.1 20 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
23 Discarded Bags / Liner
Raw Materials/Pr
oducts
33.1 0.2 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.
24 Off Specification Products
R&D 28.4 1.0 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Company is obtain the provisional membership of TSDF & CHWIF
Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Ankleshwar for Common TSDF & CHWIF vide letter no BEIL/ANK/2020 dated 16/09/2020
F-3 Details of Non-Hazardous waste & its disposal (MSW and others)
Not Applicable
G Solvent management, VOC emissions etc.
G-1 Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)
SOLVENT RECOVERY AFTER LDAR
Sr. No.
Type of Solvent
% Recovery
% Losses
Air Water Haz
1 Methanol 96.4 0.86 1.84 0.90
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2 Cyclohexane 96.0 0.93 2.07 1.00
3 Methylne Dichloride 96.3 0.89 1.96 0.95
4 Ethyl Acetate 96.4 0.91 1.79 0.90
5 Dimethyl Formamide 96.5 0.76 1.87 0.87
6 Ethylene Dichloride 96.3 0.97 1.81 0.92
7 Acetone 96.4 0.88 1.82 0.90
8 Toluene 96.3 0.94 1.84 0.92
Justification of Reuse of solvent
Name of Solvent Total requirement
MT/Month
Total quantity of solvent recovered MT/Month
Methanol 95.06 91.63
Cyclohexane 37.40 35.89
Methylne Dichloride 64.00 61.6
Ethyl Acetate 44.00 42.41
Dimethyl Formamide 24.00 23.15
Ethylene Dichloride 210.00 202.26
Acetone 30.00 28.92
Toluene 260.00 250.32
--
G-2 Brief Note on LDAR proposed:
Company will be installed double mechanical seal and MSW Gaskets in solvent pipelines to prevent leakage from flanges
Company will be reduced the joints and valves in pipelines. All the rotating equipment like pumps will be installed with double Mechanical Seals to arrest
any sort of emissions. Flanges will be sealed so less losses will be there. Down the Temperature of Cooling tower to 5 0C Chilled Brine at -10 0C will be used to trap any traces of Solvent which is slipped from
Secondary condenser. Closed loop system. For continue vapor travelling 100mm of Hg (slight vacuum) will be applied on secondary
condenser. --
G-3 VOC emission sources and its mitigation measures (Brief note on LDAR)
Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.
Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.
To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps.
Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with on-line pH meter with hotter system for better operational control.
Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers.
All the raw materials will be pneumatically transfer to the reactor. Emphasis will be given to solvent management/solvent loss prevention. Control by having proper scrubbing system. Condenser to trap VOC. Proper gland packing will be maintained for pumps and valves and to the extent possible
pumps with mechanical seal.
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H Safety Detail
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
Details regarding storage of Hazardous chemicals
Storage details Name of major Hazardous chemicals Remarks
Storage tanks -- --
Drum/Barrel storage
All Other Raw material storage into Drum & Bags only like Methylene Dichloride, Acetic acid, Hydrochloric acid, Sulphuric acid.
Bottles --
Cylinder Ammonia gas, Hydrogen gas & Chlorine gas
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
FLP type light fittings will be provided. Proper ventilation will be provided in Godown. Proper label and identification board /stickers will be provided in the storage area. Conductive drum pallets will be provided. Drum handling trolley / stackers/fork lift will be used for drum handling. Separate dispensing room with local exhaust and static earthing provision will be made. Materials will be stored as per its compatibility study and separate area will be made for
flammable, corrosive and toxic chemical drums storage. Smoking and other spark, flame generating item will be banned from the Gate.
Safety details of Hazardous Chemicals:
Type of Hazardous Chemicals
Safety measures
Sulfuric Acid Milk of magnesia
Hydrochloric Acid Milk of Magnesia, Drink Large Quantity of Water
Acetic Acid Milk of magnesia
Methanol In case of acidosis give Sodium Bicarbonate. In case of delirium give Diazepam 10 mg. by intravenous injection.
Acetonitrile Hydroxocobalamin or the cynide antidote kit
Applicability of PESO : Company will apply for PESO after getting EC if applicable
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
Type of Process Safety measures including Automation
Hydrogenation Installed DCS Systeam FLP type area will be provided. Total enclosed process system. Instrument & Plant Air System. Nitrogen blanketing in Hydrogenation reactor. Safety valve and Rupture disc provided on reactor. Cooling Chilling and power alternative arrangement have been
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made on reactor. Hydrogen and Nitrogen Cylinder bank away from the auto clave
reactor. PRV station with shut off valve, safety valve provision will be
made for hydrogenation reaction safety. Before Hydrogen Gas charging in to reactor and after completion
of reaction Nitrogen flushing will be done. Flame arrestor will be provided on vent line of reactor and it will
be extended up to roof level. Open well ventilated and fragile roofs will be provided to on
reactor. Safe Catalyst charging method will be adopted. SOP will be prepared and operators will be trained for the same. Static earthing and electric earthing (Double) provided. Reactor vent extended outside the process area and flame
arrestor provided on vent line. Dumping vessel arrangement will be made. Dumpers for static earthing on pipeline flanges of flammable
chemical will be provided.
Ammonia Valve, pipeline will be checked and maintain, in good condition. All Gaskets will be checked periodically & if new one replaces
found defective. Joints will be checked regularly to found any Leakage. ADEQUATE PPE will be kept to handle the Hazard. ISI Portable fire extinguisher & Hydrant line will be provided as
per TAC norms. Sufficient amount of sand/soil are kept to control any spillage. Flame proof fitting provided. Eye washer cum shower will be provided near tank-farm area. Spark arrester will be installed on all vehicles inside the premises. SBA set, Canister mask and airline mask will be provided. Earthing& bonding on tanks will be provided. Vent line dipped in water will be provided.
Chlorination Chlorine Hood with blower will be provided with scrubbing arrangement.
Chlorine absorption system will be provided. In case of chlorine leakage in chlorine shed it will be suck through blower and it will be scrubbed in Caustic scrubber.
Safety Shower and eye wash will be provided in Chlorine shed area.
Emergency siren will be provided. First Aid Boxes and Occupational health centre will be made at
site. Chlorine cylinders will be stored in cylinder storage area. Safety Valve and pressure gauge will be provided on reactor. All emergency valves and switches and emergency handling
facilities will be easily assessable. All the vessels and equipments will be earthed appropriately and
protected against Static Electricity. Materials will be transferred by pumping through pipeline or by
vacuum Flame proof light fittings will be installed in the plant. All the Plant Personnel will be provided with PPE All employees will be given and updated in Safety aspects
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through periodic training in safety
Nitration The Reactor will have Temperature control system cascaded with cooling water system consisting of Cooling tower, pumps and circulating system. In case of high temperature the steam will get cut off and cooling water will start circulating through the reactor coils. Alternately Chilled water system is also provided for extreme emergencies.
The Reactor will have rupture disc and safety valves which will take care of excess pressure and the outlet of which is connected to the scrubbers.
The Reactor will also have a separate high local vent with pressure relief valve which is connected to a catch pot with water. The catch pot contents will be separated for recycle purpose. This will be additional safety, if 1 & 2 fail at the same time, which is unlikely.
In case of contact with eyes, immediately flush eyes with plenty of water for at least 15 minutes. Cold water may be used. Get medical attention immediately.
In case of contact with skin, immediately flush skin with plenty of water for at least 15 minutes while removing contaminated clothing and shoes. Cover the irritated skin with an emollient. Cold water may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention immediately.
Wash with a disinfectant soap and cover the contaminated skin with an anti-bacterial cream. Get medical attention.
If inhaled, remove to fresh air. If not breathing, give artificial respiration. If breathing is difficult, give oxygen. Get medical attention immediately.
Evacuate the victim to a safe area as soon as possible.
--
H-3 Details of Fire Load Calculation
Total Plot Area: 2883
Area utilized for plant activity: 300
Area utilized for Hazardous Chemicals Storage: 440
Number of Floors: G+2
Water requirement for firefighting in KL/hr: 3.51
Water storage tank provided for firefighting in KL 200
Details of Hydrant Pumps: One Fire pump, One diesel driven pump and one Jockey pump are being implemented.
Nearest Fire Station : Panoli GIDC – 2.25 Km
Applicability of Off Site Emergency Plan: N.A
-
H-4 Details of Fire NOC/Certificate: Company will apply for Fire NOC/Certificate after getting EC if applicable
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 15
Number of Contractual person/Labour : 10
Area provided for OHC: 15 Sq. Meter provided in Ground Floor at Admin Building
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Number of First Aid Boxes : 2
Nearest General Hospital : Welcare hospital – 0.8 KM
Name of Antidotes to be store in plant :
--
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. Ozone Enviro tech remains present during
video conference meeting.
This is new proposal of API and Its Intermediates plant at GIDC, Panoli. Source of water supply is GIDC.
Committee noted that proposed plot is taken over by PP on rental basis from plot owner namely, M/s
Baid Export Pvt. Ltd., which is textile unit. Upon asking, PP informed that original plot holder has done
sub-plotting and sub-plot was taken over as rent basis. PP could not furnish documents regarding the
NOC of GIDC for sub plotting of original plot and plot allotment letter mentioning purpose of the original
Plot.
After detailed discussion, Committee unanimously decided to defer the project and consider the
project only after submission of following documents,
1. Documents regarding the NOC of GIDC for sub plotting of original plot.
2. Plot allotment letter mentioning purpose of the original Plot.
4. SIA/GJ/IND2/164606/2020 M/s. Aalidhra Pharmachem Pvt. Ltd.
Plot No: C-289,289/1, GIDC Saykha, Ta-
Vagra, Dist: Bharuch
Appraisal
Category of the unit: 5(f)
Project status: New
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/164606/2020 on dated
29.09.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
This is a new unit proposes for manufacturing of synthetic organic chemicals [API and API
Intermediates] as tabulated below,
Sr. No.
Product Name CAS No. MT/ Month End Use
1 Fenofibrate 49562-28-9 22.0 to help Lower "bad" cholesterol and fats
2 Fexofenadine 83799-24-0 an antihistamine
3 Deferasirox 201530-41-8 to treat iron overload
4 Montelukast sodium 151767-02-1 to prevent and manage asthma symptoms
5 Nebivolol 99200-09-6 to treat high blood pressure
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6 Pregabalin 148553-50-8 20.0 an antidepressant
7 Derifenacin 133099-04-4 to treat an overactive bladder
8 Febuxostat 144060-53-7 to treat hyperuricemia
9 Linezolid 165800-03-3 antibiotic
10 Dabigatran 211915-06-9 anticoagulant
11 Metoprolol succinate 98418-47-4 18.0 to treat angina and hypertension
12 Metoprolol Tartrate 37350-58-6 to treat high blood pressure
13 Rivarixaroban 366789-02-8 to treat or prevent blood clots
14 Etoricoxib 202409-33-4 To treat eases pain and swelling
15 Olmesartan 144689-63-4 15.0 to treat high blood pressure
16 Telmisartan 144701-48-4 to treat high blood pressure
17 Brexpiprazole 913611-97-9 an antipsychotic medication
18 Macitentan 441798-33-0 to treat high blood pressure
19 Teneligliptin 760937-92-6 12.0 to treatment of type 2 diabetes mellitus
20 Vildagliptin 274901-16 to treatment of type 2 diabetes
21 Alogliptin 850649-62-6 to treatment of type 2 diabetes
22 Sitagliptin 486460-32-6 to treatment of type 2 diabetes
23 Duloxetine Hydrochloride 136434-34-9 10.0 to treat depression and anxiety
24 Selexipag 475086-01-2 to treat high blood pressure
25 Apixaban 503612-47-3 to prevent serious blood clots from forming due to a certain irregular heartbeat
26 Ticagrelor 274693-27-5 to treat angina and hypertension
27 Atorvastatin calcium 134523-00-5 9.0 to help Lower "bad" cholesterol and fats
28 Rosuvastatin calcium 147098-20-2 to help Lower "bad" cholesterol and fats
29 Bosentan 147536-97-8 to treat pulmonary arterial hypertension
30 Lurasidone Hydrochloride 367514-88-3 to treat certain mental/mood disorders
31 Nintedanib 656247-17-5 5.0 To treatment of idiopathic pulmonary fibrosis
32 Imatinib 152459-95-5 to treat certain types of cancer
33 Gefitinib 184475-35-2 to treat lung cancer
34 Ibrutinib 936563-96-1 to treat certain cancers
35 Apremilast 608141-41-9 3.0 to treat a certain type of skin condition
36 Vilazodone 163521-08-2 to treat depression
37 Brivaracetam 357336-20-0 anti-epileptic drug anticonvulsant
38 Erlotinib 183321-74-6 Cancer medicine
39 Lacosamide 175481-36-4 anti-epileptic drug
R & D -- 0.5 --
TOTAL 114.5 MT/Month
ENDUSE OF PRODUCTS
Sr. No.
Name of the Products
CAS no. Type/ Category of Product (API/
Stage i.e. n-1, n-2, etc.
Name of API in which Intermedia
CAS no. (API)
Said API is used for/End Use of said API
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Intermediate)
te Used/ End use of said Intermediate
1 Fenofibrate 49562-28-9 API -- -- -- to help Lower "bad" cholesterol and fats
2 Fexofenadine 83799-24-0 API -- -- -- an antihistamine
3 Deferasirox 201530-41-8
API -- -- -- to treat iron overload
4 Montelukast sodium
151767-02-1
API -- -- -- to prevent and manage asthma symptoms
5 Nebivolol 99200-09-6 API -- -- -- to treat high blood pressure
6 Pregabalin
148553-50-8
API -- -- -- an antidepressant
7
Derifenacin
133099-04-4
API -- -- -- to treat an overactive bladder
8 Febuxostat 144060-53-7
API -- -- -- to treat hyperuricemia
9 Linezolid 165800-03-3
API -- -- -- antibiotic
10 Dabigatran 211915-06-9
API -- -- -- anticoagulant
11 Metoprolol succinate
98418-47-4 API -- -- -- to treat angina and hypertension
12 Metoprolol Tartrate
37350-58-6 API -- -- -- to treat high blood pressure
13 Rivarixaroban 366789-02-8
API -- -- -- to treat or prevent blood clots
14 Etoricoxib 202409-33-4
API -- -- -- To treat eases pain and swelling
15 Olmesartan 144689-63-4
API -- -- -- to treat high blood pressure
16 Telmisartan 144701-48-4
API -- -- -- to treat high blood pressure
17 Brexpiprazole 913611-97-9
API -- -- -- an antipsychotic medication
18 Macitentan 441798-33-0
API -- -- -- to treat high blood pressure
19 Teneligliptin 760937-92-6
API -- -- -- to treatment of type 2 diabetes mellitus
20 Vildagliptin 274901-16 API -- -- -- to treatment of type
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2 diabetes
21 Alogliptin 850649-62-6
API -- -- -- to treatment of type 2 diabetes
22 Sitagliptin 486460-32-6
API -- -- -- to treatment of type 2 diabetes
23 Duloxetine Hydrochloride
136434-34-9
API -- -- -- to treat depression and anxiety
24 Selexipag 475086-01-2
API -- -- -- to treat high blood pressure
25 Apixaban 503612-47-3
API -- -- -- to prevent serious blood clots from forming due to a certain irregular heartbeat
26 Ticagrelor 274693-27-5
API -- -- -- to treat angina and hypertension
27 Atorvastatin calcium
134523-00-5
API -- -- -- to help Lower "bad" cholesterol and fats
28 Rosuvastatin calcium
147098-20-2
API -- -- -- to help Lower "bad" cholesterol and fats
29 Bosentan 147536-97-8
API -- -- -- to treat pulmonary arterial hypertension
30 Lurasidone Hydrochloride
367514-88-3
API -- -- -- to treat certain mental/mood disorders
31 Nintedanib 656247-17-5
API -- -- -- To treatment of idiopathic pulmonary fibrosis
32 Imatinib 152459-95-5
API -- -- -- to treat certain types of cancer
33 Gefitinib 184475-35-2
API -- -- -- to treat lung cancer
34 Ibrutinib 936563-96-1
API -- -- -- to treat certain cancers
35 Apremilast 608141-41-9
API -- -- -- to treat a certain type of skin condition
36 Vilazodone 163521-08-2
API -- -- -- to treat depression
37 Brivaracetam 357336-20-0
API -- -- -- anti-epileptic drug anticonvulsant
38 Erlotinib 183321-74-6
API -- -- -- Cancer medicine
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39 Lacosamide 175481-36-4
API -- -- -- anti-epileptic drug
The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr. no. Particulars Details
A-1 Total cost of Proposed Project (Rs. in Crores):
Total Project
10.0 Crores
Break-up of proposed project Cost:
Details Project Cost (Rs. In Crores)
Land 1.0
Building 2.0
Machinery 3.0
A-2 Details of Environmental Management Plan (EMP) As below:
Environment Issue/ Component
Remedial Measures
Component Capital Cost of EMP
Recurring Cost of EMP /Year
Hazardous waste generation & disposal
Proper collection, Safe Handling, Storage within premises and disposal of waste at approved TSDF, incineration facility, re-cyclers, re-processors.
Cost of TSDF/CHWIF site membership letter
Rs. 2,00,000/- --
Construction of Hazardous waste storage yard
Rs. 10,00,000/- --
Cost for TSDF disposal
-- Rs. 1,88,24,000/-
Cost for incineration disposal
-- Rs. 12,65,40,000/-
Effluent generation and treatment
ETP Construction Construction cost of ETP, STP
Rs. 1,50,00,000/- Rs. 2,00,000/-
--
Treatment cost of effluent/ year
-- Rs. 3,24,00,000/-
Rs. 10,51,20,000/-
Common MEE Membership
Rs. 1,00,000 --
STP Plant Rs. 3,50,000/- Rs. 25,000/-
Details of Air Adequate Cost of stack Rs. 10,00,000 --
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Emission pollution control system will be provided for control of gaseous emission. Adequate stack height for better dispersion of pollutants
installation of Stack
Cost of scrubber Rs. 4,50,000 --
Cost of MCS with bag filter
Rs. 7,00,000 --
Cost of LDAR With DSC in
Solvent Distillation
Rs.10,00,000 Rs. 25,000/- per year
Cost of
maintenance of APCM System
-- Rs. 1,50,000/- per year
Plantation 40 % of the plant area will be developed as greenbelt.
Cost of tree plantation
Rs. 40,95,000/- --
Cost of
maintenance -- Rs. 60,000/-
Monitoring of Environmental parameters
Regular monitoring of various environmental parameters will be carried out to check the effectiveness of the control system.
Cost of monitoring of various environmental parameters In-house COD, BOD, NH3-N, Instruments lab Set up. Third Party Monitoring
Rs. 15,00,000/- Rs. 1,50,000/-
Occupational Health and safety precaution
First aid box, Fire Fighting system, Periodical medical Check-up of employees, doctor‘s visit to the unit, insurance policy of the employees
Cost of PPE & Antidote 5 Beds, Oxygen Cylinder, Antidote, etc. (OHC)
Rs. 3,00,000/- Rs.30,000/-
Imparting safety training to employees every 6 months
-- Rs. 40,000/-
Medical examination of employees
-- Rs. 80,000/-
Cost of firefighting equipment's
Rs. 15,00,000/- Rs. 1,00,000/-
Cost of Fire Hydrant
Rs. 51,80,565 Rs. 5,00,000/-
Safety measures for Hazardous Operation- like Nitration, Ammoniation, i.e. Rupture disc, safety valve, alternate cooling
Rs. 18,00,000/- Rs. 1,00,000/-
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arrangement with DCS System
Safety measures for hydrogenation, & bromination i.e. DCS, O2 detector, auto damping system,
Rs. 10,00,000/- Rs. 1,00,000 per
year
Safety measures for Ammonia i.e. HCL torch detector, auto damping system with DCS System
Rs. 9 Lakhs Rs. 1,00,000 per
year
Trees Plantation and Provide Tree Protection Cage at Nearest Village Sayakaha & Vahiyal 260.0 Nos. of Trees
Rs.4,00,000/- --
To Provide Solar Lamps And Lights to Nearest School, Kothia, Pipaliya Village, Total No. 50
Rs.5,00,000/- --
Water Purifier System in Village (RO), Village: Bhersam, Chilad
Rs.5,00,000/- --
Setting up solar system in Sayakha village.
Rs.6,00,000/- --
Total Rs.
4,04,25,30565/- Rs.
28,43,44,000/-
Summary
Cost of Project in Crores 10.0 Crore
EMP Capital Cost in Crores per Annum and Percentage:
4.0 Crore
EMP Recurring Cost in Crores per Annum and Percentage:
28.43 Crore
A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide 31.10.2019.)
% as per the OM
Rs. in Crores
2 % 20.0 Lakh
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Brief note on proposed activities: As per OM no. 22-65/2017 on dated 01/05/2018 regarding ―Corporate Environment Responsibility‖ (CER), Expansion projects have to contribute 2% of the Additional Capital Investment, the company will contribute Rs 10.0 Lakhs as funds for CER activities Activities to be carried out under CER: Education,
Health, Environment Agriculture
B Land / Plot ownership details: Plot Allotment letter
B-1 Plot area
Total Plot area 33,168.00
10925.77 Sq. m. Green Belt
B-2 Brief note on Area adequacy in line to proposed project activities:
B-3 Green belt area
Total (Sq. meter)
Area in Sq. meter
10945.44 Sq. m.
% of total area
(33%)
C Employment generation
Total
Direct:25 Indirect:25
D WATER
D-1
Source of Water Supply (GIDC, Bore well, Surface water, Tanker supply etc...) GIDC Water Supply
Status of permission from the concern authority. Permission Granted
D-2
Water consumption (KLD)
Category
Quantity KLD
Remarks
(G) Domestic 15.0
(H) Gardening
12.0
(I) Industrial
Process 130.0
Washing 12.0
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Boiler 50.0
Cooling 50.0
Scrubber/Others 3.5
Industrial Total 245.5
Grand Total (A+B+C)
272.5
Brief Note on worst case scenario for water consumption:
Group:1 Product No: 01: Fenofibrate: 17.7 KLD Group:2 Product No: 06: Pregabalin: 28.37 KLD Group:3 Product No: 11: Metoprolol succinate: 13.29 KLD Group:4 Product No: 17: Brexpiprazole: 24.8 KLD Group:5 Product No: 19: Teneligliptin: 7.0 KLD Group:6 Product No: 23: Duloxetine Hydrochloride: 18.38
KLD Group:7 Product No: 29: Bosentan: 9.0 KLD Group:8 Product No: 34: Ibrutinib: 4.8 KLD Group:9 Product No: 36: Vilazodone: 7.29 KLD
-
Summary of water requirement
Quantity KLD
Remarks
Total water requirement for the project (A)
272.5
Quantity to be recycled (B)
59.0 KLD
Total fresh water requirement (C)
213.5
Ensure Total water requirement = Fresh water + Recycled water i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]
Source of waste water for reuse in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
STP Water Gardening pH: 7.0 COD: <50.0 BOD: <30.0
--
Boiler Condensate Cooling pH: 7.0 COD: <50.0 BOD: <30.0
--
In case of no reuse/recycle of waste water, Give brief
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note on justification as why no reuse/recycle.
D-3 Waste water generation (KLD)
Category Waste water
KLD Remarks
(C) Domestic 12.0
STP Plant
(D) Industrial
Process 160.0
Washing 12.0
Boiler 1.5
Cooling 1.5
Scrubber/Others 4.58
Total Industrial
waste water
179.58
Total [A + B] 191.58
Brief Note on worst case scenario for waste water generation (Qualitative and Quantitative):
Group:1 Product No: 02: Fexofenadine: 18.2 KLD Group:2 Product No: 06: Pregabalin: 21.59 KLD Group:3 Product No: 14: Etoricoxib: 18.46 KLD Group:4 Product No: 15: Olmesartan: 21.5 KLD Group:5 Product No: 19: Teneligliptin: 27.41 KLD Group:6 Product No: 23: Duloxetine Hydrochloride: 17.13 KLD Group:7 Product No: 28: Rosuvastatin calcium:11.95 KLD Group:8 Product No: 32: Imatinib: 6.70 KLD Group:9 Product No: 38: Erlotinib: 17.4 KLD
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (Whichever is applicable).
D-4 Mode of Disposal & Final meeting point
-
Domestic: Domestic waste water (12.0 m3/day) will be Treated In STP Plant and Reuse in Gardening
Industrial: Total water requirement will be 272.5 m3/day which will be met through GIDC water supply. The wastewater generation will be 191.58 m3/day. (Industrial: 179.58 KLD + Domestic: 12.0 KLD) 145.0 KLD Low COD/TDS Stream will be in Stream: 1 ETP:1 with Primary, Secondary Treatment and send to CETP of Saykha For final treatment and disposal. 30.0 KLD High COD/TDS Stream:2 will be treated in ETP:2 With Primary
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Treatment and send to Common MEE. Scrubbing media will be reuse in plant premises or send to end users having rule-9 permission.
- Clearly mention about final disposal
D-5 Treatment facilities
For Domestic waste water: Capacity of STP: 12.0 KLD
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed. DETAILS OF EFFLUENT TREATMENT PLANT Stream I (Low COD & TDS Stream) First all non-toxic and biodegradable streams (low & medium COD & TDS) of wastewater shall pass through oil & grease removal tank (ogrt-01) where floating o & g shall be removed manual from top and collected in o & g collection tank (ogct-01). Then effluent shall be collected in collection cum equalization tanks-01 (cets-01). Pipe grid is provided at bottom of the cets-01 to keep all suspended solids in suspension and to provide proper mixing. 2 nos. Of air blowers (1w+1 stand-by) shall supply air through to pipe grid. Then after, equalized wastewater shall be pumped to neutralization tank-1 (nt-01-b) where the continuous addition and stirring of lime solution is done to maintain neutral ph of wastewater from lime dosing tanks (ldt-01-a/b) as per requirement with help of lime dosing pumps. Then after, neutralized wastewater shall go to flash mixer (fm-01) by gravity. Alum shall be dosed from alum dosing tanks (adt-01-a/b) with help of dosing pumps. Then coagulated effluent shall be collected in flocculator (fl-01) where polyelectrolyte shall be dosed from polyelectrolyte dosing tank-1 (pedt-01) with help of pumps to carry out flocculation with help of flocculator mechanism. Then after, coagulated wastewater shall be settled in primary clarifier-1 (pcl-01). Clear supernatant from pcl-01 shall be passed in aeration tank-1 (at-01). Here, condensate from MEE and ATFT through condensate storage tank (cst-01) mix with effluent. Here, biodegradation of organic matter of the wastewater shall be carried out by bacteria (suspended growth) in the at-01 and for that oxygen shall be supplied by 2 nos. of air blowers (b-02) through diffusers. Air blowers also keep MLSS in suspension. Then after, wastewater shall go to secondary clarifier-1 (scl-01). Here, the suspended solids shall be settled. Sludge shall be removed from bottom of scl-01 and pumped to at-1 to maintain MLSS and excess activated sludge shall be sent to sludge sump (ss-01). Clear supernatant from scl-01 shall go to aeration tank-2 (at-02). Here biodegradation of left out organic matter of the wastewater shall be carried out by bacteria (suspended growth) and for that oxygen shall be supplied by two nos. Of blowers (b-03) with help of diffusers. Then after, wastewater shall go to secondary clarifier-2 (scl-02) from at-2. Here, the suspended solids shall be settled. Activated sludge shall be removed from bottom of scl-02 and pumped to at-02 to maintain MLSS and remaining will be sent to ss. Nutrients will be added from nutrient dosing tanks (ndts-01) to aeration tank-1 & 2 for growth of bacteria. Clear shall be collected in intermediate sump (is-01) by gravity. Thereafter, the wastewater shall be passed through multi grade filter (mgf-01) to remove left out TSS and activated carbon filter (acf-01) for final effluent polishing. After tertiary
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treatment, effluent shall be collected in treated effluent sump-01 (tes-01) before sent to CETP Dahej for further treatment. Sludge settled in pcl-01, pcl-02 and excess sludge from scl-01-b/02-b shall be collected in sludge sumps (sss-01-a/b) then sludge shall be pumped to centrifuge (cf-01) where poly shall be mixed from poly dosing tank-2 (pdt-02) with sludge to increase efficiency of centrifuge sludge dewatering. Then, dewatered sludge shall be stored in in HWSA and then ultimate disposal to TSDF. Leachate from cfs-01 and backwash from mgf-01 and acf-01 shall be collected in drain pit and pumped back to cet-01-a/b for further treatment. Stream II (High TDS stream) All high TDS streams of wastewater shall be collected in equalization cum neutralization tank-01 (ent-01). Here caustic shall be added from ldt-01 by gravity. Mixer is provided at bottom of the ent-01 to keep all suspended solids in suspension and for proper mixing. Then, neutralized wastewater shall be pump to flash mixer-02 (fm-02) where alum and polyelectrolyte shall be dosed from alum dosing tank (adt-01) and polyelectrolyte dosing tank (pedt-01) respectively by gravity. Then it will go into pst-01 where solids are allowed to settle and clear supernatant from pst-01 shall be collected in treated effluent sump (tes-01) before sent to common MEE M/s. BEIL for further treatment. EXPECTED CHARACTERISTICS OF WASTEWATER BEFORE & AFTER TREATMENT EXPECTED CHARACTERISTICS OF WASTEWATER: LOW COD STREAM
Sr. No.
Category of Wastewater
Untreated Primary Treated
Secondary Treated
Tertiary Treatment
CETP Norms
1 pH 4.5-8.5 6.5-7.5 6.5-7.5 6.5-7.5 6.5-7.5
2 COD (mg/L) 5000 3600 1600 1450 3000
3 BOD3 (mg/L) 1600 1100 500 400 1000
4 TDS (mg/L) 4000 4500 4500 4100 8000
5 NH3-N (mg/L)
30 30 30 30 50
High COD & TDS stream
Sr. No. Category of Wastewater Before Treatment After Treatment
1 pH 3.5 - 8.5 6.5 - 7.5
2 COD (mg/L) 28000 22000
3 BOD3 (mg/L) 9000 7000
4 TDS (mg/L) 33000 36000
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
CETP of Sayakha.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Total water requirement will be 272.5 m3/day which will be met through GIDC water supply. The wastewater generation will be 191.58 m3/day. (Industrial: 179.58 KLD + Domestic: 12.0 KLD) 145.0 KLD Low COD/TDS Stream will be in Stream: 1 ETP:1 with Primary, Secondary
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Treatment and send to CETP of Saykha For final treatment and disposal. 30.0 KLD High COD/TDS Stream:2 will be treated in ETP:2 With Primary Treatment and send to Common MEE. Scrubbing media will be reuse in plant premises or send to end users having rule-9 permission.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
Common MEE of M/s. BEIL
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
CETP of Sayakha
D-7 Simplified water balance diagram with reuse / recycle of waste water
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario thereof:
E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)
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DETAILS OF FLUE GAS
Sr. no. Source of emission With Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions i.e. Air Pollutants
Air Pollution Control Measures (APCM)
1 Boiler (5.0TPH)
30 m Briquettes of Bio-Coal
12.5 MT/Day
PM<150 mg/Nm3 SO2< 100 ppm NOx< 50 ppm
Multi-Cyclone Separator with bag filter With water scrubber
2 TFH (8 lakh kcal/hr.)
30 m Briquettes of Bio-Coal
14.0 MT/Day
Multi-Cyclone Separator with bag filter With water scrubber
3 D.G. Set (500 KVA)
11 m HSD 2500 lit/Day
Adequate height Provided
E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
DETAILS OF PROCESS GAS EMISSION
Sr. no.
Specific Source of emission (Name of the Product & Process)
Type of emission
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
1 Process Vent*-1 product no.06,21
HCl < 20 mg/Nm3 SO2<40.0 mg/Nm3
11m Two Stage Water + Alkali Scrubber
2 Process Vent*-2 Product No.18,29
NH3 < 175.0 mg/Nm3
11m Two Stage Water Scrubber
3 process vent-3 Product No.7,13,
HBr < 30.0 mg/Nm3
11 m Two Stage Water Scrubber
Note: Details of gaseous raw materials used in proposed project Estimation of process gas emission (Product wise and Total) Requirement of the scrubbing media (KL per Day) considering solubility (Product wise
and Total) Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its
sound management in HW matrix.
Sr. No.
Emissions
Assumed Quantity of Gaseous
Emissions (MT/Day)
Water required to
scrub pollutants (KL/Day)
% of solution Quantity of bleed
liquors (KL/Day)
1 HCl SO2
0.48 0.24
1.14 NaOH: 0.72
Dil. HCL (30 %) Sodium Sulphite
soln.
1.62 0.96
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(25 %)
2 NH3 0.20 0.89 Ammonia soln. (15-20 %)
1.09
3 HBR 0.25 0.75 Hbr Solution (25 %)
1.0
Total 3.5 KL/Day 4.58 KL/Day
E-4 Fugitive emission details with its mitigation measures.
Following measures will be adopted to prevent and control fugitive emissions: 1. Airborne dust at all transfers operations/ points will be controlled either by spraying water or
providing enclosures. 2. Adequate ventilation will be provided. 3. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent
leakages and thus minimizing the fugitive emissions. 4. Entire process will be carried out in the closed reactors with proper maintenance of pressure and
temperature. 5. Periodic monitoring of work area will be carried out to check the fugitive emission. 6. Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with on-line
pH meter with hooter system for better operational control. 7. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be
connected to vent chillers. 8. Minimum number of flanges, joints and valves in pipelines. 9. Regular inspection of floating roof seals and proper preventive maintenance of roofs and seals for
tanks. 10. Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer
area will be collected through hoods and ducts by induced draft and controlled by scrubber/ dust collector.
11. Dedicated scrubber will be provided are used for fugitive emissions to control. 12. For dust emissions bag filter will be provided. 13. Enclosures to chemical storage area, collection of emission from loading of raw materials in
particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
-
Sr. no.
Type/Name of Hazardous waste
Specific Source of generation (Name of the Activity, Product etc.)
Category and Schedule as per HW Rules.
Quantity (MT/Annum)
Management of HW
1 ETP Sludge
ETP Sch-I /35.3 502.0 MT/Annum
Collection, Storage, Transportation and dispose to TSDF site.
2 Discarded Drums /Containers
Raw material Sch-I/33.1 100.00 MT/Annum
Collection, Storage, Transportation, Decontamination & Disposal by selling to
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3 Discarded Liner/Bag
Raw material Sch-I/33.1 12.00 MT/Annum
registered recycler
4 Used Oil
Plant Machinery Sch-I/5.1 6.00 MT/Annum
Collection, Storage, Transportation, Disposal by selling to registered recycler or re-use as lubricant
5 Spent Sulphuric Acid
From Mfg. Of Sch-I/28.1 (II-B-B15)
1962.0 MT/Annum
Collection, Storage, Transportation and sell to end user
6 Spent Carbon
From mfg. process
Sch-I/28.3 194.0 MT/Annum
Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site.
7 Spent Catalyst
From mfg. process
Sch-I/28.3 20.0 MT/Annum
Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site.
8 Spent Solvents
From mfg. Process
Sch-I/28.6 16800.00 MT/Annum
Collection, Storage, recovered through in house distillation or sent for distillation job work to authorized recycler then reuse in process
9 Distillation Residue
From Solvent recovery plan
Sch-I/28.1 504.00 MT/Annum
Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site
10 Organic Waste
From process of Sch-I/28.1 7718.0 MT/Annum
Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site
11 Inorganic waste
From process Sch-I/28.1 8910.0 MT/Annum
Collection, Storage, Transportation and dispose to TSDF site.
12 Sodium Sulphate
From mfg. process
Sch-I/28.1 1208.4 MT/Annum
Collection, Storage, Transportation And send to end user having rule-9 permission.
13 HCl (30%) From Scrubber Sch-I/28.1 535.0 MT/Year
Collection, Storage, Transportation And send to end user having rule-9 permission.
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14 Sodium Sulfite
Solution (25%)
From Scrubber Sch-I/28.1 317.0 MT/Year
Collection, Storage, Transportation & sell to end user having Rule-9 Permission.
15 Liq. Ammonia (15-20%)
From Scrubber Sch-I/28.1 360.0 MT/Year
Collection, Storage, Transportation & sell to end user having Rule-9 Permission.
16 HBr Solution (25%)
From Scrubber Sch-I/28.1 330.0 MT/Year
Collection, Storage, Transportation & sell to end user having Rule-9 Permission.
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility.
F-3 Details of Non-Hazardous waste & its disposal (MSW and others)
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
1
2 Fly Ash
From APCM
440 MT/Annum Collection, Storage, Transportation & send to brick manufacturer
3
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.
All the solvents shall be directly distilled from product mixes and; if required shall be purified in packed column with the help of reflux and therefore there is no generation of any distillation residue from the solvent distillation.
The solvent distillation system shall be designed so as to achieve minimum 96.0 % recovery of solvent.
Pure solvent, crude solvent and distilled (recovered) solvent shall be stored only in storage tanks and we shall not be using drums at any stage in the Solvent Management System.
Wherever required, the solvents shall be directly pumped into day tanks from the storage tanks and shall be charged into the reactors without involving any manual handling.
All the pumps shall be mechanical seal type to avoid any leakage of solvent.
All necessary fire fighting systems shall be provided with alarm system. Flame proof wiring and flame proof electrical accessories shall be provided to avoid any mishap.
All the storage tank and day tank shall be connected to a vent system through cooling water and chilled brine condensers to prevent loss of solvents in the atmosphere.
All the distillation column vents will be also connected to cooling water/chilled brine
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condensers for maximum possible recovery of the solvents.
All the vents will be connected to a common carbon Adsorber for removing traces of solvent from vent gases.
Residue generated from the distillation will be incinerated in-house or sent to BEIL incinerator site.
Coolant to be used Primary Condensers Cooling Water Secondary Condensers Chilled Brine up to -5
0C
G-2 Brief Note on LDAR proposed:
LEAK DETECTION AND REPAIR (LDAR) To prevent losses of these solvents in atmosphere, following infrastructure shall be used in
addition to LDAR program: Leak Free Pumps for transfer of solvents MSW Gaskets in solvent pipelines to prevent leakage from flanges Minimum number of flanges, joints and valves in pipelines. Down the Temperature of Cooling tower to -5
0C.
Chilled Brine at -15 0C will be used to trap any traces of Solvent which is slipped from
Secondary condenser. For continue vapor travelling 100mm of Hg (slight vacuum) will be applied on secondary
condenser. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at
all solvent pumps. All the rotating equipments like pumps will be installed with Mechanical Seals to arrest any
sort of emissions. Condenser and scrubber post Reactor with cooling arrangement Enclosures to chemical storage area, collection of emission from loading of raw materials in
particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send to ETP.
If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark
Flanges will be sealed so less losses will be there.
IMMEDIATE REPAIR OF DEVICES IN CASE OF LEAKAGES A regular preventive maintenance schedule will be in place to replace or rectify all gaskets
and joints etc to ensure no fugitive emissions shall take place. Plant shall also maintain adequate number of spares and consumables required to repair the
leaking device Plant shall also have competent contractor team to handle Leakages and can repair the same
immediately Standby equipments like Pumps, valves etc shall be kept basis the criticality and usage Plant shall also have access equipments like Boom lift to handle leakages at height
immediately
MONITORING OF SOLVENT LOSSES In warding, storage and consumption of solvents in various products shall be measured
through Level Transmitters and Load cells weighing systems resp. The quantity at each stage shall be reconciled periodically to arrive at Losses.
Periodic monitoring of work area will be carried out to check the fugitive emission. VOC detectors will be installed at various places to detect leak.
PREVENTIVE MAINTENANCE TO PREVENT LEAKAGES In order to prevent leakage from Pump, Seals, Valves etc, preventive maintenance shall be
carried out periodically as per plan. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.
Sr. No. Component Preventive Maintenance schedule
1 Pump seals with visible liquid dripping
Daily
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2 Valves/flanges Quarterly
3 Compressor seals Quarterly
4 Pressure relief devices Yearly
5 Pipeline Thickness Testing Yearly
G-3 VOC emission sources and its mitigation measures
During operation stage, leakage through valves/pumps, leakage and emission from open drum containing chemicals, open feeding, storage tanks, etc. will be major sources of fugitive emissions and VOCs. Excess use of solvent/s may also results fugitive emission from the process vessels.
Solid raw material charging will be done through closed system.
Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.
Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers.
Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area, will be collected through hoods and ducts by induced draft and controlled by scrubber/dust collector.
Emphasis will be given to solvent management/solvent loss prevention.
Control by having proper scrubbing system.
Condenser to trap VOC.
Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber/dust collector to be ensured.
Proper maintenance schedule will be adhered to avoid emissions through flange joints, pump seals etc.
Minimum number of flanges, joints and valves in pipelines.
Proper gland packing will be maintained for pumps and valves and to the extent possible pumps with mechanical seal.
All the raw materials will be pneumatically transfer to the reactor.
All rotating equipments like pumps will be installed with mechanical seals to arrest any sort of emissions.
A regular preventive maintenance schedule will be in place to replace or rectify all gaskets and joints etc. as a part of ISO systems to ensure no fugitive emissions take place.
Periodic monitoring of work area will be carried out to check the fugitive emission.
Solvent tank vents will be connected to vent chillers.
Adequate ventilation will be provided.
Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures.
Breather valves will be provided on solvent tanks.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
- Brief note on storage of Hazardous chemicals in Tanks
All chemical store in Drums
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
All chemical store in Drums
Safety details of Hazardous Chemicals:
Sr. No. Name Of Hazardous Substance
Control Measures Provided
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1 Sulphuric Acid 1. Store in a cool, dry, ventilated storage area with acid resistant floors and good drainage. Protect from physical damage. Keep out of direct sunlight and away from heat, water, and incompatible materials. Do not wash out container and use it for other purposes.
2 Caustic Lye 1. Store at ambient temperatures with venting open. Protect containers against physical damage and water.
2. Handling should occur in a chemical fume hood.
3 35 % Hydrochloric Acid
1. Safeguard containers against mechanical injury. 2. Emergency eyewash fountains and safety showers
should be available in the immediate vicinity of potential exposure. Do not puncture or incinerate containers.
3. Wear appropriate chemical protective clothing.
4 Thionyl Chloride 1. Store in a cool, dry, area away from incompatible substances. Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment., No manual handling
5 Phenol 1. Store in a cool, dry, underground storage area away from incompatible substances. Flammables-area. Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment.
6 Toluene 1. Store in a, dry well-ventilated location, away from any area where the fire hazard may be acute. If the exposure limit is exceeded and engineering controls are not feasible, a full face piece respirator with organic vapor cartridge may be worn up to 50 times the exposure limit or the maximum use concentration specified by the appropriate regulatory agency or respirator supplier, whichever is lowest above flash point, vapor-air mixtures are explosive within flammable limits noted above.
7 EDC 1. Keep away from heat, sparks, and flame. Keep away from sources of ignition. Store in a tightly closed container, Wear appropriate protective eyeglasses or chemical safety goggles., Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment., No manual handling
8 IPA 1. Store in a cool, dry place. Store in a tightly closed container, Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment., No manual handling
9 HBR HBR will be stored in Iso-container in separate storage area and transported in Iso-container.
10 Methanol Flame proof plant, pumping transfer, close process, etc. Double Static earthing, Dyke wall , Tanker unloading procedure. SCBA sets available. Flame proof plant, pumping transfer, close process, etc. Jumper clips on flanges, Fire extinguishers, Fencing and No, Smoking and prohibited area., Tanker unloading procedure., Flame arrestor provided on vent line of the tank, Hydrant system
11 Dimethyl Formamide
12 Hydrogen
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13 Nitric Acid Safety Showers provided
Caution note provided
Dyke wall provided
Level gauge provided.
Double drain valve provided
Scrubber provided, Required PPEs provided to all employees
Applicability of PESO : Not Applicable All Raw material will be store as PESO Standards
H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
- Hydrogenation Plant: • FLP type area will be provided. • Total enclosed process system. • Instrument & Plant Air System. • Nitrogen blanketing in Hydrogenation reactor. • Safety valve and Rupture disc provided on reactor. • Cooling Chilling and power alternative arrangement have been made on reactor. • Hydrogen and Nitrogen Cylinder bank away from the auto clave reactor. • PRV station with shut off valve, safety valve provision will be made for hydrogenation
reaction safety. • Before Hydrogen Gas charging in to reactor and after completion of reaction Nitrogen
flushing will be done. • Flame arrestor will be provided on vent line of reactor and it will be extended up to
roof level. • Open well ventilated and fragile roofs will be provided to on reactor. • Safe Catalyst charging method will be adopted. • SOP will be prepared and operators will be trained for the same. • Static earthing and electric earthing (Double) provided. • Reactor vent extended outside the process area and flame arrestor provided on vent
line. • Dumping vessel arrangement will be made. • Jumpers for static earthing on pipeline flanges of flammable chemical will be
provided. Nitration process
• Total enclosed process system. • Instrument & Plant Air System. • Safety valve and Rupture disc provided on reactor. • Cooling and power alternative arrangement have been made on reactor. • Emergency cooling alternative arrangement have been made on reactor. • Nitric acid storage away from the auto clave reactor. • Open well ventilated and fragile roofs will be provided to on reactor. • Scrubbing system will be installed to scrub nitrous gases generated during reaction. • SOP will be prepared and operators will be trained for the same. • Employees will be trained to handle nitric acid and continuous training schedule will be made. • Dumping vessel arrangement will be made.
H-3 Details of Fire Load Calculation
FIRE LOAD CALCULATION
1 Name & Address of factory : M/s. Aalidhra Pharmachem Pvt. Ltd. Plot no. C-289,289/1, GIDC Saykha, Ta-Vagra, Dist-Bharuch, Gujarat, India.
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2 Phone Number : +91 99798 62155
3 Name of Occupier : Mr. Manish Gondalia
4 Total Floor of the factory : G + 1
5 Detail of Combustible Area (In sq. Meter)
a) Total Floor Area : 19650.0 M2
b) Open Space Area in which Combustible Material stored
: 100 M2
c) Area having more than 15 meter Height
: 0 M2
d) Area having Wooden material
: 500 M2
Total (a + b + c + d) : 20250 M2
6 a + b + c + d . 20
: 20250/20= 1012.5 L/Min
7 Total Requirement of Water (based on area in sr. no-6)
: 60750 Ltrs
8 Current Water storage Capacity for fire hydrant (Proposed)
: 750000 Ltrs
Under ground Tank + over head tank + On ground Tank
: UG Water Tank:
375,000 UG Water
Tank: 375,000
Ltrs
9 In case of Fire, Arrangement for water to be used in fire fighting
a) Is Hydrant Line available? If Yes give dimension of Pipe.
: Fire Hydrant Line with 6‖ pipe diameter is being implemented
b) Which type of arrangement are available for Supply water on ground or upper floor i.e. Pipe line and it's Diameter (c.m.); Give detail
: 1700 meter length of 6‖ pipe diameter will be provided for fire hydrant system.
c) Are Fire Water Pump Available or Not? Give detail
: Kirloskar main pump*2 (30000 Lit/Hr, 110-meter head) and one jockey pump (15 m3/hr, 75-meter head) will be provided
10
If the Value of Sr. 6 is more than 550, then requirement of trailer Pump is applicable. If it applicable then what is the arrangement for the Same. Give detail
: Trailer pump will be available having capacity of 1800 LPM at 7 kg/cm2
11
How many water buckets required?
: 90 nos
12
How Many 9 Litres water type Extinguisher required?(Water Bucket/6)
Fire Extinguisher
required =
90 / 6 = 15
Bucket may be dispensed with provided supply of extinguisher
is double than indicate above =
15 + 15
= 30
1 Requirement of 5 Kg CO2 : 0 nos
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3 Type Fire Extinguisher for Class - E fire. Floor wise (1 for every 15 m length)
Total requirement of Fire extinguishers (5 Kg ABC).
: 35 + 0 35 Nos.
14
Details of installed Fire Extinguishers.
Type nos
ABC (5 kg) : 35
CO2_ : 15
SAND BUCKET : 25
FOAM () : 30
FOAM TROLLY 45 Lit : 05
DCP : 20
TOTAL : 130
15
Additional Fire Extinguisher Required
: 20
16
Emergency Fire Exit provided to Each Floor? Ladder Provided to Each floor?
: YES
17
Arrangement for Fire warning. i.e. Hooter / Ele. Bell / Other
: YES
18
Water Sprinkler Provided? : YES
-
H-4 Details of Fire NOC/Certificate:
Unit will apply for fire NOC before getting CCA/NOC.
H-5 Details of Occupational Health Centre (OHC):
Occupational health impacts on the workers and mitigation measures proposed to avoid the human health hazards along with the personal protective equipment to be provided. Provision of industrial hygienist and monitoring of the occupational injury to workers as well as impact on the workers. Plan for periodic medical checkup of the workers exposed. Details of work place ambient air quality monitoring plan as per Gujarat Factories Rules. Expected Occupational Health Hazards & Safety
Physical Hazards: Noise, Heat, Dust Chemical Hazards: Corrosive (like Sulfuric acid), Toxic Substances (like Methanol &
Liquid Ammonia.). Psychological hazards resulting from stress and strain Hazards associated with the non-application of ergonomic principles, for
example badly designed machinery, mechanical devices and tools used by workers, improper seating and workstation design, or poorly designed work practices
Occupational Health effects of Chemicals primarily in the: Respiratory System: Lungs and Respiratory Track Brain – memory loss, confusion, difficulty concentrating, fatigue, headache Reproductive system – miscarriages, fetal alcohol syndrome Kidneys - Glomerulonephritis Skin – Irritant dermatitis, defatting Liver – Fatty liver, chemical hepatitis And Cardiovascular system – Increased sensitivity to epinephrine, exacerbation of coronary artery disease by CO due to methylene chloride, carbon disulfide.
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Mitigation Measures will be taken : - Proper PPE and sanitation facility will be provided - Washing Facility provided with adequate Lockers - Good Hygiene Measures will be adopted - Training will be imparted - Medical Surveillance program will be started.
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. Aqua Air Environmental Engineers Pvt. Ltd
remains present during video conference meeting.
Committee noted that the proposal is for new project in GIDC Saykha. PP submitted details regarding
area adequacy. Source of water is GIDC. Product profile along with end use discussed in depth. Looking
to layout plan, Committee insisted for submit revised layout plan with mentioning water sprinkler in raw
material storage area which is later on submitted by PP.
Committee noted that PP has submitted waste water management and industrial effluent will be
segregated. High COD stream will be treated in primary ETP-1 and treated effluent will be sent to CMEE
of M/s BEIL for evaporation. Low COD stream will be treated in ETP-2 consist of primary, secondary and
tertiary ETP units and treated effluent will be sent to CETP of GIDC Saykha for further treatment and
disposal. Domestic sewage will be treated in STP. Committee discussed regarding stage wise reduction
of BOD, COD and TDS in ETP. Committee insisted for submit revised water balance diagram with
mentioning reuse of waste water and PP later on submitted revised water balance diagram with
mentioning reuse of boiler condensate for cooling tower in water balance diagram.
PP submitted that they have proposed boiler and thermo pack. Fuel used will be briquettes of bio coal for
boiler and thermo pack. Two stage scrubbers will be provided as APCM with each process reactor stack.
PP submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.
Upon asking regarding provision of fire hydrant network and proposed fire extinguishers details, PP has
addressed the Site Plan/layout plan with provision of fire hydrant network, periphery road with entry and
exit separately, proposed fire extinguishers details adequate fire water reservoir and fire load calculation.
Committee noted that PP has addressed fire evacuation plan, worker‘s safety and occupational Health
centre (OHC) and process hazard and its safety control measures. Committee insisted for fire hydrant
cost, Cost of LDAR with DSC in Solvent Distillation and PP later on submitted revised EMP with
mentioning its cost. Committee noted that PP presented details of auto control system for critical hazard
process. PP presented Hazardous chemical storage area with its risk assessment.
Committee deliberated on storage and safety aspects of hazardous chemicals, green belt area, EMP,
CER, etc.
Committee found submission of project proponent satisfactory.
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After detailed discussion, Committee unanimously decided to recommend the project to SEIAA,
Gujarat for grant of Environment Clearance
SPECIFIC CONDITIONS:
1. PP shall comply conditions of any subsequent amendment or expansion or change in product mix,
after the 30th March 2021, considered as per the provisions in force at that time as mentioned in the
Notification vide S.O. 1223 (E) dated 27/03/2020 and S.O. 3636 (E) dated 15/10/2020.
2. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients (API) as
per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any subsequent
amendments.
3. PP shall submit six monthly compliance report of Environmental Clearance without fail and the same
shall be critically assessed by the regulatory authority.
4. Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB directions to all
SPCB vide letter no. B-29016/04/06PCI-1/5401 dated 05/02/2014 for effluent discharge and air
emission as per pollutants discharge/emission from respective project and an arrangement shall also
be done for reflecting the online monitoring results on the company's server, which can be
assessable by the GPCB/CPCB on real time basis. [For Small/Large/Medium (Red Category) &
Whichever (Air emission & Effluent discharge) is applicable].
5. Wastewater shall be fed to MEE only after providing adequate treatment in such a way that no
pollutant get air borne during evaporation to avoid adverse impact on Human Health & Environment.
6. Treated waste water shall be sent to CETP only after complying with the inlet norms of common
facilities prescribed by GPCB to ensure no adverse impact on Human Health and Environment.
7. The PP shall develop green belt within premises (10925.77 Sq. m i.e. 33 % of the total plot area) as
per the undertaking submitted before SEAC. Green belt shall be developed with native plant species
that are significant and used for the pollution abatement as per the CPCB guidelines. It shall be
implemented within 3 years of operation phase in consultation with GPCB.
8. Domestic wastewater generation shall not exceed 1.5 KL/day for proposed project and it shall be
treated in STP. Treated sewage shall be utilized for gardening and plantation purpose within
premises after achieving on-land discharge norms prescribed by the GPCB.
9. During monsoon season when treated sewage may not be required for the plantation / Gardening /
Green belt purpose, it shall be stored within premises. There shall be no discharge of waste water
outside the premises in any case.
10. (a) R & D products shall be of similar chemistry in line with the EIA Notification vide S.O. 1223 (E)
dated 27/03/2020 and the pollution load shall remain the same as committed. (b) Project proponent
shall not take continuous/commercial production of the R & D materials. Necessary approvals shall
be obtained from the concern authorities prior to commercial production of R & D materials. (c) Unit
shall submit relevant details of R & D products like raw materials, its safety measures to the
regulatory authority well before R & D activity. (d) Unit shall submit relevant details of R & D products
like different wastes generated (Quantity & Quality) and its management to the regulatory authority
within a month of R & D activity.
11. Close loop solvent recovery system with adequate condenser system shall be provided to recover
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solvent vapours in such a manner that recovery shall be maximum and recovered solvent shall be
reused in the process within premises.
12. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB
guidelines. LDAR Logbooks shall be maintained.
13. The unit shall submit the list of authorized end users of hazardous wastes along with MoU signed
with them at least two months in advance prior to the commencement of production. In the absence
of potential buyers of these items, the unit shall restrict the production of the respective items.
14. Unit shall obtain all required permissions from the Narcotics Control Bureau for manufacturing,
storage and handling of Acetic Anhydride & any such chemicals.
15. Safety and Health:
a) PP shall obtain PESO permission for the storage and handling of hazardous chemicals. (If
applicable)
b) PP shall provide Occupational Health Centre (OHC) as per the provisions under the Gujarat
Factories Rule 68-U.
c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the concern
authority as per the prevailing Rules / Gujarat Fire Prevention and Life Safety Measures Act,
2016.
d) Unit shall adopt functional operations/process automation system including emergency
response to eliminate risk associated with the hazardous processes.
e) PP shall carry out mock drill within the premises as per the prevailing guidelines of safety and
display proper evacuation plan in the manufacturing area in case of any emergency or
accident.
f) PP shall install adequate fire hydrant system within premises and separate storage of fire
water and foam for the same shall be ensured by PP. Also PP shall provide alarm system in
nearby fire station for emergency of any fire in plant area.
g) PP shall take all the necessary steps for control of storage hazards within premises ensuring
incompatibility of storage raw material and ensure the storage keeping safe distance as per
the prevailing guidelines of the concerned authority.
h) PP shall take all the necessary steps for human safety within premises to ensure that no any
harm is caused to any worker/employee or labor within premises.
i) Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.
j) Unit shall provide water sprinkler in Ammonia storage area.
k) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.
l) Unit shall store Bromine Bottle in cool dry separate area, out of direct sunlight.
m) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam
pouring system etc. to restrict cascade fire emergency in solvent tank farm.
n) Unit shall provide safety valve and rapture disc, as well as auto dump or auto quenches/,
suppresses system for nitration reaction vessel safety.
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5. SIA/GJ/IND2/166174/2020 M/s. Ambition Pharma
Survey No. 202/10, Golana Road, Village:
Sokhada, Ta: Khambhat, Dist: Anand
Appraisal
Category of the unit: 5(f)
Project status: New
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/166174/2020 on dated
29.09.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
This is a new unit proposes manufacturing of synthetic organic chemicals [API and API Intermediates] as
tabulated below,
Sr. No
Company Products
API Or Intermediate
CAs No Quantity
(MT/Month) End Use
1. Sucralfate API 54182-58-
0 25
Sucralfate is an anti-ulcer medication. Sucralfate is not greatly absorbed into the body through the digestive tract. It works mainly in the lining of the stomach by adhering to ulcer sites and protecting them from acids, enzymes, and bile salts. Sucralfate is used to treat an active duodenal ulcer.
2. Riboflavin Sodium
Phosphate API 130-40-5 10.50
Riboflavin sodiumphosphate is converted to flavin mononucleotide (FMN) and flavin adenine dinucleotide (FAD), which are required for red blood cell formation and respiration, antibody production
3. Ferrous
Ascorbate API
24808-52-4
16 Ferrous Acrobat is used in the treatment of anaemia. Anaemia cause to chronic kidney disease
Total 51.50
ENDUSE OF PRODUCTS
Sr. No.
Name of the
Product
CAS No. (Product)
Type/ Category of
Product (API/
Intermediate)
In case of Intermediate stage of API
Said API is used for/End Use of said API Stage of
Intermediate n-1, n-2, etc
Name of API in which
Intermediate Used/ End use of said
Intermediate
CAS No.
(API)
1. Sucralfate 54182-58-
0 API - - -
Sucralfate is an anti-ulcer medication. Sucralfate is
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not greatly absorbed into the body through the digestive tract. It works mainly in the lining of the stomach by adhering to ulcer sites and protecting them from acids, enzymes, and bile salts. Sucralfate is used to treat an active duodenal ulcer.
2.
Riboflavin Sodium
Phosphate 130-40-5 API - - -
Riboflavin phosphate sodium is converted to flavin mononucleotide (FMN) and flavin adenine dinucleotide (FAD), which are required for red blood cell formation and respiration, antibody production.
3. Ferrous
Ascorbate 24808-52-
4 API - - -
Ferrous Acrobat is used in the treatment of anaemia. Anaemia cause to chronic kidney disease
The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr. no.
Particulars Details
A
A-1
Total cost of Proposed Project (Rs. in Crores):
Total Project
2.0 Crores
Break-up of proposed project Cost:
Details Project Cost (Rs. In Crores)
Land 0.7
Building
Machinery 1.3
A-2
Details of Environmental Management Plan (EMP) As below:
Sr. No
Unit Installed Capacity (KLD)
Capital Cost (Rs.in Lacs )
Operating Cost (Lacs/ Month)
Maintenance Cost (Lacs/ Month)
Total Recurring Cost (Lacs/ Month)
1 Effluent Treatment
Installation of ETP and evaporator
10 0.7 0.1 0.8
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Plant
2. APCM
Provision of odour control system Provision of gas detectors
5 0.3 0.1 0.4
3. AWH Monitoring
To conduct EMS efficacy & environment monitoring
- 1.0 - 1.0
4. Green belt development
Development of Greenbelt Area
- 3.5 - 3.5
5. Fire
Provision of Safety Measures including Fire Detectors, Sensors, Alarm, Fire Hydrant, Fire Extinguishers, Lightening arrestors etc
12 2.0 0.50 2.50
6. Health & Safety
Provision of Occupational Health Centre with Antidotes
5 1.0 0.5 1.50
7. Other CER 4.0 - - -
PLC, SCADA 10 2.0 0.5 2.5
Total 46 10.5 1.7 12.2
Summary
Cost of Project in Crores per Annum: 2.0
EMP Capital Cost in Crores per Annum and Percentage:
0.44 (13 %)
EMP Recurring Cost in Crores per Annum and Percentage:
0.12
A-3
Details of CER as per OM dated 01/05/2018 (In case of project falls under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide 31.10.2019.)
% as per the OM Rs. in Lakh
2.0 4.0
Brief note on proposed activities
No. CER-Proposed Planned Activities Identified Villages
Year wise Budget (Lakhs)
1st Year
1
Contribution towards Installation of RO System (100 LPH) and other required materials to Primary School, and primary health center at Sokhda Village.
Sokhda Village 4.0
Total (Year Wise) 4.0
Grand Total 4.0 lac
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B Land / Plot ownership details:
B-1
Total Plot area ( sq. meter)
Total Plot area
5722 Sq. m.
B-2
Brief note on Area adequacy in line to proposed project activities:
Sr No.
Description of Area Area (sq. m)
1 Production 1200
2 Raw material Storage 150
3 Product Storage 150
4 Storage tank Area 150
5 Occupational Health Center 25
6 Utility 270
7 Effluent Treatment plant 60
8 Sewage Treatment Plant 30
9 Water Storage tank 30
10 Green Belt 1890
11 Road & Open 1767
TOTAL 5722
B-3
Green belt area
Total (Sq. meter)
Area in Sq. meter 1890
% of total area 33.0
C Employment generation
Total
40
D Water
D-1
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...) Bore well
Status of permission from the concern authority. The unit obtained CGWA NOC
D-2
Water consumption (KLD)
Sr No
Category Water Consumption KLD
Remark
1. Domestic Purpose 2.0
2. Other use(Gardening) 1.5 Reuse from STP
3.
INDUSTRIAL
DM plant 13.0 For Process DM Water plant Inside
Boiler 6.0
Washing 1.0 Reuse
Cooling 3.0 Reuse
Total water Consumption (Domestic)
2.0
Total water Consumption 23.0
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(Industrial )
Grand total(1+2+3) 26.50
Total Fresh 21.00
Total Reuse 5.50
D-3
Waste water generation (KLD)
Sr No
Category Waste Water
Generation KLD Remark
1. Domestic Purpose 1.5 Send to STP
2.
INDUSTRIAL
Process 7.0 In house Evaporate
DM Reject 3.4 Treated in separate ETP followed by RO. RO Permeate will be
utilized in Cooling and washing
Boiler 0.6
Washing 1.0
Cooling 0.3
Total wastewater Generation (Domestic)
1.50
Total wastewater generation (Industrial )
12.3
-
Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative):
Sr. No
Name of Product
KL per MT of Product KL Per Day
Waste Water Generation
Waste Water Generation
1. Sucralfate 3.5 3.5
2. Riboflavin Sodium Phosphate 5.0 2.1
3. Ferrous Ascorbate 2.2 1.4
TOTAL KLD 7.0
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (If any applicable to proposal).
D-4
Mode of Disposal & Final meeting point
Domestic: Domestic sewage 1.50 KLD generated will be reuse in Gardening After Treatment in STP Plant
Industrial: Total industrial 12.3 KLD Waste water generation from manufacturing Process and other ancillary Operation
The Wastewater from process 7.00 KLD will be treated in ETP -1 and evaporated along with RO Reject water from ETP 2
The stream other than process will be treated in ETP 2 followed RO and RO Permeate will be reuse in washing and cooling
- Clearly mention about final disposal In house Evaporation System
D-5
Treatment facilities
For Domestic waste water:
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Capacity of STP: 1.5 KLD
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed. ETP 1
ETP 2
ETP – 1
Sr. No. Name of Unit Capacity (KL)
1. Stripping tank 10.0
2. Effluent collection tank 10.0
3. Primary Settling tank 5.0
4. Holding tank-1 5.0
5. Pressure Sand Filter 1.0 m dia
6. Holding tank-2 5.0
7 Evaporator 1 KLPH
8. Sludge Drying Bed 1.5 m x 1.5 m, 4 Nos.
ETP – 2
Sr. No. Name of Unit Capacity (KL)
1. Effluent collection tank 6.00
2. Primary Settling tank 5.0
3. Holding tank-1 6.0
4. RO System 500 LPH
5. Holding tank-2 5.0
Sr No
Parameter
Unit Process Washing Boiler Cooling Combine
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1. pH pH Scale 4-5 7-8 7-8 7-8 4-5
2. T.D.S. mg/l 4000-5000 1500-2000 500-800 500-800 4000-5000
3. C.O.D mg/l 2000-4500 1200-1500 250-300 250-300 2000-4500
Sr No Parameter Unit ETP inlet After primary treatment
Evaporate
1. pH pH Scale 4-5 7-8 7-8
2. T.D.S. mg/l 4000-5000 5000-6000 5000-6000
3. C.O.D mg/l 2000-4500 1800-2000 1800-2000
Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
Total industrial 12.3 KLD Waste water generation from manufacturing Process and other ancillary Operation
The Wastewater from process 7.00 KLD will be treated in ETP -1 and evaporated along with RO Reject water from ETP 2
The stream other than process will be treated in ETP 2 followed RO and RO Permeate will be reuse in washing and cooling
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Total industrial 12.3 KLD Waste water generation from manufacturing Process and other
ancillary Operation
The Wastewater from process 7.00 KLD will be treated in ETP -1 and evaporated along with RO Reject water from ETP 2
The stream other than process will be treated in ETP 2 followed RO and RO Permeate will be reuse in washing and cooling
.
D-6
In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF
Not Applicable
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
Not Applicable
D-7
Simplified water balance diagram with reuse / recycle of waste water
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E Air
E-1
Brief Note on fuel based heat energy requirement and worst case scenario thereof:
E-2
Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)
-
Sr. no
Stack attached to
Stack height and dia
Fuel Quantity of
Fuel MT/Day
APCM Types of Emission
1 Steam boiler (1.5 TPH)
20.0 m
Briquettes or Agro waste
1 Cyclone Separator
PM SOx NOX
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2 HAG 5 lac Kcal/hr
20.0 m
Briquettes or Agro waste
4 Cyclone Separator
3 D.G Set (200 KVA)
5.0 m HSD 0.6 adequate stack Height
E-3
Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
-
Sr. No.
Stack Attached to Stack
Height (m) APCM
Parameter & Permissible
Limit
1 Spray Dryer for Product 500 LPH
15.0 Cyclone Separator+ Two
stage Water Scrubber PM
Note:
Details of gaseous raw materials used in proposed project Estimation of process gas emission (Product wise and Total) Requirement of the scrubbing media (KL per Day) considering solubility (Product wise and
Total) Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its sound
management in HW matrix.
E-4
Fugitive emission details with its mitigation measures: As below:
The entire manufacturing activities will be carried out in the closed reactors and regular checking and maintenance of reactors will be carried out to avoid any leakages.
The tank vents will be equipped with either a carbon filter or an oil trap to prevent water vapour from entering the tank as it breathes.
Control of all parameters on a continuous basis will be done by adequate control valves, pressure release valves and safety valves etc.
All the flange joints of the pipe lines will be covered with flange guards. All the raw materials will be stored in isolated storage area and containers tightly
closed. There will also be provision of adequate ventilation system in process plant and hazardous
chemical storage area
A regular preventive maintenance will be planned to replace or rectify all gaskets, joints etc.
The unit will also develop green belt within the factory premises to control the fugitive emission from spreading into surrounding environment.
F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.
Disposal to scrap vendors/vendors/traders is not allowed
F-1
Hazardous waste management matrix
Sr Types of Specific Category Propose Management of HW
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. No
Hazardous Waste
Source of generation (Name of the Activity, Product etc.)
and Schedule as per HW Rules.
MT/Year
1. ETP Sludge
ETP area 35.3 60
Collection, Storage, transportation and disposal at any registered TSDF site
2.
Process Wastes, sludge
Riboflavin Sodium Phosphate, Ferrous Ascorbate
21.1 250
Collection, Storage, Transportation, Disposal at Registered TSDF or Disposal by co-processing or Incineration
3. Used Oil Plant Machinery
5.1 0.050
Collection, Storage, Transportation, sell to MoEFCC approved recyclers OR Reused as Lubricant within premises
4.
Discarded Container/ Liner
Material Storage and Handling
33.3 1.0
Collection, storage, Transportation and Dispose to Registered Recycler
5. Solvent residue
Distillation Unit
26.3 36
Collection, Storage, Transportation and disposal by co processing or by disposal to CHWIF
6. Spent solvent
Riboflavin Sodium Phosphate, Ferrous Ascorbate
26.4 1200
Recovered, storage and reused in the next batch of same product after Distillation
7. Evaporation Residue
Evaporation
35.3 15.0
Collection, Storage, transportation and disposal at any registered TSDF site
-
F-2
Membership details of TSDF, CHWIF etc. (For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility. We will obtained after getting NOC from GPCB
F-3
Details of Non-Hazardous waste & its disposal (MSW and others)
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
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1 NIL NIL NIL NIL
G Solvent management, VOC emissions etc.
G-1
Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.
Sr. No
Name of Product Solvent Total Solvent Quantity
Recover of Solvent
Loss of Solvent
% of recovery
% of Losses
1.
Riboflavin Sodium Phosphate,
Methanol 6250 6100 313 97.6 2.4
2. Ferrous Ascorbate
Methanol 2310 2217 93 96.0 4.0
G-2
Brief Note on LDAR proposed:
The industry is engaged in the manufacturing of bulk drugs and fine chemical, which require solvents during various unit processes. The unit uses solvent which is
The spent solvent generated during the manufacturing process will be recovered by way of distillation and will be reused in the process. The process of the solvent recovery system is described hereunder;
After completion of the reaction, the whole mass in the reactor will be pumped to SS reactor which is subjected to the distillation to separate finished product and recover solvent.
Firstly, the mass will be distilled at required temperature and pressure where pure solvent will be distilled out depending on their boiling points and it will be collected in the recovered solvent storage tank and reused in the process.
Vacuum will also be applied as per requirement during distillation.
The overall requirements and mass balance for the solvent based on mass balance of each product and summary has been worked out which is given in Table as above. The schematic diagram of the solvent recovery system is shown in the Figure Measures for achieving maximum solvent recovery:
The entire manufacturing activities & distillation process will be carried out in totally closed system.
Regular maintenance of the pipeline and valves & fittings will be carried out regularly to avoid any leakages.
Distillation column will be connected with condenser where cooling water will be used as media and also equipped with vacuum system.
The condenser will be provided with the sufficient HTA and residence time to achieve more than 98% recovery.
During the manufacturing activity as well as during distillation process 2% of the total solvent will be lost; approx. 98 % of solvent will be recovered during the process. The fresh solvent requirement will depend on solvent loss during distillation as well as manufacturing activity.
G-3
VOC emission sources and its mitigation measures
Sources of fugitive emissions include storage of chemicals, solvents storage, loading and unloading section, raw material handling and, hazardous waste storage area
Measures: The fugitive emissions in terms of handling losses will get reduced by proper storage and
handling. Hazardous chemicals will be stored as per standard criteria. Periodically monitoring will be carried out as per the post project monitoring plan. Proper ventilation in storage & production area shall be ensured All materials must be stored in suitable packing to prevent contamination of air
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Enclosed system & efficient procedures for materials charging shall be ensured. Procedures for start-up shut down, operation & maintenance procedures shall be established &
maintained. The coverage of greenbelt around the plant also acts as natural barrier to stop carrying of dust
along with the wind current.
H Safety Detail
H-1
Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
Sr No
Name of Raw Material
State
Storage Capacity in KL
Number of Tank
Storage at time (KL)
IDLH ppm
Boiling Point °C
Flash Point °C
Dyke Wall height
Capacity of Dyke (KL)
Hazard characteristic
Fire extinguisher Type
1 Methanol
Liquid
15 1 15
6000
64.7
9 1.3 16.5 Flammable
CO2, Dry Chemical or Foam
2
Distilled Methanol
Liquid
5 1 5
6000
64.7
9 1.3 5.5 Flammable
CO2, Dry Chemical or Foam
3
Spent Methanol
Liquid
10 1 10
6000
64.7
9 1.3 11 Flammable
CO2, Dry Chemical or Foam
4 Suphuric Acid
Liquid
10 1 10 15
193 - 1.3 11 Corrosive
Sand Bucket
5 HCl Liquid
5 1 5 50
83 - 1.3 5.5 Corrosive
Sand Bucket
Brief note on storage of Hazardous chemicals in Tanks
Methanol
• Tank, valve, pipeline are checked and maintain, in good condition through preventive maintenance
• Joints are checked regularly to detect any Leakage. • ISI Portable fire extinguisher & Fire Hydrant line is provided as per TAC norms. • Flame proof electrical fittings / installation provided. • Proper Earthing, Bonding & flange-to-flange jump ring is provided. • Flame arrester provided on vent line. • CCE approved Separate Storage area with door having locking arrangement. • Auto & manual sprinkler provided. • Spark arrester are installed on all vehicles inside the premises. • Apron, Hand gloves, gumboot, goggles and helmet provided. • Train operator employed. • Eye washer & shower provided. • Tank‘s thickness measured on regular interval. • Good ventilation in the area. • Flame arrester with breather valve. • Perforated dip pipe in dyke wall will be provided to monitor & detect any leakage from
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tank. • Sump will be made under dyke to recover leakage material from dyke. • Tanks will be kept under RCC dyke. • Tanks will be kept under shed.
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
Ferrous Sulphate PhosphrousOxi chloride Riboflavin Gluconic Acid Soda ash
Safety details of Hazardous Chemicals:
Type of Hazardous Chemicals
Safety measures
Methanol • The charging of material will be carried out by PLC based SCADA System semi automization
• Tank, valve, pipeline are checked and maintain, in good condition through preventive maintenance
• Joints are checked regularly to detect any Leakage. • ISI Portable fire extinguisher & Fire Hydrant line is provided as per
TAC norms. • Flame proof electrical fittings / installation provided. • Proper Earthing, Bonding & flange-to-flange jump ring is provided. • Flame arrester provided on vent line. • CCE approved Separate Storage area with door having locking
arrangement. • Auto & manual sprinkler provided. • Spark arrester are installed on all vehicles inside the premises. • Apron, Hand gloves, gumboot, goggles and helmet provided. • Train operator employed. • Eye washer & shower provided. • Tank‘s thickness measured on regular interval. • Good ventilation in the area. • Flame arrester with breather valve. • Perforated dip pipe in dyke wall will be provided to monitor & detect
any leakage from tank. • Sump will be made under dyke to recover leakage material from
dyke. • Tanks will be kept under RCC dyke. • Tanks will be kept under shed.
Sulphuric Acid
• The Entire plant will be operated by PLC based SCADA System and semi atomization
• Store in cool, dry and well ventilated area in compliance with compatible chart
• Dyke wall with sufficient size is provided. • Tank, valve, pipeline are checked and maintain, in good condition. • Apron, Hand gloves, gumboot, goggles and helmet will be provided. • ISI Portable fire extinguisher & Hydrant line is provided as per TAC
norms. • Sufficient amount of sand/soil are kept to control any spillage. • Eye washer cum shower is provided near tank-farm area. • Level indicator provided.
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• Vent line dipped in dilute caustic will be provided. • RCC foundation will be provided. • The material transfer is only from pump and fixed line in receiver
tank with return valve to main tank
HCL • The charging of material will be carried out by PLC based SCADA System and semi automization.
• Dyke wall provided. • Dyke wall with sufficient size is provided. • Tank, valve, pipeline are checked and maintain, in good condition. • Apron, Hand gloves, gumboot, goggles and helmet will be provided. • ISI Portable fire extinguisher & Hydrant line is provided as per TAC
norms. • Sufficient amount of sand/soil are kept to control any spillage. • Eye washer cum shower is provided near tank-farm area. • Level indicator provided. • Vent line dipped in water will be provided. • RCC foundation will be provided. • Transfer material to another empty tank/ Vessel.
Applicability of PESO :
H-2
Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
Type of Process
Safety measures including Automation
NIL There is no nay hazardous Process involved
H-3
Details of Fire Load Calculation
Total Plot Area: 5722
Area utilized for plant activity: 1650
Area utilized for Hazardous Chemicals Storage: 150
Number of Floors: GF
Water requirement for firefighting in KL : 11.100 KL
Water storage tank provided for firefighting in KL: 200 KL
Details of Hydrant Pumps: 6.0 Inch Diameter fire hydrant line will be provided connected to Jockey Pump having 07 bar pressure with sprinkler system. The jockey pump is placed with the fire water tank having capacity of 200 KL.
Nearest Fire Station : Khambhat @5.12 KM
Applicability of Off Site Emergency Plan: Not Applicable
H-4
Details of Fire NOC/Certificate:
We will obtained after getting NOC from GPCB
H-5
Details of Occupational Health Centre (OHC):
Number of permanent Employee: 15
Number of Contractual person/Labour : 20
Area provided for OHC: 25 Sq. m
Number of First Aid Boxes : At least one box containing such items and placed and maintained in accordance with the requirements of Sec. 45 is separately provided.
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Nearest General Hospital : The Cambay General Hospital Khambhat@ 4.0 Km
Name of Antidotes to be store in plant : Injection -morphia, pethidins, atropins, adrenaline, coramine, novocan Fomepizole, Cobalt EDTA, Diazem, Epinephina, Efidrine, Ethanol, Milk of Magnesia epicake syrup, Sodium Hydro-Carbonate (4% Conc.), Milk, Lime Juice, Soda Water, Soframycine
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. Satva Environ Consultancy remains present
during video conference meeting.
This is a new proposal of API and Its Intermediates plant at Survey No. 202/10, Golana Road, Village:
Sokhada, Ta: Khambhat, Dist: Anand, located outside notified area. Source of water supply is Bore well.
Committee asked for status of CGWA permission for ground water source, PP informed that they have
apply for CGWA permission. Also PP has presented NA permission for proposed plot is for industrial
purpose. PP submitted Google map showing that there is no any water bodies, villages, School,
monuments etc. within 500 m radius of the project site. PP also submitted that there are no Eco sensitive
zones, wild life sanctuaries within the 10 km area from the boundary of the project site.
Product profile along with End Use discussed in depth. Committee noted that PP has addressed area
adequacy for proposed project with layout plan.
Committee noted that effluent stream segregation will be carried out. High COD effluent from Process
will be treated in primary treatment plant, ETP-1 and treated effluent will be evaporated in in-house
evaporator. Low COD stream will be treated in ETP-2 followed by RO plant. RO reject will be evaporated
in evaporator. Committee insisted for clarification regarding high COD and TDS stream evaporated in
evaporator is technically feasible with treatability report for ETP and evaporator and justification
regarding totally evaporation of effluent in evaporator with heat balance, technical expert of PP could not
addressed properly during meeting.
Committee noted that agro waste or briquette will be used as fuel for boiler and hot air generator.
Cyclone separator as APCM will be attached with boilers and thermo pack. Committee insisted for
technical clarification regarding proposal of cyclone separator as APCM for 1.5 TPH boiler and Hot air
generator and 1 TPD agro waste or briquette consumption as fuel for 1.5 TPH boiler. Cyclone separator
and water scrubber will be provided as APCM with spray dryer. Technical expert addressed hazardous
waste management including scrubber bleed liquor and spent solvent disposal.
Committee noted that PP has addressed LDAR and solvent recovery, green belt development, EMP and
CER for proposed project. PP explained regarding safety control measures for process hazard and
Hazardous chemical storage and its management. Committee discussed in length regarding fire hydrant
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system, evacuation plan, storage and safety measures of hazardous chemicals.
Since, the unit falls in B2 category as per the MoEF&CC‘s amended EIA Notification vide S.O. 1223(E)
dated 27.03.2020, the public consultation is not applicable as per paragraph 7(i) III (i) (e) of the
Environment Impact Assessment Notification-2006.
After detailed discussion, Committee unanimously decided to consider the project only after
submission of following documents,
1. Submit clarification regarding high COD and TDS stream evaporated in evaporator is technically
feasible with treatability report for ETP and evaporator and also justification regarding totally
evaporation of effluent in evaporator with heat balance.
2. Submit technical clarification regarding proposal of cyclone separator as APCM for 1.5 TPH boiler
and Hot air generator and 1 TPD agro waste or briquette consumption as fuel for 1.5 TPH Boiler.
6. SIA/GJ/IND2/166235/2020 M/s. Global Medicines Limited
Plot No. 5068, GIDC- Ankleshwar, Dist -
Bharuch
Appraisal
During SEAC VC meeting on dated 17.12.2020, Project Proponent and their technical expert remain
absent. PP has submitted letter via Email stating that they would remain absent during meeting. PP
also requested to schedule the project in any upcoming SEAC meeting.
Hence, Committee decided to defer this proposal and consider this in one of the upcoming SEAC
meeting.
7. SIA/GJ/IND2/173473/2020 M/s. Skanttr Life science LLP
Survey no.: 340 & 345, Amipura,
Ta. Bavla, Dist: Ahmedabad
Appraisal
Category of the unit: 5(f)
Project status: Expansion
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173473/2020 on dated
05.10.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
This is an existing unit and now proposes expansion in manufacturing of synthetic organic chemicals
[API and API Intermediates] as tabulated below,
Sr. no.
Name of the Products
API OR
INTERMEDIA
TE
CAS no.
Quantity MT/Month
End-use of the products * Exi
sting
Proposed
Total
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1 Itraconazole API 84625-
61-6
-
12.5
MT/M
20
MT/M
(Either/
or)
Anti-Fungal
2
Ketoconazol
e
API
65277-42-1
-
Anti-Fungal
3
Vardenatil API 224785-
90-4 -
Phosphodiesterase inhibitors
4
Miconazole
API
22916-47-8
- Anti-Fungal
5
Ticonazole
API
65899-73-2
- Anti-Fungal
6
Atorvastatin calcium
API 134523-
00-5 6
Cardiovascular
diseases
7
Candesartan API 139481-
59-7
Anti-Hypertensive
8
Carbidopa API 28860-95-9
1.5
used to treat symptoms of Parkinson's
disease, such as muscle stiffness, tremors, spasms
9
Losartan
Potassium
API 124750-
99-8 -
Anti-hypertensive/T
ablet
10 Hydroxychlor
oquine API
118-42-
3 4
-6.5
MT/M
20
MT/M
(Either/
or)
rheumatoid
arthritis
11 Rosuvastatin
e Calcium API
287714-41-4
1.5
To reduce your LDL (bad) cholesterol levels and
increase your HDL (good) cholesterol
levels
12 Montelukast
sodium API
158966-92-8
5
It is used to control and
prevent symptoms
caused by asthma (suc
h as wheezing and shortness of
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breath)
13 Luliconazole API 187164-
19-8 - Anti Fungal
14 Clotrimazole API 25593-75-1
- Anti Fungal
15 Sodium
valproate API
1069-66-5
-
Sodium valproate is used to treat epilepsy and
bipolar disorder.
16 Pantoprazole
Sodium API
138786-67-1
16
It is used to treat damage
from gastroesophag
eal reflux disease
17 Azilasartanm
edoxoil API
147403-03-0
- Anti-
Hypertensive
18 Telmisartan API 144701-
48-4 -
13.2
MT/M
20
MT/M
(Either/
or)
Anti
Hypertensive
19 Valsartan API 137862-
53-4 -
Anti Hypertensive
20 Ranolazine API 142387-
99-3 - Anti Anginal
21 Amlodipine Besylate
API 88150-42-9
6.8
used to treat high blood pressure (hype
rtension).
22 Valproic acid API 99-66-1 - Used to treat
migraine headache
23 Olmesartan API 144689-
63-4 -
Angiotensin receptor blockers
24 Abiraterone
Acetate API
154229-
19-3 -
-2.2
MT/M
10
MT/M
(Either/
or)
Anti-Cancer
25 Linezolid API 165800-
03-3 - Anti bacterials
26 Quetiapine Fumarate
API 111974-
69-7 -
anti-psychotic drug
27 Rivaroxaban API 366789-
02-8 - Anti coagulant
28 Glimepiride API 93479-97-1
10
Controlling high blood sugar
helps prevent kidney
damage, blindness,
nerve problems
29 Escitalopram
Oxalate API
219861-08-2
- Anti-
Depressant
30 Fexofenadin API 153439- 2.2 Fexofenadine i
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e hydrochlorid
e
40-8 s an antihistamin
e used to relieve allergy
symptoms such as
watery eyes, runny
nose, itching eyes/nose, sneezi
ng, hives,
31 Atenolol API 29122-
68-7 9.6
-7.9
MT/M
10
MT/M
(Either/
or)
Used to treat
high blood
pressure
32 Levosulporid
e API
23672-07-3
2.1
Levosulpiride is used in
the treatment of
Gastroesophageal reflux disease
33 Aripiprazole API 129722-
12-9 3.0
Used as an antipsychotic
drug
34 Olanzapine API 132539-
06-1 3.2
Used for the treatment of schizophrenia
35 Taurine API 107-35-
7 -
Use for high blood pressure,
high cholesterol
36 Levetiraceta
m API
102767-28-2
- Epilepsy
37 Bupivacaine API 38396-
39-3 -
4.8
MT/M
10
MT/M
(Either/
or)
Local-
Anesthetic
38 Lidocaine
HCl API
137-58-6
- Local-
Anesthetic
39 Febuxostat API 144060-
53-7 -
Xanthine Oxidase Inhibitors
40 Levamisole API 16595-80-5
- Anti fugal
41 Labetalol
hydrochloride
API 36894-69-6
3
Labetalol is used to treat hypertension (high blood pressure).
42 Lafutidine API 118288-
08-7 2.2
used to treat stomach acid-
related disorders such
as gastroduodenal
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ulcers
43 Clopidogrelbi
sulphate API
120202-
66-6 -
3.4
MT/M
5
MT/M
(Either/
or)
Anti-Platelet
44 Oseltamivir Phosphate
API 204255-
11-8 - Anti Viral
used for the treatment of
osteoarthritis, rheumatoid
arthritis, acute pain in adults, and primary
dysmenorrhea
45 Rofecoxib API 162011-
90-7 -
46 Ticagrelor API 274693-
27-5 - Anti Platelet
47 Methylcobala
min API
288315-09-3
0.1 used to treat
anemia, diabetes
48 Albuterol API 18559-94-9
1.5
Albuterol is used to prevent
and treat difficulty
breathing, wheezing,
shortness of breath, etc.
49 Etoricoxib API 202409-
33-4 -
Anti-Inflammation
50 Sertraline
hydrochloride
API 79617-96-2
- Anti-
Depressant
52 Favipiravir API 259793-
96-9 -
1.9
MT/M
5
MT/M
(Either/
or)
Anti-Viral
53 Silodosin API 160970-
54-7 - alpha blockers
54 Saxagliptin API 709031-
78-7 1 alpha blockers
55 Artemether API 71963-77-4
- Anti-Malerial
56 Artesunate API 88495-63-0
- Anti-Malerial
57 Abacavir Sulphate
API 216699-
07-9 2.1
This lower the chances of getting HIV
complications such as
infections, cancer
58 Dapagliflozin API 461432-
26-8 - -1.6
MT/M
5
MT/M
Anti-Diabetic
59 Empagliflozin API 864070- - Anti-Diabetic
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44-0 (Either/
or) 60 Paliperidone API 144598-
75-4 - Schizophrenia
61 Ursodeoxych
olic acid API
128-13-2
1.4 Used to treat a certain type of liver dieases
62 Folic acid API 59-30-3 3
Folic acid is used to treat deficiencies, which can
cause certain types
of anemia and other problems
63 Ciprofloxacin API 85721-33-1
-
used to treat serious infectio
ns, such as: chest infections
(including pneumonia)
skin and bone infections
.
64 Praziquantel API 55268-74-1
- anthelmintics
65 Ramipril API 87333-19-5
- Anti
Hypertensive
66 Lisinopril API 83915-83-7
- Anti
Hypertensive
67 Eszopiclone API 138729-
47-2 - Insomnia
68 Nebivolol API 99200-09-6
- Anti
Hypertensive
69 Ipratropium
Bromide API
7726-95-6
2.2
Ipratropium is used to control
and prevent symptoms
(wheezing and shortness of
breath) caused by
ongoing lung disease
70 Captopril API 62571-86-2
- Anti-
Hypertensive
R&D activity, pilot batches
0.5 0.5
Total
87.
4
MT/
M
18.1
MT/M
105.5
MT/M
ENDUSE OF PRODUCTS
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Sr. no.
Name of the Products
CAS no. Product
Type/Category
of Product (API/Intermedia
te)
In case of intermediate stage of API
End-use of the said API
Stage of
Intermediate n-1, n-2, etc
Name of API in which
Intermediate Used/ End use of said
Intermediate
CAS No.
(API)
1. Itraconazole 84625-61-6
API -
Anti-Fungal
2.
Ketoconazole
65277-42-1
API -
Anti-Fungal
3. Vardenatil 224785-90-4
API - Phosphodiesteras
e inhibitors
4. Miconazole
22916-47-8
API - Anti-Fungal
5. Ticonazole
65899-73-2
API - Anti-Fungal
6. Atorvastatin
calcium 134523-
00-5 API
Cardiovascular diseases
7. Candesartan 139481-
59-7 API Anti-Hypertensive
8. Carbidopa 28860-95-9
API
used to treat symptoms of Parkinson's
disease, such as muscle stiffness, tremors, spasms
9.
Losartan Potassium
124750-99-8
API Anti-
hypertensive/Tablet
10. Hydroxychlor
oquine 118-42-
3 API
rheumatoid arthritis
11. Rosuvastatin
e Calcium 287714-
41-4 API
To reduce your LDL (bad)
cholesterol levels and increase your
HDL (good) cholesterol levels
12. Montelukast
sodium 158966-
92-8 API
It is used to control and prevent
symptoms caused by asthma (such as wheezing and
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shortness of breath)
13. Luliconazole 187164-
19-8 API Anti Fungal
14. Clotrimazole 25593-75-1
API Anti Fungal
15. Sodium
valproate 1069-66-5
API
Sodium valproate is used to treat epilepsy and
bipolar disorder.
16. Pantoprazole
Sodium 138786-
67-1 API
It is used to treat damage from
gastroesophageal reflux disease
17. Azilasartanm
edoxoil 147403-
03-0 API Anti-Hypertensive
18. Telmisartan 144701-
48-4 API
Anti Hypertensive
19. Valsartan 137862-
53-4 API Anti Hypertensive
20. Ranolazine 142387-
99-3 API Anti Anginal
21. Amlodipine Besylate
88150-42-9
API
used to treat high blood
pressure (hypertension).
22. Valproic acid 99-66-1 API Used to treat
migraine headache
23. Olmesartan 144689-
63-4 API
Angiotensin receptor blockers
24. Abiraterone
Acetate 154229-
19-3 API
Anti-Cancer
25. Linezolid 165800-
03-3 API Anti bacterials
26. Quetiapine Fumarate
111974-69-7
API anti-psychotic drug
27. Rivaroxaban 366789-
02-8 API Anti coagulant
28. Glimepiride 93479-97-1
API
Controlling high blood sugar helps
prevent kidney damage,
blindness, nerve problems
29. Escitalopram
Oxalate 219861-
08-2 API Anti-Depressant
30.
Fexofenadine
hydrochloride
153439-40-8
API
Fexofenadine is an antihistamine u
sed to relieve allergy
symptoms such as watery eyes, runny nose, itching eyes/
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nose, sneezing, hives, and itching.
31. Atenolol
29122-68-7
API
Used to treat high blood pressure
32. Levosulporid
e 23672-07-3
API
Levosulpiride is used in
the treatment of Gastroesophageal
reflux disease
33. Aripiprazole 129722-
12-9 API
Used as an antipsychotic drug
34. Olanzapine 132539-
06-1 API
Used for the treatment of schizophrenia
35. Taurine 107-35-
7 API
Use for high blood pressure, high
cholesterol
36. Levetiraceta
m 102767-
28-2 API Epilepsy
37. Bupivacaine 38396-39-3
API
Local-Anesthetic
38. Lidocaine
HCl 137-58-
6 API Local-Anesthetic
39. Febuxostat 144060-
53-7 API
Xanthine Oxidase Inhibitors
40. Levamisole 16595-80-5
API Anti fugal
41.
Labetalol hydrochlorid
e
36894-69-6
API
Labetalol is used to treat
hypertension (high blood pressure).
42. Lafutidine 118288-
08-7 API
used to treat stomach acid-
related disorders such as
gastroduodenal ulcers
43. Clopidogrelbi
sulphate 120202-
66-6 API
Anti-Platelet
44. Oseltamivir Phosphate
204255-11-8
API Anti Viral
45. Rofecoxib 162011-
90-7 API
used for the treatment of
osteoarthritis, rheumatoid
arthritis, acute pain in adults, and
primary dysmenorrhea
46. Ticagrelor 274693-
27-5 API Anti Platelet
47. Methylcobala 288315- API used to treat
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min 09-3 anemia, diabetes
48. Albuterol 18559-94-9
API
Albuterol is used to prevent and treat difficulty
breathing, wheezing,
shortness of breath, coughing
etc.
49. Etoricoxib 202409-
33-4 API Anti-Inflammation
50.
Sertraline hydrochlorid
e
79617-96-2
API Anti-Depressant
51. Solifenacin succinate
242478-38-2
API Anti muscarinics
52. Favipiravir 259793-
96-9 API
Anti-Viral
53. Silodosin 160970-
54-7 API alpha blockers
54. Saxagliptin 709031-
78-7 API alpha blockers
55. Artemether 71963-77-4
API Anti-Malerial
56. Artesunate 88495-63-0
API Anti-Malerial
57. Abacavir Sulphate
216699-07-9
API
This lower the chances of getting HIV complications such as infections,
58. Dapagliflozin 461432-
26-8 API
Anti-Diabetic
59. Empagliflozin 864070-
44-0 API Anti-Diabetic
60. Paliperidone 144598-
75-4 API Schizophrenia
61. Ursodeoxych
olic acid 128-13-
2 API
Used to treat a certain type of liver
dieases
62. Folic acid 59-30-3 API
Folic acid is used to treat
deficiencies, which can cause certain
types of anemia and other problems
63. Ciprofloxacin 85721-33-1
API
It is used to treat bacterial
infections, such as:
chest infections (including
pneumonia) skin
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and bone infections.
64. Praziquantel 55268-74-1
API anthelmintics
65. Ramipril 87333-19-5
API Anti Hypertensive
66. Lisinopril 83915-83-7
API Anti Hypertensive
67. Eszopiclone 138729-
47-2 API Insomnia
68. Nebivolol 99200-09-6
API Anti Hypertensive
69. Ipratropium
Bromide 7726-95-6
API
Ipratropium is used to control
and prevent symptoms
(wheezing and shortness of
breath) caused by ongoing lung
disease (chronic obstructive pulmonary disease-
COPD which includes bronchitis and emphysema).
70. Captopril 62571-86-2
API Anti-Hypertensive
R&D activity, pilot batches
- -
- - - -
The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr. no. Particulars Details
A-1 Total cost of Proposed Project
(Rs. in Crores):
Existing
Proposed
Total
7.048 Crores 15 Crores 22.048 Crores
Break-up of proposed project Cost:
Details Existing
(Rs. In Crores)
Proposed
(Rs. In
Total
(Rs. In
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Crores) Crores)
Land 0.25 0 0.25
Building 1.75 5 6.75
Machinery 3 7.124 10.124
EMP 2.018 0.936 2.954
Miscellaneo
us 0.03 1.94 1.97
Total 7.048 15 22.048
A-2 Details of Environmental Management Plan (EMP) As below:
Pollution control equipment
Cost in Lac Recurring
Cost (Rs. In
Lac /Annum)
Remarks
Air Pollution
75 12
Capital cost would include air pollution
control devices and the recurring cost would
include operation and maintenance of
pollution control devices and stack
emission/AAQ monitoring & sample analysis
charges.
Water Pollution
134 30.4
Capital cost would include cost of ETP units
etc. and the recurring cost would include
maintenance charges, manpower salary,
sample analysis charges etc.
Noise pollution
0.15 0.36
Capital cost would include providing
adequate sound enclosures and recurring
cost would include monitoring of noise level.
Hazardous / solid waste
management
5.5 586.27
Capital cost would include expense for
providing storage area for hazardous waste
and for the membership of TSDF/CHWIF
site. Recurring cost would be for solid/
hazardous waste packing & its disposal &
analysis charges.
Green belt
5 1
Capital cost would include development of
green belt within and outside the project
premises and recurring cost would include
maintenance charges, manpower salary etc.
Occupational
Health & Safety
40.2 0.5
Capital cost would include cost of OHS
center, PPEs , SCADA and PLC and cost of
fire and safety equipment. Recurring cost
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would include maintenance charges.
Fire and Safety cost
17 0.25
Capital cost include the cost of jockey pump,
fire hydrant system, and all the equipments
required to control fire and keep the safety in
the workplace
Miscellaneous
2.5 3
Miscellaneous activity such as development
of rain water harvesting system and
recurring cost would include maintenance
charges
CER 15 -- Drinking facility, Paver block, Medical camp,
solar street provision
Total 294.35 633.68
Summary
Cost of Project in Crores per Annum: 15/-
EMP Capital Cost in Crores per Annum and
Percentage:
2.94/- and 19.6%
EMP Recurring Cost in Crores per Annum
and Percentage:
633.68/-
A-3 Details of CER as per OM dated 01/05/2018 (In case of project falls
under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs
given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of
Environmental Clearance as per the mechanism published vide
MoEF&CC‘s OM vide 31.10.2019.)
% as per the OM
Rs. in Crores
1% 0.15
Brief note on proposed activities:
Sr. No. Activity
Year (Amount to be spent in Lakhs)
Total amount to be spent in Lakhs 1st 2nd 3rd
Safe Drinking Water Facilities
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1
Ro facility (200 liter per hour) including annual maintenance contract for drinking water in Amipura Primary Schhol (1st year) and Dahegamda Primary school (2nd year) and maintenance of the RO facility in the (3rd year).
1.2 1.2 1 3.4
Infrastructure development & Healthcare Facilities
2
Paver block facility in nearest school Amipura Primary school (1st year) & Up gradation of Toilets and Water Tank in School (2nd year)
2 2 0 4
3 Medical camp in Amipura village and distribution of medicines to needy people.
-- -- 1.6 1.6
Renewable energy
4 Solar street light (12 W) in Amipura (1st year, 25 Units), Dahegamda village (2nd year, 25 Units)
3 3 - 6
Total 6.2 6.2 2.6 15
B Land / Plot ownership details: The Land documents attached with
Fom-1
B-1 Plot area
Existing
Proposed
Total
14485 Sq. m. 0 Sq. m. 14485 Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities: The plat
area of the project is 14485 sq. m. with green belt of 4823.6 sq.m. and the
detailed plant layout with the feasibility of the capacity of production is
attached in Annexure-2
B-3 Green belt area
Existing
Proposed
(Sq. meter)
Total
(Sq. meter)
Area in
Sq. meter 4767 m2 56.6 4823.6 m2
% of total 33% --. 33.3%
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area
C Employment generation
Existing
Proposed
Total
110 30 140
D WATER
D-1
Source of Water Supply
(GIDC, Bore well, Surface water, Tanker supply etc...)
Borewell
Status of permission from the concern authority.
Unit has already applied for CGWA and obtained the NOC approval for
existing unit & The unit has also applied for CGWA for proposed unit.
D-2 Water consumption (KLD)
Category
Existing KLD
Proposed (Additiona
l) KLD
Total after Expansion
KLD Remarks
( A) Domestic
5.5 2 7.5
(B) Gardening
16.5 0 16.5
(C) Industrial
RO
47 (35 KLD permeate + 12 KLD RO
reject.
RO permeate
will be used in boiler, DM plant
and cooling tower
30.5
72.5 (58 KLD permeate +
14.5 RO reject)
RO permeate will be used in
boiler and process
Boiler 2
24 26
Cooling
16.2 138.22 154.42
DM water 16.8 - -
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Process
13.7 18.3 32
Washing 2 2 4
Scrubber
1 5.6 6.6
Industrial Total
(C)
47 (out of
47 KLD, 35 KLD will be
recycled water so
fresh water requirement for industrial purpose will be 12 KLD
190.52
237.52 (Out 237.52 KLD,
59.67 KLD will be the recycled
water hence 177.85 KLD will
be the fresh water
requirement for industrial purpose.)
Total (A+B+C) 69 KLD 192.52 261.52 KLD
Recycled water 35 KLD 24.67 59.67 KLD
Fresh water requirement
34 KLD 167.85 201.85 KLD
Brief Note on worst case scenario for water consumption:
-
Summary of water requirement
Existing KLD
Proposed (Additional)
KLD
Total after Expansion
KLD
Remarks
Total water
requirement for the project (A)
69 KLD
192.52 KLD
261.52 KLD
Quantity to be recycled (B) 35 KLD
24.67 KLD
59.67 KLD
Total fresh water requirement (C) 34 KLD
167.85 KLD
201.85 KLD
Ensure Total water requirement = Fresh water + Recycled water
i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility.
[Source of reuse & application area]
Source of waste water for reuse in KLD (From
where it is coming)
Application area with
quantity in KLD (Where it
is used)
Characteristics of waste water to be
reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
RO permeate Total 59.67 KLD from RO will be used in
industrial purpose such
Particular Ro Permeate
Quantity 59.67s
pH 6.5-7.5
RO permeate
will be used in industrial
activities
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as washing, process and
allied equipments
TDS <500
COD <250
TSS <10
In case of no reuse/recycle of waste water, Give brief note on
justification as why no reuse/recycle.
D-3
Waste water generation (KLD)
Category
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(E) Domestic
4.5 1.85 6.35
(F) Industrial
RO rejected water 12 2.5 14.5
Process 18.3 3.83 22.13
Washing 2 2 4
Boiler 0.1 2.4 2.5
Cooling 1.6 13.82 15.42
Scrubber 1 3.78 4.78
Total Industrial
waste water
39.5
(Domest
ic:4.5KL
D &
Industria
l: 35
KLD)
30.18
(Domestic:
1.85 KLD &
Industrial:
28.33 KLD)
69.68
(Domestic :6.5
KLD and 63.1
KLD is
Indsutrial w/w.
Brief Note on worst case scenario for waste water generation (Qualitative and
Quantitative):
In worst case scenario maximum waste water from group A will be generated
during the production of the following
S.NO. Product Group Waste water generation (KL/day)
1 Ketoconazole A 5.1
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2 Pantoprazole Sodium B 1.6
3 Valproic Acid C 4
4 RIVAROXABAN D 3.9
5 Levetiracetam E 1.4
6 Levamisole F 0.9
7 Sertraline hcl G 3
8 Artesunate H 1.704
9 DAPAGLIFLOZIN I 0.5
Brief justification in case of no process effluent generation or no industrial
effluent generation or no high concentration effluent generation from proposed
project (Whichever is applicable).
Not applicable
D-4 Mode of Disposal & Final meeting point (Existing and Proposed)
Zero Liquid Discharge
Existing and Proposed
Domestic: Domestic waste water generated from existing and proposed unit will be
Treated in in-house ETP containing Primary, secondary and tertiary unit of
treatment
Industrial: Industrial waste water generated from existing and proposed unit will be
Treated in in-house ETP containing Primary, secondary and tertiary unit of
treatment
-
Clearly mention about final disposal: Zero Liquid Discahrge
D-5 Treatment facilities
Existing ETP units
Sr. No. Unit Size/
Capacity Quantity
1. Collection Tank -1 5.4 KL 2 Nos.
2. Ammonia Stripper 550 lit/hr 1 No.
3. Collection cum Neutralization tank-2
20 KL 2 Nos.
4. ETP 42 KLD 1 No.
5. RO 5000 lit/hr 1 No.
6. MEE/MVR 2000 lit/hr 1 No.
7. Centrifuge 1000 lit/hr 1 No.
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Details of Effluent treatment plant after expansion
Sr. No. Unit No. of units Size/ Capacity
1. Collection tank-1 2 5.4 KLD
2. Ammonia stripper 1 550 lit/hr
3. Collection cum
Neutralization tank - 1 2 20 KL
4. Solvent Stripper 1 3 m3/hr
5. Holding Tank 1 40 KLD
6. MEE 1 3 m3/hr
7. ATFD 1 1.5 m3/hr
8. Collection cum
Neutralization tank - 2 2 50 KLD
9. Primary Clarifloccutor 1 40 KLD
10. Aerobic Tank 1 40 KLD
11. Secondary Clariflocculator 1 40 KLD
12. PSF/ACF 1 4 m3/hr
13. RO-2 2 2 m3/hr
W/W generated from from industrial activities will be 68.82 KLD. The 22.13 KLD W/W stream containing Ammonical Nitrogen will be treated in ammonia
stripper and then it will be sent to ETP. 17.01 KLD high COD w/w from process, 2 KLD w/w from washings and 3.78 KLD w/w
from scrubber will be collected in collection cum neutralization tank then it will passed through solvent stripper and w/w coming from solvent stripper will be sent to MEE. Condensate water from MEE along with 11.75 KLD w/w rejected from RO, 2.4 KLD boiler blow-down and 13.82 KLD cooling tower blow down will be taken to ETP.
ETP will be consisting of collection cum neutralization tank, primary clariflocculator, aeration tank, secondary clariflocculator, PSF, ACF& RO.
Sludge generated from ETP and MEE salt will be sent to TSDF site Thus, unit will maintain Zero liquid discharged.
For Domestic waste water:
Capacity of STP/ Secondary treatment unit: 40 KLD
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each
stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP
(ETP-1, ETP-2….) for each stream shall be proposed.
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w/w
from
Scrub
ber
High
COD
strea
m
After
ammon
ia
stripper
Washi
ng
Composit
e
(Concentr
ated
Stream)
After
VOC
Stripp
er
RO
reject
Composi
te to
MEE
inlet
MEE
condensate
Quantity
(KLD) 4.78 17.01 5 4 30.79 30 15.5 45.5 36.4
pH 6.5-7.5 3.4-
4.5 4.5-5.5 6.5-7.5 4.46-5.51 6.5-7 6.5-7.5 6.5-7.17 6.5-7.5
TSS
(mg/l) 20-30
200-
250 200-250
200-
250
172.05-
215.84
120-
200 20-30 85-143 43-75
TDS
(mg/l)
1500-
2000
40000
-
45000
400000-
450000
200-
300
28852.54-
32517.37
25000
-
28000
5000-
5150
18200-
20220 900-1000
COD
(mg/l) 100-
200
50000
0-
60000
0
500000-
600000
400-
500
35800-
43000
29280
-
36510
10-20 19300-
24080 6700-8400
w/w from MEE
condensate
Dilute
stream
composi
te
Composite After
PST After SST
After
RO/perme
ate water
Quantity
(KLD) 36.4 38.7 75.1 12.6 12.6 8.8
pH 6.5-7.5 6.6-8.3 6.5-7.9 6.5-7.5 6.5-7.5 6.5-7.5
TSS
(mg/l) 43-75 100-190 70-130 30-40 10-20 <10
TDS
(mg/l) 900-1000
1920-
2390 1430-1720 1250-1440 450-470 <500
COD
(mg/l) 6700-8400 185-360 3370-4270 1000-1200 200-240 <250
Note: (In case of CETP discharge) :
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Management of waste water keeping in view direction under section 18 (1) (b) of
the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB
regarding compliance of CETP.
Not applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
W/W generated from from industrial activities will be 68.82 KLD. The 22.13 KLD W/W stream containing Ammonical Nitrogen will be treated in ammonia
stripper and then it will be sent to ETP. 17.01 KLD high COD w/w from process, 2 KLD w/w from washings and 3.78 KLD w/w
from scrubber will be collected in collection cum neutralization tank then it will passed through solvent stripper and w/w coming from solvent stripper will be sent to MEE. Condensate water from MEE along with 11.75 KLD w/w rejected from RO, 2.4 KLD boiler blow-down and 13.82 KLD cooling tower blow down will be taken to ETP.
ETP will be consisting of collection cum neutralization tank, primary clariflocculator, aeration tank, secondary clariflocculator, PSF, ACF& RO.
Sludge generated from ETP and MEE salt will be sent to TSDF site Thus, unit will maintain Zero liquid discharged.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer,
Common MEE, CHWIF etc.
Name of Common facility (CF) (For waste water treatment)
Project proponent already have TSDF Provisional certificate from BEIL
Membership of Common facility (CF) mentioning total capacity, consented
quantity, occupied capacity and spare capacity and norms of acceptance of
effluent from member units in-line with the direction given by GPCB vide Letter No.
GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
D-7 Simplified water balance diagram with reuse / recycle of waste water
(Existing and Proposed)
Existing:
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After expansion
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E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case
scenario there of:
Coal/Briquettes will be used for heat energy. The GCV of coal is 4500
kcal/hr.
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr,
MT/hr, KVA etc.
(In case of Project located within CPA/SPA , APCM shall be in line to the
mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)
Existing & Proposed
Flue gas emission from existing unit
Sr.
No.
Stack
attached to
Stack
Height
(m)
Fuel
Requirement APC System
Expected
Pollutant
1 Steam Boiler
(1*1 TPH) 30
Coal/Briquette
s
(1 MT/day)
Cyclone
separator
followed by
Bag collector
SPM: <150 mg/Nm3
SO2: <100 ppm
NOx: <50 ppm
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2 D.G.Set
(1*125 kVA) 6.5
HSD
(21 Lit/hr.)
Adequate
stack height
Sr.
No. Stack attached to Status
Stack
Height
Fuel
Requireme
nt
APC System
Expecte
d
Pollutant
1 Steam Boiler
(1*1 TPH) Existing 30 m
Coal/Briquet
tes
(1 MT/day)
Cyclone
separator
followed by
Bag collector
SPM
150
mg/Nm3
SO2
100 ppm
NO2 50
ppm
2 Steam Boiler
(2*4 TPH) Proposed
Common
Stack of
30 m
Coal/Briquet
tes
(15 MT/day)
Multi-cyclone
separator
followed by
bag filter
followed by
water scrubber
3
Thermic fluid
Heater
(2 nos.)
(1*1000000 Kcal/hr.
& 1*600000
Kcal/hr.)
Proposed
Common
Stack of
30 m
Coal/Briquet
tes
(2 MT/day)
Multi-cyclone
separator
followed by
bag filter
followed by
water scrubber
4
D.G.Set
(1*125 kVA)
(1*250 kVA)
(1*500 kVA)
Existing
&
Proposed
6.5 m
H.S.D.
(21 Lit/hr.)
(50 Lit/hr.)
(100 Lit/hr.)
Adequate stack
height
E-3 Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing
Sr. No.
Stack attached to
Height of the stack
APC System Expected Pollutant
1 Glimepiride 12 m Common duct to Caustic
scrubber Adequate
HCL
2 Carbidopa 12 m SO2
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3 Folic acid 12m stack height
H2S
After expansion
Sr.
No.
Stack
attached to
Height
of the
stack
APC System Expected
Pollutant
1
Reactor
vessel
(30 nos.)
12 m
Dual Condenser System on each
Reactor (water + Brine) followed by
dual stage Scrubber (Primary water
+ secondary alkali media) followed
by activated carbon column
HCL, VOCs
2
Reactor
vessel
(8 nos.)
12 m
Dual Condenser System on each
Reactor (water + Brine) followed by
dual stage Scrubber (Primary water
+ secondary acidic media) followed
by activated carbon column
NH3, VOCs
3
Reactor
vessel
(15 nos.) &
suction hood
to Bromine
handling area
12m
Dual Condenser System on each
Reactor (water + Brine) followed by
dual stage Scrubber (Primary
water + secondary alkali media)
followed by activated carbon
column
SO2,
Cl2, HBr, H2S,
VOCs
4
Reactor
vessel
(57 nos.)
12 m
Dual stage condenser system
(primary cooling water circulation
and second Brine chilled media
circulation) followed by the
Activated carbon column
VOCs
5 Dryer 12 m Activated carbon column VOCs
Note:
Details of gaseous raw materials used in proposed project : Yes, Bromine, chlorine,
hydrogen gas are going to be used as raw material
Estimation of process gas emission (Product wise and Total): There will be the
chances of emission of HCL, NH3, SO2, Br2, H2S, CL2
Requirement of the scrubbing media (KL per Day) considering solubility (Product
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wise and total): For Ammonia, media used in scrubber will be 670.4 l/day for HCl it will
be 1037 l/day, Cl2 it will be 2166.4, for SO2 it will be 514.4 l/day, H2S it will be 7.2 l/day,
Br2 it will be 1099.5 l/day. So total will be = 5.6 kl/day scrubbing media is required.
Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and
its sound management in HW matrix.
E-4 Fugitive emission details with its mitigation measures.
Sources of fugitive emissions include storage of chemicals, loading and
unloading section, raw material handling, hazardous waste storage area.
Mitigation Measures
Water shall be sprinkled during the construction.
Mechanical seals for pumps etc. should be used and maintained.
Closed unloading, conveying and packing system
All the reactors shall be closed.
Safety devices shall be provided to workers.
Raw material storage in closed storage area.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and
Transboundary Movement) Rules 2016.
Note:
Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9
permission, TSDF/CHWIH.
Quantification of hazardous waste shall be based on mass balance
and calculations shall be incorporated in EMP details separately.
Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Existing & Proposed
Sr. No.
Description Category
Existing
Proposed
Total Quantity (MT/Annum)
Mode of Disposal
1 ETP Sludge 35.3 252 42.17 294.17 Collection, storage, transport and disposal at approved TSDF site.
2 Process Residue / Process Sludge
28.1 - 829.7 829.7
Collection, Storage, Transportation (Through GPS mounted vehicles) and Disposal by sending to registered recycler for regeneration /for co-processing/ Incinerated
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at CHWIF.
3 Spent Carbon(process)
28.3 79.6 3400.2 3479.8
Collection, Storage, Transportation and Incinerated at CHWIF/ for co-processing
4 Distillation Residue
20.3 641.5 7269.54
7911.04
Collection, Storage, Transportation (Through GPS mounted vehicles) and Disposal by sending to registered recycler for regeneration /for co-processing/Incinerated at CHWIF.
5 Off Specification Drugs
28.4 5 1 6 Collection, Storage, Transportation and Incinerated at CHWIF.
6 Date Expired Product
28.5 48 1 49 Collection, Storage, Transportation and Incinerated at CHWIF.
7
Spent Solvent 28.6 22.6 27.4 50
Collection, Storage, Transportation and Incinerated at CHWIF/ for co-processing
Spent Solvent 28.6 - 67729.64
67729.64 Collected, Treated and Recover& Reuse in the next batch.
8 Spent Catalyst 28.2 215.3 215.3 Collection, Storage, Transportation and Incinerated at CHWIF.
9 Bleed liquor 35.1 - 302.13 302.13 Collection, Storage, Transportation and Incinerated at CHWIF.
10 Used Oil 5.1 0.1 3 3.1
Collection, storage and used within premises as a lubricant / sold to registered recycler.
11 Discarded Plastic Bags / Barrels / Liners
33.3 28.6 50 78.6 Collection, storage & sold to registered recycler.
12 Bleed Liquor 35.1 - 832.22 832.22 Collection and sent to ETP for further Treatment
-
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
Unit will apply for TSDF site membership
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Details of Membership letter no. & Date with spare capacity of the Common Facility.
The unit will send the w/w to common facility at the time of maintenance of ETP and
MEE and unit will apply for the same after getting EC.
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
Existing Proposed Total
1 Municipal solid waste
18 7.2 25.2 Treated in in-house ETP
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery,
reuse of recovered Solvents etc.
Sr. No.
Raw Materials Comsumpt
ion Mt/M Recovered
Mt/M % Recovery
1. Acetone 903 777 86.05
2. Acetonitrile 654.5 620.4 94.79
3. Benzene 9.4 8.4 89.36
4. Butanol 10 9.7 97.00
5. Chloroform 213.76 195.75 91.57
6. Cyclohexane 678.6 644.6 94.99
7. Dimehtyl Sulfoxide (DMSO)
217 201.8 93.00
8. Dimethyl
formamide (DMF)
116.1 112.1 96.55
9. Ethanol 246.5 222.2 90.14
10. Ethyl Acetate 3156.4 2861.1 90.64
11. Ethylene diamine
27 26 96.30
12. Heptane 15.2 14.89 97.96
13. Hexane 99.16 92.9 93.69
14. Isopropyl alcohal
735.8 690.46 93.84
15. Methyl Ethyl
ketone (MEK) 70.29 67.76 96.40
16. Methanol 2541.1 2416.11 95.08
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17. Methyl Isobutyl Ketone (MIBK)
150 142.51 95.01
18. Methylene dichloride
(MDC) 2489.21 2320.98 93.24
19. O-xylene 41.32 39.88 96.52
20. Pyridine 100.27 96.25 95.99
21. Tetra Hydro Furan (THF)
585.17 556.08 95.03
22. Toluene 1650.2 1502.5 91.05
23. Triethylamine 100 96 96.00
24. 1-4 dioxane 105 98.7 94.00
25. Acetic acid 93.9 86.1 91.69
26. Diethyl ether 80 76 95.00
The unit will provide solvent recovery system/distillation for the recovery of solvent. The solvent will be recovered and reused back in manufacturing process. The solvent will be recovered through distillation process. The distillation is a process where because of difference in boiling point solvent will be recovered.
G-2 Brief Note on LDAR proposed:
Components Average quantity
Average Uncontrolled
VOC Emissions (ton/year)
Percentage of total emission
Preventive Measures
Pumps 8 1.52 7.36
-Use Sealless design -Use Dual mechanical seal with barrier fluid maintained at a higher pressure than the pumped fluid -Provide Closed-vent system -Use Spare pumps at the time of repair. Tightening the packing glands. The pump will be flushed of VOC as much as possible before opening for seal replacement.
Valves 90 4.96 24.03
-Use Sealless design. -Plug type valves can be lubricated with grease to reduce emissions. Many valves have no means of in-service repair and must be isolated from the process.
Connectors 150 2.51 12.17
-Weld together -In some cases, leaks from flanges can be reduced by replacing the flange gaskets.
Open ended lines
90 1.45 7.00 -It can be controlled by using Blind, cap, plug, or second
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valve and flanges.
Sampling Connections
50 6.88 33.29 -Provide Closed-loop sampling
Pressure relief valves
60 3.33 16.14
-Provide Closed-vent system. -Installation of a rupture disk in the line prior to relief valve Connection of the discharge port of the relief valve to a closed vent system use of Soft seat technology such as elastomer "0-rings.
G-3 VOC emission sources and its mitigation measures
Unit has provided the dryer attached to reactors for controlling the VOC emission
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
Details of raw material storage and hazardous chemicals are included in risk
assessment report, which is attached with form-1.
Sr. no Name of Chemical Capacity of
Tank
Number of
Tanks
Hazardous
Characteristi
cs of
Chemical
1 - - - -
2 - - - -
3 - - - -
Brief note on storage of Hazardous chemicals in Tanks
Not applicable
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum,
Barrels, Carboys, Bags etc.
Details of raw material storage and hazardous chemicals are included in risk
assessment report which is attached with form-1
Safety details of Hazardous Chemicals: Detailed of hazardous chemicals and its
safety measures are included in risk assessment report which is attached with Fomr-1
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Type of
Hazardous
Chemicals
Safety measures
- -
- -
Applicability of PESO : Unit will obtain permission from PESO department After
getting EC
H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process,
Exothermic Reaction etc.)
-
Type of
Process
Safety measures including Automation
Nitration Fire / explosion occurred during the nitration process.
Control measures:
Nitration is exothermic reaction leads to runaway reaction. So, entire process of nitration is to be followed as per standard operating procedure established by industry.
All engineering controls w.r.t nitration process i.e. temperature and pressure controller, jacket surrounding to reactor etc. will be provided.
Chilled water to control exothermic reaction during nitration. NOx fumes will be scrubbed in ventury Scrubber from the Nitration
reactor. Only trained person will be allocated for handling nitration process. Programmable Logic Controller (PLC) based control plan will be
provided for Nitration. Direct Contact with skin and eyes will be avoided. Appropriate personal protective equipment‘s like Safety Gloves,
Goggles, shoes etc., will be provided to workers. Periodically inspection of scrubber system will be carried out
Bromination Toxic flames/ explosion occurred during the bromination process.
Control Measures:
Bromination is exothermic reaction leads to runaway reaction. So, entire
process of bromination is to be followed as per standard operating
procedure established by industry.
All engineering controls w.r.t bromination process i.e. temperature and
pressure controller, jacket surrounding to reactor etc. will be provided.
Chilled water to control exothermic reaction during bromination
Exothermic
reaction
Fire/Explosion
Control Measures:
Exothermic reaction leads to runaway reaction. So, entire process is to
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be followed as per standard operating procedure established by industry.
All engineering controls w.r.t exothermic reaction i.e. temperature and pressure controller, jacket surrounding to reactor etc. will be provided.
Chilled water circulation to control exothermic reaction. Only trained person will be allocated to operate. Programmable Logic Controller (PLC) based control plan will be
provided. Appropriate personal protective equipment‘s like Safety Gloves,
Goggles, shoes etc., will be provided to workers.
Hydrogenati
on
Improper handling of cylinders Control Measures: Separate hydrogenation plant will be provided to carryout hydrogenation
reaction.
Hydrogen gas will be transferred from cylinder to reactor through closed transfer system.
Hydrogenation process is exothermic reaction process so temperature and pressure will be maintained to control the rate of reaction.
All the precautions will be followed as per statutory guideline. SOP will be made available to handle hydrogenation process Adequate scrubbing system will be for Hydrogen gas Only trained person will be allow to access in hydrogenation plant. Appropriate PPEs will be provided for person working in hydrogenation
plant
H-3 Details of Fire Load Calculation
-
Total Plot Area: 14485 sq.m.
Area utilized for plant activity: 17958.00 sq.m.
Area utilized for Hazardous Chemicals
Storage:
1797.00 sq.m.
Number of Floors: There will be ground floor and 1st,2nd floor and terrace will be provided.
Water requirement for firefighting in KLD :
49.5125 KLD
Water storage tank provided for firefighting
in KLD:
170 KL
Details of Hydrant Pumps: Yes, 2 electrical pump (180 lit/min) and 1 diseal pump (2280 lit/min) at 7 kg /cm2 pressure. Yes , one trailer Pump
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of 1600 lit/Min at 7 Kg/cm2 pressure.
Nearest Fire Station : Bavla & Prahladnagar Fire Station disctance from project site is 13 Km & 38 km respectively
Applicability of Off Site Emergency Plan: Shown in Risk Hazards report.
-
H-4 Details of Fire NOC/Certificate: Unit will apply after getting EC
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 140
Number of Contractual person/Labour : 30
Area provided for OHC: 15 m2
Number of First Aid Boxes : 10
Nearest General Hospital : Parekh hospital
bavla is 13 Km
away from project
site
Name of Antidotes to be store in plant : 10
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. T.R. Associates remains present during video
conference meeting.
This is an existing unit and now proposes expansion for API and Its Intermediates plant at Vill- Amipura,
Ta- Bavla, Dist- Ahmedabad, located outside notified area. Source of water supply is Bore well.
Committee asked for status of CGWA permission for ground water source, PP informed that they will
apply for CGWA permission. PP submitted Google map showing that there is no any water bodies,
villages, School, monuments etc. within 500 m radius of the project site. There are no Eco sensitive
zones, wild life sanctuaries within the 10 km area from the boundary of the project site.
Product profile along with End Use discussed in depth. Committee noted that PP has addressed area
adequacy for proposed project with layout plan. PP has submitted EC and its self compliance report and
informed that they have still not started plant and not converted existing EC in CTO order.
Committee noted that effluent stream segregation will be carried out. High COD effluent from Process
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will be treated in primary treatment plant, ETP-1 followed by solvent stripper and Ammonia stripper.
Treated effluent will be evaporated in in-house MEE. Low COD stream will be treated in ETP-2 followed
by RO plant. RO reject will be evaporated in in-house MEE. MEE condensate and RO permeate will be
reused back in process.
Committee noted that coal and briquette will be used as fuel for boilers and thermo pack. Multi Cyclone,
bag filter and water scrubber as APCM will be attached with boilers and thermo pack separately. Two
stage scrubbers will be provided as APCM with each process stacks. Technical expert addressed
hazardous waste management including scrubber bleed liquor and spent solvent disposal.
Committee noted that PP has addressed LDAR and solvent recovery, green belt development, EMP and
CER for proposed project. PP explained regarding safety control measures for process hazard and
Hazardous chemical storage and its management. Committee discussed in length regarding fire hydrant
system, evacuation plan, storage and safety measures of hazardous chemicals and Risk assessment for
Hazardous chemicals considering worst case scenario.
Since, the unit falls in B2 category as per the MoEF&CC‘s amended EIA Notification vide S.O. 1223(E)
dated 27.03.2020, the public consultation is not applicable as per paragraph 7(i) III (i) (e) of the
Environment Impact Assessment Notification-2006.
Committee found that presentation and documents submitted by Project Proponent satisfactory.
After detailed discussion, Committee unanimously decided to recommend the project to SEIAA,
Gujarat for grant of Environment Clearance with the following specific condition.
SPECIFIC CONDITIONS:
1) PP shall comply conditions of any subsequent amendment or expansion or change in product
mix, after the 30th March 2021, considered as per the provisions in force at that time as
mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020 and S.O. 3636 (E) dated
15/10/2020.
2) PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients
(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any
subsequent amendments.
3) PP shall submit six monthly compliance report of Environmental Clearance without fail and the
same shall be critically assessed by the regulatory authority.
4) Wastewater shall be fed to in-house MEE only after providing adequate treatment in such a way
that no pollutant get air borne during evaporation to avoid adverse impact on Human Health &
Environment.
5) Unit shall obtain all required permissions from the Narcotics Control Bureau for manufacturing,
storage and handling of Acetic Anhydride & any such chemicals.
6) Close loop solvent recovery system with adequate condenser system shall be provided to recover
solvent vapours in such a manner that recovery shall be maximum and recovered solvent shall be
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reused in the process within premises.
7) Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB
guidelines. LDAR Logbooks shall be maintained.
8) PP shall maintain Complete Zero Liquid Discharge [ZLD] status all the time and there shall be no
drainage connection from the premises and no wastewater discharge outside premises by any
means.
9) (a) R & D products shall be of similar chemistry in line with the EIA Notification vide S.O. 1223 (E)
dated 27/03/2020 and the pollution load shall remain the same as committed. (b) Project
proponent shall not take continuous/commercial production of the R & D materials. Necessary
approvals shall be obtained from the concern authorities prior to commercial production of R & D
materials. (c) Unit shall submit relevant details of R & D products like raw materials, its safety
measures to the regulatory authority well before R & D activity. (d) Unit shall submit relevant
details of R & D products like different wastes generated (Quantity & Quality) and its management
to the regulatory authority within a month of R & D activity.
10) The unit shall submit the list of authorized end users of hazardous wastes along with MoU signed
with them at least two months in advance prior to the commencement of production. In the
absence of potential buyers of these items, the unit shall restrict the production of the respective
items.
11) Unit shall strictly Compliance of ODS (Ozone Depleting Substances) Rules 2000 and its
amendments time to time for use of ODS chemicals as raw material in proposed project.
12) PP shall obtain CGWA permission for ground water source i.e. bore well within premises before
start production activity.
13) Domestic wastewater generation shall not exceed 6.35 KL/day for proposed project and it shall
be treated in ETP. It shall not be disposed off in soak pit and septic tank.
14) Unit shall provide buffer water storage tank of adequate capacity for storage of treated waste
water in case of any shut down of MEE.
15) Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB directions to all
SPCB vide letter no. B-29016/04/06PCI-1/5401 dated 05/02/2014 for effluent discharge and air
emission as per pollutants discharge/emission from respective project and an arrangement shall
also be done for reflecting the online monitoring results on the company's server, which can be
assessable by the GPCB/CPCB on real time basis. [For Small/Large/Medium (Red Category) &
Whichever (Air emission & Effluent discharge) is applicable].
16) The PP shall develop green belt within premises (4823.6 m2 i.e. 33 % of the total plot area) as per
the undertaking submitted before SEAC. Green belt shall be developed with native plant species
that are significant and used for the pollution abatement as per the CPCB guidelines. It shall be
implemented within 3 years of operation phase in consultation with GPCB.
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17) Safety & Health:
a) PP shall provide Occupational Health Centre (OHC) as per the provisions under the Gujarat
Factories Rule 68-U.
b) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the concern
authority as per the prevailing Rules / Gujarat Fire Prevention and Life Safety Measures Act,
2016.
c) Unit shall adopt functional operations/process automation system including emergency
response to eliminate risk associated with the hazardous processes.
d) PP shall carry out mock drill within the premises as per the prevailing guidelines of safety and
display proper evacuation plan in the manufacturing area in case of any emergency or
accident.
e) PP shall obtain PESO permission for the storage and handling of hazardous chemicals. (If
applicable)
f) Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.
g) PP shall install adequate fire hydrant system within premises and separate storage of water
for the same shall be ensured by PP.
h) PP shall take all the necessary steps for control of storage hazards within premises ensuring
incompatibility of storage raw material and ensure the storage keeping safe distance as per
the prevailing guidelines of the concerned authority.
i) PP shall take all the necessary steps for human safety within premises to ensure that no any
harm is caused to any worker/employee or labor within premises.
j) Unit shall store Bromine Bottle in cool dry separate area, out of direct sunlight.
k) Unit shall provide water sprinkler to the ammonia storage drum/barrel.
l) Unit shall provide safety valve and rupture disc with hydrogenation reactors.
m) Unit shall provide safety valve and rapture disc, as well as auto dump or auto quench/,
suppress system for nitration vessel and exothermic reaction vessel safety.
n) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam
pouring system etc. to restrict cascade fire emergency in solvent tank farm.
8. SIA/GJ/IND2/173537/2020 M/s. Adarsh Dye Chem (Unit-II)
Plot No. A-1/3621 & 3620, Opp. ETL, GIDC
Estate Ankleshwar, Dist.: Bharuch
Appraisal
Project proponent (PP) submitted application by proposal no- SIA/GJ/IND2/173537/2020 for obtaining
Environmental Clearance.
Project proponent (PP) has e-mail, requesting for withdrawal of Environmental Clearance application
vide e-mail on dated 14/12/2020.
Proposal was considered in the SEAC meeting dated 17/12/2020.
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During SEAC meeting dated 17/12/2020, Committee noted that PP stated reason for withdraw the
Environmental Clearance application for the proposed project.
PP submitted that, they have changed mode of disposal from In house ZLD to NCTL for CETP discharge
in this expansion proposal. However, they have not yet received booked effluent load certificate.
In view of the above, Committee decided to recommend to permit project proponent for
withdrawal of their application of Environmental Clearance and to delist the proposal from the list
of pending applications & to close the file.
9. SIA/GJ/IND2/173557/2020 M/s. Zeni Healthcare
Plot No. C-349, GIDC- Saykha, Ta:Vagara,
Dist.: Bharuch
Appraisal
Category of the unit: 5(f)
Project status: New
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173557/2020 on dated
05.10.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
This is a new unit proposes manufacturing of synthetic organic chemicals [API and API Intermediates] as
tabulated below,
Sr. No.
Name of the Products
API OR INTERMEDIATE
CAS no. Quantity
MT/Month *End-use of products
1.
Alpha Ketoanalogue to Isoleucine Calcium Salt
API 51828-96-7
150 MT/MONTH
API / Nutritional Supplement for kidney disease
2.
Alpha Ketoanalogue
to Leucine Calcium Salt
API 51828-95-6
3.
Alpha Ketoanalogue
to Phenylalanine Calcium Salt
API 51828-93-4
4.
Alpha Ketoanalogue
to Valine Calcium Salt
API 51828-94-5
5.
Alpha Hydroxy Methionine
Calcium Salt API 4857-44-7
6. Iron Sucrose API 8047-67-4 API / Increase Haemoglobin
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7. Diacerein API 13739-02-1 API /used to
treat joint diseases
8. Tolfenamic
Acid API 13710-19-5 API / Chronic Pain
9. Diosmin API 520-27-4 API / Varicose Veins
10.
1,2,4 Triazolo [4,3-A] Pyridin-3-One (T.P.O)
Intermediate 6969-71-7 Trazodone HCl/
treat CNS
11. Ferric Carboxy
Maltose API 9007-72-1
API/ Increase Haemoglobin
12. Sucroferric
Oxyhydroxide API 12134-57-5
API/ Increase Haemoglobin
13. Couple Amine Hydrochloride
Intermediate 141109-19-
5
Clopidogrel Bisulphate/preventin
g strokes 14. Azithromycin API 83905-01-5
API/Respiratory System
15. Clarithromycin API 81103-11-9
16.
Erythromycin Ethyl-
Succinate API 1264-62-6
17. Erythomycin
Stearate API 643-22-1
18. Roxithromycin API 80214-83-1
19. Ciprofloxacin Hydrochloride
API 86393-32-0
API/Infection of Lungs 20. Levofloxacin API
100986-85-4
21. Ofloxacin API 82419-36-1
22.
Alpha Ketoanalog to
Isoleucine Magnesium
Salt
API 1560-54-9
API/ Nutritional Supplement for kidney disease
23.
Alpha Ketoanalog to
Leucine Magnesium
Salt
API 816-66-0
24.
Alpha Ketoanalog to
Methionine Magnesium
Salt
API 59-51-8
25.
Alpha Ketoanalog to Phenylalaine Magnesium
Salt
API 150-30-1
26.
Alpha Ketoanalog to
Valine Magnesium
Salt
API 516-06-3
27. Ketoconazole API 65277-42-1 API/skin infection
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28. Quetiapine
Hemifumarate API
111974-72-2
API/schizophrenia
29. 2-(Phenylthio) benenamine
Intermediate 1134-94-7
Quetiapine Hemifumarate/ schizophrenia
30.
Phenyl 2-(Phenylthio)
phenylcarbamate
Intermediate 111974-73-
3
31.
Dibenzo[b,f][1,4] thiazepine-11-(10H)one
Intermediate 3159-07-7
32.
1,1-piperazinyl-dibenzo[b,f]
[1,4] thiazepine
Intermediate 111974-74-
4
33. Acyclovir API 59277-89-3 API/cold Sores
34.
Diacetylacyclovir(9-[(2-
Acetoxyethoxy)methyl] -N2-acetylguanine
Intermediate 59278-00-1 Acyclovir/Cold sores
35. Telmisartan API 144701-48-
4
API/treat high blood pressure strokes, Kidney problem
36.
Methyl 4 bromomethyl biphenyl-2-carboxylate
Intermediate 114772-38-
2
Telmisartan/ treat high blood pressure
strokes, Kidney problem
37. Telmisartan Methyl Ester
Intermediate 528560-93-
2
38. Sulindac API 38194-50-2 API/treat high blood pressure strokes, Kidney problem
39.
3.-(4-Floro Phenyl) 2-
Methyl Propionic Acid
Intermediate 22138-73-4
Sulindac /treat high blood pressure strokes, Kidney
problem
40.
6-Flouro-2-Methyl 2-3-dihydro-1H-indon-1-one
Intermediate 37794-19-7
41.
5-fluro-2-methylindene-
3-Acid Intermediate 399-72-4
42. Sulindac Acid Intermediate 38194-50-2
43. Irbesartan API 138402-11-
6
API/treat high blood pressure strokes, Kidney problem
44.
4‘-Bromomethyl-
2-Cyanobiphenyl
Intermediate 114772-54-
2 Irbesartan/ treat
high blood pressure strokes, Kidney
problem 45.
4‘((2-Butyl-4-Oxo-1,3-
Intermediate 138401-24-
8
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diazaspirol[4,4]non-1-en-3-yl)methyl)-
[1,1‘-biphenyl]-2-carbonitrile
46. Irbesartan
Crude Intermediate
138402-11-6
47. Valacyclovir
Hydrochloride API
124832-27-5
API/cold sores
48.
N-[(benzayloxy)c
arbonyl]-L-valine-2-[2-amino-1,6-
dihydro-6-oxo-9H-purin-9-yl) methoxy] ethyl
ester
Intermediate 124832-31-
1 Valacyclovir
Hydrochloride/cold sores
49. Valacyclovir
acid Intermediate
124832-26-4
50.
6-Amino-2,4-dihydroxy-5-
nitrosopyrimidine
Intermediate 5442-24-0 Uracil/synthesis of
enzymes in the body
51. Phenyl
Acetonitrile Intermediate 83552-81-2
Peniciline G/ Antibiotic
52. Phenyl Acetic
Acid API 103-82-2 API/Antibiotic
53.
Tetra Butyl Ammonium
Bromide API 1643-19-2
API/Levitrasetam Phase transfer
catalyst
54. Tramadol
Hydrochloride API 27203-92-5 API /Painkiller
*R&D 100 Kg/Month
TOTAL 150 MT/Month
ENDUSE OF PROPOPOSED PRODUCTS
Sr. No.
Name of the Product CAS No. (Product)
Type/ Category of Product (API/ Intermediate)
In case of Intermediate stage of API
Said API is used for/End Use of said API
Stage i.e. n-1, n-2, etc.
Name of API in which Intermediate Used/ End use of said Intermedi
CAS no. (API)
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ate
1. Alpha Ketoanalogue
to Isoleucine Calcium Salt
51828-96-7
API - - - API / Nutritional
Supplement for kidney disease
2. Alpha Ketoanalogue to Leucine Calcium
Salt
51828-95-6
API - - - API / Nutritional
Supplement for kidney disease
3. Alpha Ketoanalogue
to Phenylalanine Calcium Salt
51828-93-4
API - - - API / Nutritional
Supplement for kidney disease
4. Alpha Ketoanalogue
to Valine Calcium Salt 51828-94-5
API - - - API / Nutritional
Supplement for kidney disease
5. Alpha Hydroxy
Methionine Calcium Salt
4857-44-7
API - - - API / Nutritional
Supplement for kidney disease
6. Iron Sucrose 8047-67-
4 API - - -
API / Increase Haemoglobin
7. Diacerein 13739-02-1
API - - - API /used to treat joint
diseases
8. Tolfenamic Acid 13710-19-5
API - - - API / Chronic Pain
9. Diosmin 520-27-4 API - - - API / Varicose Veins
10. 1,2,4 Triazolo [4,3-A] Pyridin-3-One (T.P.O)
6969-71-7
Intermediate of API
n-1 Trazodon
e HCl 25332-39-2
Trazodone HCl/ treat CNS
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11. Ferric Carboxy
Maltose 9007-72-
1 API - - -
API/ Increase Haemoglobin
12. Sucroferric
Oxyhydroxide 12134-57-5
API - - - API/ Increase Haemoglobin
13. Couple Amine Hydrochloride
141109-19-5
Intermediate of API
n-1
Clopidogrel
Bisulphate
120202-66-6
Clopidogrel Bisulphate/preventing
strokes
14. Azithromycin 83905-01-5
API - - - API/Respiratory System
15. Clarithromycin 81103-11-9
API - - - API/Respiratory System
16. Erythromycin Ethyl-
Succinate 1264-62-
6 API - - - API/Respiratory System
17. Erythomycin Stearate 643-22-1 API - - - API/Respiratory System
18. Roxithromycin 80214-83-1
API - - - API/Respiratory System
19. Ciprofloxacin Hydrochloride
86393-32-0
API API/Infection of Lungs
20. Levofloxacin 100986-
85-4 API - - - API/Infection of Lungs
21. Ofloxacin 82419-36-1
API - - - API/Infection of Lungs
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22. Alpha Ketoanalog to
Isoleucine Magnesium Salt
1560-54-9
API - - - API/ Nutritional
Supplement for kidney disease
23. Alpha Ketoanalog to Leucine Magnesium
Salt 816-66-0 API - - -
API/ Nutritional Supplement for kidney
disease
24. Alpha Ketoanalog to
Methionine Magnesium Salt
59-51-8 API - - - API/ Nutritional
Supplement for kidney disease
25. Alpha Ketoanalog to
Phenylalaine Magnesium Salt
150-30-1 API - - - API/ Nutritional
Supplement for kidney disease
26. Alpha Ketoanalog to Valine Magnesium
Salt 516-06-3 API - - -
API/ Nutritional Supplement for kidney
disease
27. Ketoconazole 65277-42-1
API - - - API/skin infection
28. Quetiapine
Hemifumarate 111974-
72-2 API - - - API/schizophrenia
29. 2-(Phenylthio) benenamine
1134-94-7
Intermediate of API
n-4
Quetiapine
Hemifumarate
111974-72-2
Quetiapine Hemifumarate/ schizophrenia
30. Phenyl 2-(Phenylthio)
phenylcarbamate 111974-
73-3 Intermediate
of API n-3
Quetiapine
Hemifumarate
111974-72-2
Quetiapine Hemifumarate/ schizophrenia
31. Dibenzo[b,f][1,4] thiazepine-11-
(10H)one
3159-07-7
Intermediate of API
n-2
Quetiapine
Hemifumarate
111974-72-2
Quetiapine Hemifumarate/ schizophrenia
32. 1,1-piperazinyl-
dibenzo[b,f] [1,4] thiazepine
111974-74-4
Intermediate of API
n-1
Quetiapine
Hemifumarate
111974-72-2
Quetiapine Hemifumarate/ schizophrenia
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33. Acyclovir 59277-89-3
API - - - API/cold Sores
34.
Diacetylacyclovir(9-[(2-
Acetoxyethoxy)methyl] -N2-acetylguanine
59278-00-1
Intermediate of API
n-1 Acyclovir 59277-89-3
Acyclovir/Cold sores
35. Telmisartan 144701-
48-4 API - - -
API/treat high blood pressure strokes, Kidney
problem
36.
Methyl 4 bromomethyl biphenyl-2-carboxylate
114772-38-2
Intermediate of API
n-2 Telmisart
an 144701-48-4
Telmisartan/ treat high blood pressure strokes,
Kidney problem
37. Telmisartan Methyl
Ester 528560-
93-2 Intermediate
of API n-1
Telmisartan
144701-48-4
Telmisartan/ treat high blood pressure strokes,
Kidney problem
38. Sulindac 38194-50-2
API - - - API/treat high blood
pressure strokes, Kidney problem
39. 3-(4-Floro Phenyl) 2-Methyl Propionic Acid
22138-73-4
Intermediate of API
n-4 Sulindac 38194-50-2
Sulindac /treat high blood pressure strokes,
Kidney problem
40. 6-Flouro-2-Methyl 2-
3-dihydro-1H-indon-1-one
37794-19-7
Intermediate of API
n-3 Sulindac 38194-50-2
Sulindac /treat high blood pressure strokes,
Kidney problem
41. 5-fluro-2-
methylindene-3-Acid 399-72-4
Intermediate of API
n-2 Sulindac 38194-50-2
Sulindac /treat high blood pressure strokes,
Kidney problem
42. Sulindac Acid 38194-50-2
Intermediate of API
n-1 Sulindac 38194-50-2
Sulindac /treat high blood pressure strokes,
Kidney problem
43. Irbesartan 138402-
11-6 API - - -
API/treat high blood pressure strokes, Kidney
problem
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44. 4‘-Bromomethyl-2-
Cyanobiphenyl 114772-
54-2 Intermediate
of API n-3
Irbesartan
138402-11-6
Irbesartan/ treat high blood pressure strokes,
Kidney problem
45.
4‘((2-Butyl-4-Oxo-1,3-diazaspirol[4,4]non-1-en-3-yl)methyl)-[1,1‘-
biphenyl]-2-carbonitrile
138401-24-8
Intermediate of API
n-2 Irbesarta
n 138402-11-6
Irbesartan/ treat high blood pressure strokes,
Kidney problem
46. Irbesartan Crude 138402-
11-6 Intermediate
of API n-1
Irbesartan
138402-11-6
Irbesartan/ treat high blood pressure strokes,
Kidney problem
47. Valacyclovir
Hydrochloride 124832-
27-5 API - - - API/cold sores
48.
N-[(benzayloxy)carbonyl]-L-valine-2-[2-amino-1,6-dihydro-6-oxo-9H-purin-9-yl) methoxy]
ethyl ester
124832-31-1
Intermediate of API
n-2
Valacyclovir
Hydrochloride
124832-27-5
Valacyclovir Hydrochloride/cold sores
49. Valacyclovir acid 124832-
26-4 Intermediate
of API n-1
Valacyclovir
Hydrochloride
124832-27-5
Valacyclovir Hydrochloride/cold sores
50. 6-Amino-2,4-dihydroxy-5-
nitrosopyrimidine
5442-24-0
Intermediate of API
n-1 Uracil 66-22-8 Uracil/synthesis of
enzymes in the body
51. Phenyl Acetonitrile 83552-81-2
Intermediate of API
n-1 Peniciline
G - Peniciline G/ Antibiotic
52. Phenyl Acetic Acid 103-82-2 API - - - API/Antibiotic
53. Tetra Butyl
Ammonium Bromide 1643-19-
2 API - - -
API/Levitrasetam Phase transfer catalyst
54. Tramadol
Hydrochloride 27203-92-5
API - - - API /Painkiller
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The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr. no.
Particulars Details
A-1 Total cost of Proposed Project (Rs. in Crores):
Total Project
8.92Crores
Break-up of proposed project Cost:
Details Project Cost (Rs. In Crores)
Land 2.50
Building 2.00
Machinery 2.50
A-2 Details of Environmental Management Plan (EMP) As below:
Sr. No
Unit Detail
Capital Cost
(Rs. In Lakhs)
Operating Cost/ Month (Rs. In Lakhs)
Maintenance Cost /
Month (Rs. In Lakhs)
Total Recurring Cost / Month (Rs. In Lakhs)
1 Waste Water
ETP: 68 KLD + Stripper: 65 KLD
80.00 27.95 2.80 30.75
Membership 1.00 6.45 6.45
2 Air & LDAR
4 No. Scrubber, 1 No. MCS,
Cyclone, Bag Filter & Water
Scrubber
30.70 0.77 0.38 1.15
3 Hazardous
Management
Membership & Disposal + Incineration
1.00 8.10 - 8.10
Transportation - 0.08 - 0.08
4 Fire & Safety
Fire Hydrant & pipeline System
19.10 0.10 0.05 0.15
Safety equipment/PPES
6.75 0.02 0.01 0.03
Fire Extinguisher & Foam Trolley
4.36 0.05 0.10 0.15
Integrated DCS 20.00 1.00 0.02 1.02
Trailer Driven Pump (6000
LPM) 4.00 0.05 0.10 0.15
5 AWH
Monitoring In House
Monitoring 1.50 0.20 0.05 0.25
6 Green Belt
Development 632 Trees 3.48 0.35 0.15 0.50
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7 Occupational
Health
OHC, Training & Medical Checkup
2.00 0.05 0.10 0.15
8 CER
Activities
2% as per OM dated
01/05/2018 18.00 0.06 0.04 0.10
Total 191.89 49.03
Summary
Cost of Project in Crores 8.88Crores
EMP Capital Cost in Crores 1.91Crores
EMP Recurring Cost in Crores 0.49 Crores
A-3 Details of CER as per OM dated 01/05/2018 (In case of project falls under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide 31.10.2019.)
% as per the OM
Rs. in Lakhs
2% 18.00
Brief note on proposed activities:
Activities
(On basis of Needs Assessment)
Phase Wise Budget (Rs. In Lakhs)
1st Year
2nd Year
TOTAL
Health-
Provide Ambulance with medical equipment (No.1) –Village Vorasamni
8.0 - 8.0
Infrastructure-
Solar Panel to Gram Panchayat Offices: 6
KW X 2 Nos (2 lakh each) Village- Vilayat,
Bhersam
2.0 2.0 4.0
Solid Waste Management–
Installation of OWC 500 Kg X 3 Nos @ 2 Lacs/Unit – Village Ankot, Saran, Cholad
Bins for segregation of waste
Operation & Maintenance of OWC
Training
3.0 3.0 6.0
Total Cost Approx. INR 18.0 Lakhs
B Land / Plot ownership details: Possession Receipt on the name of Proprietor – Mansukh N Radadia vide letter No. GIDC/DEE(Road)/BRH/60 on Dated: 05/02/2020
B-1 Plot area
Total Plot area
9576.272Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities: Company will store its raw material in Drums &Tanks (We procure Raw Materials from
the local market. 90% of these rawmaterials are easily available from this market. Hence,
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no excess quantity of raw materials will be stored). List of Hazardous chemicals stored in tanks shown below.
Sr. no Name of Chemical Capacity of
Tank Number of
Tanks Total Qty. to be store (KL)
PESO Tank 12Nos.
1 Methylene Chloride 15 KL 15 KL X 5 No 75 KL
2 Toluene 15 KL 1 No 15 KL
3 Ethyl Acetate 20 KL & 10 KL 20 KL X 2 Nos. 10 KL X 1 No
50 KL
4 Denatured Spirit 15 KL 2 No 30 KL
5 Acetic Acid 5 KL 1 No 5 KL
Non-PESO Tank 6 Nos.
1 Sulphuric Acid 10 KL 2 20 KL
2 Hydrochloric Acid 10 KL 2 20 KL
3 Sodium Hydroxide 10 KL 1 10 KL
4 Liq. Ammonia 10 KL 1 10 KL
Area required for ETP 210.0m²
120.0 m² area provided for the Boiler & TFH.
700.0 m² (G+2) area will be provided for the manufacturing of the proposed products.
S.N. Particulars Criteria for
Storage Inventory Required (MT)(KL)
Area Required
m2
Area Proposed
m2
1 Finished product
storage area (2 week inventory)
1 MT/ 1m2 75.00 75.00 120.00
2 Raw Material Store area
(2 week inventory) 1 MT/ 1m2 300.00 300.00 455.00
3 Drum Storage Area (Storage at a time)
1 MT/ 1m2 50.00 50.00 240.00
4 Petroleum Storage Area
(PESO) (Storage at a time)
- 175.00 350.00 720.00
5 Tank farm Area (Non-
PESO) (Storage at a time)
- 60.00 120.00 510.00
6 Cylinder Storage Area
(Nitrogen gas) (Storage at a time)
- 0.18 5.00 20.00
7 Hazardous Waste
Storage Area (G+1) (90 Day Inventory)
- 350 & 73 (Fly Ash)
423.00 500.00
1083.18
MT 1248.00
m2 2565.00
m2
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Hence, Adequate area is available for proposed Bulk drug intermediate mfg.
Facility.
B-3 Green belt area
Total (Sq. meter)
Area in Sq. meter 3161.00 Sq. m. (33 % of total plot area) Within plant premises
% of total area 33%
C Employment generation
Total
50 Employees Direct = 40 Employees
Indirect = 10 Employees
D WATER
D-1
Source of Water Supply (GIDC, Bore well, Surface water, Tanker supply etc...)
GIDC Water Supply Authority
Status of permission from the concern authority. Letter No.: GIDC/DEE (WS)/BRH/626 Dated: 19/09/2020.
D-2 Water consumption (KLD)
Sr. No.
Category
Total Fresh Water Consumption (KL/Day)
Remarks Total Water
Reused/ Recycled
Fresh Water
1. Domestic 2.30 - 2.30 GIDC Water Supply
Authority 2. Gardening 12.60 - 12.60
3. Industrial
Process 45.00 - 45.00
Worst Case: (1,1-piperazinyl-dibenzo[b,f] [1,4]
thiazepine)
Boiler 54.00 43.2 10.8
Total Water requirement: 54 KLD
Condensate Recovery: 43.2 LD
Make up Water: 10.8 KLD
Cooling 7.00 7.00 -
Washing 1.00 0.50 0.50
Scrubbing 4.00 2.00 2.00
Total Industrial 111.00 52.70 58.30
Total (1 + 2 + 3) 125.90 52.70 73.20
Brief Note on worst case scenario for water consumption:
Total Water Requirement of the proposed project will be 125.90 KLD, out of which Water Consumption for Process will be 45.0 KLD.
Worst Case Scenario;
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S.N Product Name Water req. (in KL)
for 1 MT production
Total Production (MT/Month)
Total water req. (KLD)
1.
1,1-piperazinyl-dibenzo[b,f] [1,4]
thiazepine 9.0 150.0 45.00
Hence Worst Case Considered is 45 KLD
- Summary of water requirement Quantity
KLD Remarks
Total water requirement for the project (A)
125.90 -
Quantity to be recycled / reused (B)
52.70 Reused & Recycled
Total fresh water requirement (C)
73.20 GIDC Water Supply Authority
Ensure Total water requirement = Fresh water + Recycled water i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]
Source of waste water for reuse in KLD (From where it is coming)
Application area with quantity in KLD (Where it is used)
Characteristics of waste water to be reused (COD, BOD, TDS etc.)
Remarks regarding feasibility to reuse
Boiler Condensate 38.5 KLD (Boiler)
pH: 7.5-8.0 TSS: < 60mg/l
TDS: <900 mg/l BOD: <10 mg/l COD: <30 mg/l Yes, it is
feasible.
From ETP
9.5 KLD (Cooling,
Washing & Scrubbing)
pH: 6.5-7.5 TSS: < 75 mg/l
TDS: <1000 mg/l BOD: <90 mg/l
COD: <250 mg/l
In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. -
D-3 Waste water generation (KLD)
Category
Proposed (KL/Day)
Remarks
1. Domestic 1.80 Will be treated in ETP
2. Industrial
Process 51.20 Worst Case: (Telmisartan)
Boiler 0.70
Cooling 0.70
Washing 1.00
Scrubbing Solution
(25-30% NaCl) 1.00
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Scrubbing Solution
(18-20% Na2SO3) 1.00 End User
Scrubbing Solution
(25-30% Liq. Ammonia) 1.00 Reused within premises
Scrubbing Solution (25-30%HBr/NaBr)
1.00 End User
Total Ind. 57.60
Total (1 + 2) 59.40
-
Brief Note on worst case scenario for waste water generation (Qualitative and Quantitative):
Total Waste Water Generation of the proposed project will be 59.40 KLD, out of which Waste Water Generation for Process will be 51.2KLD.
Worst Case Scenario;
S.N Product
Waste Water Gen. (in KL)
for 1 MT production
Total Production (MT/Month)
Total Waste water Gen. (KLD)
Characteristics
1. Telmisartan 10.24 150.0 51.2
pH – 6.5 to 7.5 (Neutralization at source) TSS-190 mg/l TDS-23560 mg/l BOD- 7820 mg/l COD-26122 mg/l
Hence Worst Case Considered is 51.2 KLD
Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (Whichever is applicable).
Not Applicable. There will be effluent generation. The detail has been furnished in water Balance.
D-4 Mode of Disposal & Final meeting point
Domestic: Domestic wastewater@ 1.8 KLD will be Subjected to ETP.
Industrial: Total Effluent 54.79 KLD will be treated in ETP.
45.00 KLD discharged to CETP of Saykha GIDC and 9.5 KLD treated water will be reused in Cooling,Washing & Scrubbing.
- Clearly mention about final disposal
D-5 Treatment facilities
For Domestic waste water: Capacity of STP: Not Applicable
For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed. Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Hydraulic Load – In-house Stripper: 51.20 KLD
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In-House ETP:54.79 KLD
Capacity— In-house Stripper: 65.0 KLD In-House ETP: 68.0 KLD
Stream 1 - Waste water from process @ 51.20 KLD will be subjected to solvent stripper. Outlet
of stripper @50.59 KLD will be treated in ETP (Primary & Secondary).
SR.
No.
Para Unit
Worst case Process Water After Solvent
Stripper Telmisartan
Quantity (KLD) 51.20 50.59
1 pH pH Unit 6.5-7.5
(Neutralization at source) 6.5-7.5
2 TSS mg/L 190 190
3 TDS mg/L 23560 23560
4 BOD mg/L 7820 3910
5 COD mg/L 26122 10449
6 Ammo. Nitrogen mg/L Nil Nil
Stream 2 - Waste water from 0.7 KLD Boiler Blow Down, 0.7 KLD cooling blow down, 1.0 KLD Washing
and 1.0 KLD Scrubbing Soln (25-30% NaCl Sol.) = 3.4 KLD will be Subjected to ETP (Primary & Secondary).
Sr. No.
Parameter
Unit
Stream from other utilities Characteristics Combine
Effluent Boiler Cooling Washing Scrubbin
g
Quantity (KLD) 0.7 0.7 1.0 1.0 3.4
1 pH pH Unit 7.5-8.0 7.5-8.0 6.0-8.0 6.0-8.0 6.0-8.0
2 TSS mg/L 56 87 150 120 109
3 TDS mg/L 500 1200 2500 500 1232
4 BOD mg/L 10 16 487 190 204
5 COD mg/L 30 50 2298 524 846
6 Ammo.
Nitrogen mg/L Nil Nil Nil Nil Nil
Stream 3 – Totally 53.99 KLD (Stream 1: 50.59 KLD After Solvent Stripper + Stream 2: 3.4 KLD Dilute
Stream) will be allowed to in-house ETP (Primary).
Sr. No.
Parameter Unit
After Solvent stripper
Combine Effluent (Dilute
Stream)
Composite Effluent
After Primary
treatment
Quantity (KLD) 50.59 3.4 53.99 52.99
1 pH pH Unit
6.5-7.0 6.0-8.0 6.5-7.5 6.5-7.5
2 TSS mg/L 190 109 185 55
3 TDS mg/L 23560 1232 22154 23262
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Primary treated Waste water @52.99 KLD along with Domestic Waste Water @1.8 KLD will
be allowed in Secondary ETP.
Sr. No.
Parameter
Unit
After Primary Treatme
nt
Domestic
Composite Effluent
After Secondar
y Treatmen
t
After Tertiary
Treatment
Quantity (KLD) 52.99 1.8 54.79 54.29 9.50
1 pH pH Unit
6.5-7.5 6.0-8.0 6.5-7.5 6.5-7.5 6.5-7.5
2 TSS mg/L 55 300 64 74 <50
3 TDS mg/L 23262 750 22522 22522 <1000
4 BOD mg/L 2941 250 2853 428 <90
5 COD mg/L 7875 10 7617 1143 <250
6 Ammo.
Nitrogen mg/L Nil Nil Nil Nil Nil
Stream 4(Scrubbing Solution) – 1.0 KLD 25-30% NaCl Scrubbing Soln will be treated in-house ETP. 1.0 KLD 18-20% Na2SO3 and 1.0 KLD 25-30 % NaBr/HBr scrubbing soln will be sent to end
users registered under Rule-9. 1.0 KLD 25-30% Liq. Ammonia will be reused within premises.
4 BOD mg/L 3910 204 3677 2941
5 COD mg/L 10449 846 9844 7875
6 Ammo.
Nitrogen mg/L Nil Nil Nil Nil
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP. Total Effluent 54.79 KLD will be treated in ETP.
45.00 KLD discharged to CETP of Saykha GIDC and 9.5 KLD treated water will be reused in Cooling, Washing& Scrubbing.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Not Applicable – Total Effluent 54.79 KLD will be treated in ETP.
45.00 KLD discharged to CETP of Saykha GIDC and 9.5 KLD treated water will be reused in Cooling, Washing& Scrubbing.
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)
Common ETP of M/s. GIDC - Saykha
Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
Common ETP of M/s. GIDC – Saykha Permission Letter No. GIDC/BRH/XEN/WD/975 on dated 17/09/2020.
D-7 Simplified water balance diagram with reuse / recycle of waste water
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E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case scenario thereof:
SN Fuel Based Heat Energy
Proposed Fuel
Calorific Value (kcal/kg)
Working Hours (Worst Case)
Fuel Consumption in worst case
1 Boiler 3.0
TPH
Natural Gas
7900 – 8500 kcal/kg
18 Hrs 5085SCM/Day
OR
Bio Coal 3800-4300 kcal/kg 18 Hrs 11.0 MT/Day
2
Thermic Fluid Heater
(5 Lac KCal/Hr.)
Natural Gas
7900 – 8500 kcal/kg
24 Hrs 2000 SCM/Day
OR
Bio Coal 3800-4300 kcal/kg 24 Hrs 4.0 MT/Day
E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)
Sr. No.
Stack attached
to
Stack Height&
Dia (Meter)
Type of Fuel
Fuel Consumpt
ion APCM
Concentration of Pollutants
1. Boiler (3.0
TPH) 30/0.5
Natural Gas OR
Bio Coal
5085 SCM/Day
OR 11.0
MCS + Bag Filter+ Water
Scrubber &
PM < 150 mg/Nm3
SO2 < 100 ppm
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MT/Day Adequate Stack height
NOX < 50 ppm
2.
Thermic Fluid
Heater (5 Lac
KCal/Hr.)
30/0.5
Natural Gas OR
Bio Coal
2000 SCM/Day
OR 4.0
MT/Day
Cyclone + Water
Scrubber&Adequate
Stack height
3.
D.G. Set Stand by
(125 KVA)
11/0.25 Diesel 20 lit/Hr. Adequate
Stack height
4.
D.G. Set Stand by
(450 KVA)
11/0.25 Diesel 60 lit/Hr.
E-3 Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emission
Stack/Vent Height & Dia
(meter)
Air Pollution Control
Measures (APCM)
1
Reaction Vessel-1 (Sulphonation) Couple Amine Hydrochloride
SO2: 40 mg/Nm3
18/0.2 Two Stage
Alkali Scrubber
2
Reaction Vessel-2 (Chlorination)
6-Flouro-2-Methyl 2-3-dihydro-1H-indon-
1-one
HCl: 20 mg/Nm3
18/0.2 Two Stage Alkali
Scrubber
3
Reaction Vessel-3 (Ammination)
5-fluro-2-methylindene-3-Acid
NH3: 175 mg/Nm3
18/0.2 Two Stage Water
Scrubber
4
Reaction Vessel-4 (Bromination)
Tramadol Hydrochloride
HBr: 30 mg/Nm3
18/0.2 Two Stage Alkali
Scrubber
Note: Details of gaseous raw materials used in proposed project Estimation of process gas emission (Product wise and Total) Requirement of the scrubbing media (KL per Day) considering solubility (Product
wise and Total) Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and
its sound management in HW matrix.
Sn
Product
Gaseous Raw Materia
l
Process
Gas Emiss
ion
Total Emiss
ion (MT/D
ay)
Requirement of
Scrubbing Media (KL Per
Day)
Solution /
bleed liquor
s
Solubility (%)
Solution / Bleed liquors
(MT/Annum)
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(KLD)
1
Couple Amine
Hydrochloride
Thionyl Chlorid
e SO2 0.2
0.8 (Caustic)
1.0 > 90 365 KL
(18-20% Na2SO3)
2
6-Flouro-2-Methyl
2-3-dihydro-
1H-indon-1-one
Thionyl Chlorid
e HCl 0.3
0.7 (Caustic)
1.0 > 90
365 KL (25-30 %
NaCl)
3 5-fluro-2-
methylindene-3-Acid
Ammonium
Acetate NH3 0.3
0.7 (Water)
1.0 > 90
365 KL (25-30%
Liq. Ammoni
a)
4 Tramadol
Hydrochloride
m-Bromo Anisole
HBr 0.3 0.7
(Caustic)
1.0 >90
365 KL (25-30% NaBr/HB
r)
E-4 Fugitive emission details with its mitigation measures.
To mitigate fugitive emissions, the following steps would be taken:
Minimum number of flanges, joints and valves in pipelines
Selection / use of state-of-the art leak proof valves
Provision of mechanical seals in pumps
Proper preventive maintenance of roofs and seals for tanks
Monitoring and preventive maintenance of valves, flanges, joints, etc.
Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area, shall be collected through hoods and ducts by induced draft and controlled by dust collector.
For particulate / dust emissions from the coal handling system: Water will be sprinkled to control particulate / dust emission from coal storage area.
Green belt will be developed along the plant premises
De-dusting system will be provided at solid product finishing area.
All transfer points will be fully closed.
Overflow system with return line to storage tank from batch tank will be provided to prevent hazardous material overflow.
F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:
Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.
Quantification of hazardous waste shall be based on mass balance and
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calculations shall be incorporated in EMP details separately. Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Sr. no.
Type/Name of
Hazardous waste
Specific Source of generation (Name of the
Activity, Product etc.)
Category and
Schedule as per HW
Rules.
Quantity
(MT/ Annu
m)
Management of HW
1 ETP
Sludge ETP
35.3/ SCH-I
550.0 Collection, Storage, Transport, and Disposal at nearest TSDF.
2
Process Waste
(Inorganic)
Mfg. Process
5-fluro-2-methylindene-3-
Acid
28.1/SCH-I
360
3 Used Oil Maintenance
Activities 5.1/SCH-I 0.5
Collection, Storage, Transportation; reuse as lubricant or by selling to Authorized re- refiners.
4
Discarded Container
s/ Bags/Line
rs
Raw Material Supplier
33.1/SCH-I
50.00 (Nos. 5000
Container)
(Nos. 50000
0 Bags/Liners)
Collection, Storage, Transportation; Decontamination and Reuse or Sale to Authorized Vendor.
5 Distillation Residue
Mfg. Process
Levofloxacin
20.3/SCH-I
1152
Collection, Storage, Transportation & Disposal by selling to Pre /Co-processing unit (Cement Industries) or by incineration at CHWIF.
6 Process Waste
(Organic)
Mfg. Process
Diacetylacyclovir(9-[(2-
Acetoxyethoxy)methyl] -N2-
acetylguanine
28.1/SCH-I
864.0
7 Spent
Carbon/ Hyflow
Mfg. Process
Acyclovir
28.3/SCH-I
216.0
8 Spent
Solvent
Mfg. Process
Levofloxacin
28.6/SCH-I
*58340
Collection, Storage, Handling & Subjected to distillation assembly to recover the solvent & Reuse
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within premise.
From Solvent Stripper
222.65
Collection, Storage, Transportation & send to pre/co processing unit (Cement Industries) OR send to CHWIF.
9
Scrubbing Solution
25-30% NaCl
From Scrubber
6-Flouro-2-Methyl 2-3-dihydro-1H-indon-1-one
28.1/SCH-I
365 KL
Collection, Storage &treat in ETP
10
Scrubbing Solution
25-30% Liq.
Ammonia
From Scrubber
5-fluro-2-methylindene-3-
Acid
28.1/SCH-I
365 KL
Collection, Storage & Reuse within premises.
(In the Mfg. process of Azithromycin: 4320 MT/Annum )
11
Scrubbing Solution
18-20% Sodium Sulphite (Na2SO3)
From ScrubberCoupl
e Amine Hydrochloride
28.1/SCH-I
365 KL Collection, Storage,
Transportation& Sell to End Users having permission under Rule-9.
12
Scrubbing Solution
25-30% HBr/NaBr
From ScrubberTrama
dol Hydrochloride
28.1/SCH-I
365 KL
13
Off Specificati
on Product
Mfg. Process
(Batch Failure)
28.4/SCH-I
1
Collection, Storage Transportation & send to Pre /Co-processing unit or send to CHWIF
*Justification for spent solvent generation & Captive reused
Product Name Solvent Fresh
Qty. Used MT/Day
Qty. Recovered
MT/Day
Qty. Used MT/Day
Tank Storage (At a Time)
Levofloxacin
Methylene Chloride
3.75 71.25 75.00 75 KL
(15 KL X 5 No.)
Toluene 0.68 12.83 13.50 15 KL
(15 KL X 1 No.)
Ethyl Acetate 2.00 48.00 50.00 50 KL
(20 KL X 2 Nos. 10 KL X 1 No.)
Denatured 1.17 28.08 29.25 30 KL
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Spirit (15 KL X 2 No.)
Acetic Acid 0.10 1.90 2.00 5 KL
(5 KL X 1 No.)
Total MT/Day 7.70 162.06 169.75
Total MT/Year 2770.2
58339.8 ~ 58340
61110
F-2 Membership details of TSDF, CHWIF etc. (For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Dahej For Land Filling Letter No. Nil Dated: 11/11/2020 For Incineration Waste Letter No. Nil Dated: 11/11/2020
F-3 Details of Non-Hazardous waste & its disposal (MSW and others)
Sr. no.
Type/Name of Other wastes
Specific Source of generation
(Name of the Activity,
Product etc.)
Quantity (MT/Annum)
Management of Wastes
1 Fly Ash Boiler & TFH
Fuel (Bio-coal)
292.0
Collection, storage, transportation & send to Brick manufacturer
OR farmer for agricultural purposes
OR TSDF for Landfilling.
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.
G-2 Brief Note on LDAR proposed:
The Following methodology to be adopted during LDAR study: Identify the Chemical streams that must be monitored. Types of components (pumps, valves, connectors, etc.) to be monitored Frequency of monitoring. Actions to be taken if a leak is detected. Length of time in which an attempt to repair the leak must be performed. Actions that must be taken if a leak cannot be repaired within guidelines. Record-keeping and reporting requirements.
G-3 VOC emission sources and its mitigation measures
Leak Free Pumps for transfer of solvents. MSW Gaskets in solvent pipelines to prevent leakage from flanges. Minimum number of flanges, joints and valves in pipelines. To eliminate chances of leakages from glands of pumps, mechanical seal will
be provided at all solvent pumps. All the rotating equipments like pumps will be installed with Mechanical Seals to
arrest any sort of emissions. Condenser and scrubber post Reactor with cooling arrangement. Enclosures to chemical storage area, collection of emission from loading of raw
materials in particular solvents through hoods and ducts by induced draft, and control by condenser to be ensured.
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In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send to ETP.
If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark.
Two condensers will install with cooling water and chilled brine to recover the solvent.
Primary Condenser HE-01: Cooling Tower water or Chilled water at 5 °C will be used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser.
VOC Trap Condenser HE-02: Chilled Brine at -15 °C will be used to trap any traces of Solvent which is slipped from Secondary condenser.
Emission of VOCs can be trapped from breathing and loading losses from storage tanks, venting of process vessels, leak from piping and equipment by means of hood connected with blower and send to condenser as shown in following diagram.
Condensed VOCs will be send to spent solvent recovery plant.
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)
Sr. no Name of Chemical Capacity of
Tank Number of
Tanks
Hazardous Characteristics
of Chemical
PESO Tank 12 Nos.
1 Methylene Chloride 15 KL 15 KL X 5 No Flammable
2 Toluene 15 KL 1 No Flammable
3 Ethyl Acetate 20 KL & 10 KL 20 KL X 2
Nos. 10 KL X 1 No
Flammable
4 Denatured Spirit 15 KL 2 No Flammable
Non-PESO Tank 6 Nos.
1 Sulphuric Acid 10 KL 2 Toxic
2 Hydrochloric Acid 10 KL 2 Toxic
3 Sodium Hydroxide 10 KL 1 Toxic
4 Liq. Ammonia 10 KL 1 Flammable
Brief note on storage of Hazardous chemicals in Tanks
PESO Tank- 12 nos. (Underground)
Non-PESO- 6 Nos Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.
Some chemicals will be received at plant in drums by road truck and stored in a separate drum storage area.
FLP type light fittings will be provided. Proper ventilation will be provided in go down. Proper label and identification board /stickers will be provided in the storage
area. Conductive drum pallets will be provided. Drum handling trolley / stackers/fork lift will be used for drum handling. Separate
dispensing room with local exhaust and static earthing provision will be made.
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Materials will be stored as per its compatibility study and separate area will be made for flammable, corrosive and toxic chemical drums storage.
Smoking and other spark, flame generating item will be banned from the Gate. Safety details of Hazardous Chemicals:
Type of Hazardous Chemicals
Safety measures
PESO Tank Safety Measures for PESO Underground storage tank farm: The underground vessels shall be placed within concrete
or brick masonry pit with a gap of 1.0 meter between the walls of the pit and the vessel as well as in between the vessels.
The underground vessels shall be installed on a firm foundation and firmly secured to the foundation so as to prevent movement of floatation.
Class A Petroleum products will be received through road tanker and stored in u/g storage tank as per PESO Rule.
Tank farm will be constructed as per explosive department requirement and separation distance will be maintained.
The underground vessels covered by earth (Mound) shall be a designed to withstand external pressure due to load of the earth cover. o Provided with external anti-corrosive coating or
cathodic protection to prevent corrosion ; o Covered by earth, sand or any other non-corrosive
material free from abrasive particles likely to damage the anti-corrosive coating of the vessel-the thickness of the covering material above the top surface of the vessel shall not be less than 0.5 meter;
o Having the discharge level of the safety relief valves at least 2 meters above the top surface of the vessel, but in any case not less than 3 meters from the ground level;
o Fitted with the necessary piping's, fittings, valves and other mounting on top of vessel in such a manner that they can be operated and maintained without disturbing the earth cover. In case of above ground vessel with earth cover (mound), liquid outlet pipe at the bottom may be allowed provided the control valve and emergency valve of this line is just outside the earth cover for the purpose of operation and maintenance from outside.
Static earthing provision will be made for road tanker as well as storage tank.
Flame arrestor with breather valve will be provided on vent line.
Road tanker unloading procedure will be prepared and implemented.
Fire load calculation will be done and as per fire load hydrant system will be provided as per NFPA std. and fire extinguishers will be provided as per fire load calculation.
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Spark arrestor will be provided to all vehicles in side premises
Lightening arrestor will be provided on the top. Flame proof type equipment and lighting will be provided. Trained and experience operator will be employed for
tank farm area. NFPA label (hazard identification) capacity and content
will be displayed on tanks Solvents will be transferred by pump only in plant area
and day tank will be provided. Overflow line will be return to the storage tank or Pump On-Off switch will be provided near day tank in plant.
Jumpers will be provided on solvent handling pipe line flanges & Flexible SS hose will be used for road tanker unloading purpose and other temp. connection
PESO Area Storage & Handling Safety: (UNLOADING)
Ensure that the transfer of petroleum takes place only through electrically continuous sound hose having oil tight couplings at both ends.
Couplings of the hose at the discharge ends of the tank trucks as well as at the fill pipe end of the underground tank shall not be leaky.
Unloading operations should not commence without ensuring earthing of the tanker body to a proper earthing point. For this purpose, a proper earthing point shall be provided near filling points.
Before commencing unloading operations tanker should be parked in the retail outlet in such a manner that it can be taken out of the retail outlet immediately in case of emergency.
Dip pipe of the underground tank shall not be kept open during unloading operations.
The dealer, supervisors and pump attendants shall be trained in all aspects of safety in RO including the provisions of Petroleum Rules, 2002 in Chapter IV on Electric Installation, Rules 117 to 119,122,125 and conditions 6 to 12, 15,16,18 to 21of licence Form XIV for the RO‘s under the said Rules.
Before starting unloading of petroleum, it must be ensured that at least a safe distance of 3 M is kept clear of any kind of movement of other vehicles that come for fuelling and that there is no source of any spark in the area. In case of retail outlets that are in congested areas operations of fuelling automobiles in the retail outlet may be discontinued.
Do not use plastic hose pipes for unloading purposes. Do not use hose pipe fitted with metallic pipe
(bent pipe) at the discharge end. Do not use Hose pipes not conforming to OISD
135. Proper tightening of hose connections using
screwed/cam lock couplings.
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Make sure that there shall be no collection of leaked petroleum through hose pipe connection at tanker discharge faucet end in the plastic bucket kept on the ground below.
Provision of electrical earthing / bonding by means of flexible cable between tanker chassis and earth boss/fill pipe.
Proper training to the retail outlet staff regarding hazards associated with the petroleum road tanker decantation operation in the retail outlets.
Non PESO tank
Safety measures for Acid storage Tank: Storage tank will be stored away from the process plant. Tanker unloading procedure will be prepared and
implemented. Caution note and emergency handling procedure will be
displayed at unloading area and trained all operators. NFPA label will be provided. Required PPEs like full body protection PVC apron, Hand
gloves, gumboot, Respiratory mask etc. will be provided to operator.
Neutralizing agent will be kept ready for tackle any emergency spillage.
Safety shower, eye wash with quenching unit will be provided in acid storage area.
Material will be handled in close condition in pipe line. Dyke wall will be provided to all storage tanks, collection pit
with valve provision. Double drain valve will provided. Level gauge will be provided on all storage tanks. Safety permit for loading unloading of hazardous material
will be prepared and implemented. TREM CARD will be provided to all transporters and will be trained for transportation Emergency of Hazardous chemicals.
Fire hydrant system with jockey pump as per TAC norms will be installed.
Safety Measures of Non PESO Tank Leakage / spillage mitigation plan Tank shall be rubber lined to prevent the corrosion Dyke wall shall be provided for containment Rubber type hand gloves and chemical splash goggles
and full-face cartridge type mask and PVC apron shall be used while manual handling
Lime shall be readily available during leak to neutralize the spill material
Safety shower, eye wash with quenching unit will be provided in acid storage area.
Material will be handled in close condition in pipe line. Double drain valve will provided. Level gauge will be provided on all storage tanks. Fire hydrant system with jockey pump as per TAC norms
will be installed
Applicability of PESO: Will be obtained.
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H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Sulphonation, Chlorination process, Bromination Reaction etc.)
Type of Process
Safety measures including Automation
Hydrogenation
DCS base process controls and operation of plant will be
installed.
All electrical equipment‗s shall be installed as per Hazardous
Area Classification.
Total enclosed process system.
Instrument & Plant Air System.
Nitrogen blanketing in Hydrogenation reactor.
Emergency dumping vessel will be provided during
unforeseen circumstances.
Safety valve and Rupture disc provided on reactor.
Cooling, Chilling and alternate power arrangement have
been made on reactor.
Process area and Hydrogen cylinder bank shall be far away
as per standards practice.
PRV station with shut off valve, safety valve provision will be
made for hydrogenation reaction safety.
Standard Operating procedure shall be followed during
operation of Hydrogen Gas charging in to reactor and after
completion of reaction Nitrogen purging will be done.
Flame arrestor will be provided on vent line of reactor and it
will be extended above the roof level.
Safe Catalyst charging method will be adopted.
SOP will be displayed and operators will be trained for the
same.
Static earthing and electric earthing (Double) will be provided.
Jumpers for static earthing on pipeline flanges of flammable
chemical will be provided.
Hydrogen gas detector will be installed for early
detection of gas leak.
Bromination All end nozzles in bromine charging hose will be blinded after use.
Charging of bromine will be done when reactor is in
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vacuum and POP coated funnel will be used during charging.
Excess bromine will be neutralize or discharged by adding Sodium Bisulfite.
Make sure the absorber unit (scrubber) is working and capable of handling vented bromine fumes.
Structure of bromine bottle area will be periodically inspected to ensure stability.
Personnel employed with bromine handling are made aware of potential hazards of bromine and of appropriate first-aid measure.
Exhaust hood connected with alkali scrubber and ventilation system will be available. Exhaust hood has been provided to maintain to concentration of bromine vapor well below PEL.
Work instructions for bromine charging will be displayed in local language/Hindi.
Safety shower and eye-wash fountains will be available nearby handling and charging facility. The location of such item will be inspected and tested at fixed interval to make sure that it is in good condition.
Hypo solution, lime water slurry or soda ash solutions will be available so as to pour them over a liquid bromine spill on the floor. The bromine and neutralizer is then washed to the sump with cold water hose.
Personal Hygiene – the following personal protective equipment will be used.
Chemical safety goggles, face shields, SCBA sets, Aprons, rubber gloves, etc.
Only trained employees handled bromine charging. Training will be given to employees for bromine handling and charging.
Sulphonation & Chlorination (Only Through
Thionyl Chloride)
Provision of Safety valve & rapture disc on reactor.
Provision of auto dumping vessel.
Required PPEs like full body protection PVC apron, Hand gloves, gumboot, Respiratory mask etc. will be provided to operator.
To avoid runaway reaction, TC charging will be done gradually & slowly to avoid runaway reaction, TC charging will be done gradually & slowly.
Charging will be done only through closed line and system. Scrubber attached with closed system.
Make sure the absorber unit (two stage Alkali scrubber) is working and capable of handling vented SO2 / HCl fumes.
Neutralizing agent will be kept ready for tackle any emergency spillage.
Safety Shower and eye wash will be provided near process area.
For Thionyl Chloride evacuate area in down wind direction up to 0.3 km ( 300 meter) in small spillage.
Emergency siren and wind sock will be provided. Tele Communication system and mobile phone will be used
in case of emergency situations for communication.
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Total close process will be adopted for Thionyl chloride charging.
Caution note and emergency first aid will be displayed and train for the same to all employees.
First Aid Boxes will be available in process area. Emergency organization and team will be prepared as per
On site-Off site emergency planning. Emergency team will be prepared and trained for scenario
base emergency. Like Toxic control team, Fire control team, First aid team, communication and general administration team, Medical team etc.
Do not touch damaged containers or spilled material unless wearing appropriate protective clothing.
Use water spray to reduce vapors; do not put water directly on leak, spill area or inside container. Keep combustibles (wood, paper, oil, etc.) away from spilled material.
Cover with DRY earth, DRY sand or other non-combustible material followed with plastic sheet to minimize spreading or contact with rain.
H-3 Details of Fire Load Calculation
Total Plot Area: 9576.27Sq.mt
Area utilized for plant activity:
700Sq.mt
Area utilized for Hazardous Chemicals Storage:
500Sq.mt
Number of Floors Area:
Sr. No
Plant / Building/Facility Name
Total No. of floor
Details of Floor
Area of the floors and
galleries
in sq meter
1 Security Cabin 1 & 2 1 Ground floor 36.00
2 D.G Set 1 Ground floor 8.00
3 OHC 1 Ground floor 20.00
4 Admin Building 1 Ground floor 80.27
5 Process Building 3
Ground floor 700.00
First floor 700.00
Second floor 700.00
6 Non Peso Tank Area 1 Ground floor 510.00
7 Raw Materials Storage 1 Ground floor 455.00
8 Finished Product Storage 1 Ground floor 120.00
9 Drum Storage Area 1 Ground floor 240.00
10 Petroleum Storage Area 1 Ground floor 720.00
11 Boiler & TFH 1 Ground floor 120.00
12 ETP 1 Ground floor 210.00
13 Haz Waste Storage Area 1 Ground floor 500.00
14 Fly Ash Storage 1 Ground floor 40.00
15 Fuel Storage 1 Ground floor 50.00
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16 Cylinder Storage Area 1 Ground floor 20.00
17 Fire Pump House 1 Ground floor 40.00
5269.2
7
Water requirement for firefighting
55,804 Liters
Water storage tank provided for firefighting
4,00,000Liters
Details of Hydrant Pumps:
Fire water Pump will be available. We will have 01 No‘s of electrical fire water Pump located at pump house having capacity 4550.0 litres/min and 01 No‘s of Diesel pump having capacity 4550.0 litres/min. Apart from this we have 01 Nos Jockey Pumps of capacity 1080.0 litres/min which maintains the Fire water Header Pressure at 8.0 kg/cm².
Nearest Fire Station : Fire Station : SEZ Fire Station, Dahej (Distance from project site: 32.38km)
Applicability of Off Site Emergency Plan:
--
H-4 Details of Fire NOC/Certificate:
Will be Applied
H-5 Details of Occupational Health Centre (OHC):
Number of permanent Employee : 40
Number of Contractual person/Labour : 10
Area provided for OHC: 20Sq. m
Number of First Aid Boxes : 20
Nearest General Hospital : Pipalia Health Care Center, Pipalia
Name of Antidotes to be store in plant : Artificial respiration, First Aid, etc.
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. Greenleaf Envirotech Pvt Ltd remains present
during video conference meeting.
Committee noted that the proposal is for Greenfield project in GIDC Saykha. PP submitted details
regarding area adequacy. Source of water is GIDC. Product profile along with end use discussed in
depth. Committee noted that PP has shown Tetra Butyl Ammonium Bromide as API and its end use as
phase transfer catalyst which is not in line with MoEF&CC‘s Notification vide S.O. 1223 (E) dated
27/03/2020 in respect of Active Pharmaceutical Ingredients (API) as category B2 projects and hense
asked for clarification regarding it during meeting which is could not presented by PP properly during
SEAC meeting.
Committee noted that PP has submitted waste water management and industrial effluent will be
segregated. High COD stream will be passed through solvent stripper and then along with Low COD
stream will be partly treated in ETP consist of primary and secondary ETP units and treated effluent will
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be sent to CETP of GIDC Saykha for further treatment and disposal. Rest of treated effluent will be
further treated in tertiary ETP units and treated effluent will be reused back in process. Domestic sewage
will be treated in ETP. Committee discussed regarding stage wise reduction of BOD, COD and TDS in
ETP to achieve CETP inlet norms. Committee insisted for submit adequate treatability report for high
COD stream from process and low COD stream with stage wise reduction of BOD,COD,TDS and
Ammonical nitrogen in ETP to achieve inlet norms of CETP with mentioning characteristic of effluent
generated from each proposed products.
PP submitted that they have proposed boiler, thermo pack and DG set. Fuel used will be Natural gas or
bio coal for boiler and thermo pack.MCS, bag filter and water scrubber as APCM proposed for bio coal
fired boiler. Two stage scrubbers will be provided as APCM with each process reactor stack. PP
submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.
Upon asking regarding provision of fire hydrant network and proposed fire extinguishers details, PP has
addressed the Site Plan/layout plan with provision of fire hydrant network, periphery road with entry and
exit separately, proposed fire extinguishers details adequate fire water reservoir and fire load calculation.
Committee noted that PP has addressed fire evacuation plan, worker‘s safety and occupational Health
centre (OHC) and process hazard and its safety control measures. Committee noted that PP presented
details of auto control system for critical process and Hazardous chemical storage area with its risk
assessment.
Committee deliberated on storage and safety aspects of hazardous chemicals, green belt area, EMP,
CER, LDAR and solvent recovery etc.
After detailed discussion, Committee unanimously decided to consider the project only after
submission of following documents,
1. Submit clarification regarding Tetra Butyl Ammonium Bromide mentioned as API and its end use
as phase transfer catalyst which is not in line with MoEF&CC‘s Notification vide S.O. 1223 (E)
dated 27/03/2020 in respect of Active Pharmaceutical Ingredients (API) as category B2 projects.
2. Submit clarification regarding proposal of high COD stream from process for disposal in CETP in
place of proposal of MEE for evaporation of high COD stream.
3. Submit adequate treatability report for high COD stream from process and low COD stream with
stage wise reduction of BOD, COD, TDS and Ammonical nitrogen in ETP to achieve inlet norms
of CETP with mentioning characteristic of effluent generated from each proposed products.
10. SIA/GJ/IND2/173540/2020 M/s. Navjeevan-O-Chem
Plot No. 5903/1, GIDC Industrial Estate,
Ankleshwar, Dist-Bharuch
Appraisal
Category of the unit: 5(f)
Project status: Expansion
Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173540/2020 on dated
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05.10.2020 for obtaining Environmental Clearance.
Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as
per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration
of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.
This is an existing unit and now proposes expansion in manufacturing of synthetic organic chemicals
[API and API Intermediates] as tabulated below.
Sr. no.
Name of the Products
API OR INTERMEDIATE
CAS no.
Quantity MT/Month
End-use of the products * Existing Proposed Total
1. Ferric Chloride (Anhydrous and Lumps)
-- 7705-08-0
39.02 -- 39.02
--
2. Meta Nitro Para
Toluidine
API Intermediate
119-
32-4
-- 50.00 50.00
API Intermediate
3. Ethyl Ethoxy
Methylene
Malonate
API Intermediate
87-13-
8
API Intermediate
4. 3.5-Dihydroxy
Benzoic Acid
API Intermediate
99-10-
5
API Intermediate
5. 3.5-
Dichlorobenzoic
Acid
API Intermediate
51-36-
5
API Intermediate
6. 3-Hydroxy
Acetophenone
API Intermediate
121-
71-1
API Intermediate
7. 5-Cyano Phthalide
API Intermediate
82104-
74-3
API Intermediate
8. 2‐Chloromethyl‐4‐
methoxy‐3,5‐dimet
hylpyridine
hydrochloride
API Intermediate
86604‐
75‐3
API Intermediate
9. 2 Hydroxy 5 Nitro
Benzoic Acid
API Intermediate
96-97-
9
API Intermediate
10. R & D Products
(Nitration,
Sulphonation,
Amination,
Chlorination)
AP Intermediate
-- -- 0.10 0.10 API Intermediate
Total 39.02 50.10 89.12
ENDUSE OF PRODUCTS
Sr. No.
Name of the Product CAS No.
Type/ Category of
In case of Intermediate stage of API
Said API is used
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(Product) Product (API/ Intermediate)
Stage i.e. n-1, n-2, etc.
Name of API in which Intermediate Used/ End use of said Intermediate
CAS no. (API)
for/End Use of said API
2.
Meta Nitro Para Toluidine 119-32-4 API
Intermediate
n-2 Cyclizine
82-92-8
To Prevent Nausea, Vomiting
3.
Ethyl Ethoxy Methylene Malonate 87-13-8 API
Intermediate
n-2
4:7-Dichloro Quinoline
86-98-6
Discoid lupus
erythematosus and
systemic lupus
erythematosus
4.
3.5-Dihydroxy Benzoic Acid 99-10-5 API
Intermediate
n-2 Phenylephri
ne 59-
42-7 Stuffy Nose,
Sinus
5.
3.5-Dichlorobenzoic Acid 51-36-5 API
Intermediate
n-2
Alkylresorcinol
39341-78-
1
Metabolite, used in Human Urine
infection
6.
3-Hydroxy Acetophenone 121-71-1 API
Intermediate
n-2 Phenylephri
ne 59-
42-7 Stuffy Nose,
Sinus
7.
5-Cyano Phthalide 82104-74-3
API Intermediat
e
n-2 Citalopram
59729-33-
8
Anti-Depression
8. 2‐Chloromethyl‐4‐methoxy‐3,5‐dimethylpyridine hydrochloride
86604‐75
‐3
API Intermediat
e
n-1 Omeprazol
e
73590-58-
6 Peptic Ulcer
9.
2 Hydroxy 5 Nitro Benzoic Acid 96-97-9 API
Intermediate
n-1
Mesalamice 89-
57-6
Treat Bowel isease, Stomach
Pain
The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006
and amendment dated 27th March, 2020.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020
Salient features of the project including Water, Air and Hazardous waste management as below,
Sr. no. Particulars Details
A-1 Total cost of Proposed Project
(Rs. in Crores):
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Existing
Proposed
Total
2.45 Crores 3.5496Crores 6.00Crores
Break-up of proposed project Cost:
Details Existing
(Rs. In Crores)
Proposed
(Rs. In
Crores)
Total
(Rs. In
Crores)
Land 2.45 -- 5.9996
Buildings 0.73
Plant & Machinery 1.43
EMP Cost 1.3896
Total 2.45 3.5496 ≈ 6.00
A-2 Details of Environment l Management Plan (EMP) As below:
Sr. No Unit Detail Capital Cost (Rs. In Crore)
Operating Cost (Rs. In Crore
Maintenance Cost (Rs. In Crore)
Total Recurring Cost (Rs. In Crore)
1 Waste Water
Modification of ETP and getting membership of RO
0.5 1.4524 0.045 1.4974
Provision of RWH Pit
0.015 - 0.005 0.005
2 Air
Provision of APCS During Construction Phase
0.005 - 0.002 0.002
Installation of Stack/Vent & it‘s Monitoring Facilities and Provisio
0.3 0.032 0.003 0.035
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n of Air Pollution Control System
Provision of Odour Control System
0.01 0.0018 0.0002 0.002
Provision of VOC Detectors
0.015 0.0028 0.0002 0.003
Provision of CCTV Camera
0.01 0.0004 0.0001 0.0005
3 Hazardous Management
Getting Membership of TSDF Site
0.02 0.2016 - 0.2016
4 Fire & Safety
Provision of Safety Measures including Fire Detectors, Sensors, Alarm, Fire Hydrant, Fire Extinguishers, Lightening arrestors etc.
0.16 0.0326 0.0025 0.035
Provision of PLC based DCS type Automization
0.15 0.0208 0.0012 0.029
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system
5 AWH Monitoring
To conduct EMS efficacy & environment monitoring
- 0.02 - 0.02
6 Green Belt Development
Development of Greenbelt Area
0.05 0.0065 0.0005 0.007
7 Occupational Health
Provision of Occupational Health Centre with Antidotes
0.045 0.0185 0.0015 0.02
8 Noise
Installation of Acoustic Enclosure for D.G Set & Noise Control
0.01 0.0069 0.0006 0.0075
9 Provision of Solar Light within Plant Area
0.03 - 0.0004 0.0004
10 CER Activity 0.0696 0.005 0.0002 -
Total 1.3896 1.8013 0.0624 1.8654
Summary
Cost of Project in Crores per Annum: 6.00 Crores
EMP Capital Cost in Crores per Annum and
Percentage:
1.3896Crores
(23.16%)
EMP Recurring Cost in Crores per Annum
and Percentage:
1.8654Crores
(31.09%)
A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA,
CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times
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for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide
31.10.2019.)
% as per the OM
Rs. in Crores
2% 0.0696Crores
Brief note on proposed activities:
Sr. No.
Activities Location Year Budget
(Rs. In Lacs)
Basis Consideration
1. Provision of 15 Nos. Solar street light (Solar pole, battery, panel, LED light complete) on village road.
BhakrolVillage & Surrounding
villages* 2021 4.50
As per request received from Bakrol gram panchayat & surrounding
other villages on first cum first request
basis.
2. Provision of Dustbins at various internal village street, mosquito fogging machine.
2022 2.46
Total 6.96
B Land / Plot ownership details:
Land has been procured by GIDC, Ankleshwar. Letter No.
GIDC/SO/ANK/ALT/2154
B-1 Plot area
Existing
Proposed
Total
5000.00Sq. m. -- Sq. m. 5000.00Sq. m.
B-2 Brief note on Area adequacy in line to proposed project activities:
Unit is going for expansion of project and expansion will be carried out within
existing premises. Total plot area is 5000 m2.
At present, open space available within plant premises is also 2540 m2.
Unit will continue its existing production capacity as per consent is 39.02 MT/
Month.
Unit will manufacture any products on either and/or (Max 05 Products) basis but
the total production capacity of each group will not exceed as per mentioned
separately. Hence, additional production capacity will be 50.00 MT/Month.
Unit has proposed 0.10 MT/Month R & D Category product.
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Hence, Total Production capacity will be 89.12 MT/month
Presently, 130.00 m2 area is provided for production plant having floor in plant
(G+1) for production of ferric chloride plant and for proposed production, 300 m2
additional area will be provided having (G+2) So, total production plant area is
1160 m2.
At present, 50.00 m2area is allotted for storage of raw material having G+1 floor,
which is utilized for existing project. Additional 800 m2 area will be allotted for
storage of raw material having G+1 floor. Thus proposed RM storage area will
be 1700 m2.
At present for packing material & finished goods storage 70 m2 is allotted having
G+1 floor. For proposed expansion project, additional 126 m2 having (G+1) area
will be provided.
For utilities 100.0 m2 area is allotted will be utilized for expansion project.
Separate 20 m2 area is allotted for storage of hazardous/solid waste, and
additional 80 m2 area will be provided. So, total 100 m
2 area will be available for
HWSA.
B-3 Green belt area
Existing
Proposed
(Sq. meter)
Total
(Sq. meter)
Area in
Sq. meter
2010.00 Sq. m -- 2010.00 Sq. m
% of total
area
40.20 % -- 40.20 %
C Employment generation
Existing
Proposed
Total
16 (Male- 16,
Female- 00)
13 (Male- 13,
Female- 00)
29 (Male- 29,
Female- 00)
D WATER
D-1
Source of Water Supply
(GIDC, Bore well, Surface water, Tanker supply etc...)
GIDC, Ankleshwar
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Status of permission from the concern authority.
Unit will get permission from GIDC for additional water requirement
D-2
Water consumption (KLD)
Category
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(J) Domestic
0.50 0.81 1.31 --
(K) Gardening
0.10 4.70 4.80 --
(L) Industrial
Process 1.40 16.40 17.80 * Considering Maximum Water consumption will be take place in product no. 7
2‐Chloromethyl‐4‐methoxy‐3, 5‐dimethylpyridine hydrochloride
Washing - 2.00 2. 0 -
Boiler - 30.00 30.00 --
Cooling - 2.00 2.00 --
Others (Scrubber) - 2.00 2.00 --
Others (Fire
Hydrant)
- 0.89 0.89# #Considering
Fire water
requirements
once in a six
month due to
mock drill
Industrial Total 1.40 53.29 54.69
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Grand Total
(A+B+C)
2.00 58.80 60.80
Brief Note on worst case scenario for water consumption:
For Calculating Worst Case Scenario, Maximum process water consumption
will be take place in product no. 7 2‐Chloromethyl‐4‐methoxy‐3,
5‐dimethylpyridine hydrochloride.For worst case scenario, first of all product
water consumption is calculated by considering fully applied production
capacity. After that maximum water consumption took into consideration and
then divide quantity by number of working days per month. In addition
maximum boiler working hour, washing water requirement per day is also
taken into consideration. For in-house gardening around 4 L/m2 water is
considered. For domestic purposed around 45 Li/person/day water is
considered. Based on this our maximum water consumption shall not exceed
60.80 KLD.
-
Summary of water
requirement
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
Total water
requirement for
the project (A)
2.00 58.80 60.80
Quantity to be
recycled (B)
-- 34.42 34.42 --
Total fresh water
requirement (C) 2.00 24.38 26.38
Ensure Total water requirement = Fresh water + Recycled water
i.e. A = B + C
Reuse/Recycle details (KLD) with feasibility.
[Source of reuse & application area]
Source of waste
water for reuse
in KLD (From where
Application
area with
quantity in
Characteristics of
waste water to be
reused (COD, BOD, TDS
Remarks
regarding
feasibility
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it is coming) KLD (Where it is
used)
etc.) to reuse
RO Permeate –
17.92 KLD
Washing: 2.00
KLD
Cooling: 2.00
KLD
Scrubber: 2.00
KLD
Boiler: 11.92
KLD
COD <250 mg/L
BOD <90 mg/L
TDS <250 mg/L
Feasible for
Reuse
Boiler Condensed
Steam – 16.5-
KLD
Boiler Makeup
Water – 16.50
KLD
COD < 30 mg/lit
BOD < 10 mg/lit
TDS < 10 mg/lit
Feasible to
reuse
In case of no reuse/recycle of waste water, Give brief note on
justification as why no reuse/recycle.
Treated effluent will be utilized for preparation of dosing chemicals Solution
for ETP.
Treated effluent will be utilized in scrubber of APCS, attached with boiler flue
gas stack & same will allow in collection tank of ETP for its further treatment.
RO Permeate water (17.92 KLD) will be reused in Washing (2.00 KLD),
Cooling (2.00 KLD), Scrubber (2.00 KLD), Boiler (11.92 KLD).
D-3 Waste water generation (KLD)
Category
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(G) Domestic
0.50 0.55 1.05 --
(H) Industrial
Process 0.50 22.34 22.84** ** Considering Maximum Wastewater Generation will be from
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product no. 7 – 2‐Chloromet
hyl‐4‐methoxy‐3,
5‐dimethylpyridine hydrochloride
Washing -- 2.00 2.00 --
Boiler -- 1.35 1.35 --
Cooling -- 0.20 0.20 --
Others (Scrubber) - 0.54 0.54 --
Others (Fire
Hydrant)
- - -
Total Industrial
waste water
0.50 26.43 26.93
Brief Note on worst case scenario for waste water generation(Qualitative and
Quantitative):
Maximum Wastewater Generation will be from product no. 7 – 2‐Chloromethyl‐4‐methoxy‐3,
5‐dimethylpyridine hydrochloride. For worst case, first we have calculated waste water
generation from process for each products, as per fully applied quantity and from that we
have identified those products, which will generate more wastewater is carried out and same
is taken into consideration. In worst case we also have taken consideration boiler blow
down, cooling waste water and scrubber waste water including washing waste water. In any
case our industrial waste water generation shall not exceed 27.98 KLD.
Quality of Effluent-High COD Stream – Existing
Quality of Raw Effluent – After Expansion
Quality of Effluent-High COD Stream (24.84 KLD) – After Expansion
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Quality of Effluent-Low COD Stream (27.23 KLD)
NOTE: *Due to efficient removal of solvent in stripper. # Considering mixing of domestic, Low COD Stream & Solvent Free Effluent Stream with low COD effluent (11% dilution). ** Due to efficient removal of Organic matter in primary treatment.
Brief justification in case of no process effluent generation or no industrial effluent
generation or no high concentration effluent generation from proposed project
(Whichever is applicable).
Whichever is applicable).
Not Applicable
D-4 Mode of Disposal & Final meeting point (Existing and Proposed)
Existing and Proposed
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Domestic: Existing– Domestic effluent shall be disposed in to Septic tank / Soak pit
system.
Proposed– Domestic effluent shall be sent to ETP along with Low COD
industrial effluent.
Industrial: Existing – Industrial wastewater generated from process and other
ancillary operation is treated in to in-house for primary treatment and after
confirming CETP inlet norms it is send to CETP of M/s. ETL for the further
treatment and final disposal.
Proposed –Domestic and Industrial wastewater generated from
manufacturing process and other ancillary operation shall be segregated in
two different streams like low COD and high COD stream for which unit will
provide two separate collection tank for the same.
High COD stream of effluent (24.84 KLD) will be allow into ETP-1 for
primary (neutralization) treatment and then sent to solvent stripper to
remove mixed solvent. After than solvent free effluent (24.59 KLD) will be
mixed with domestic effluent (1.05 KLD) &Low COD stream of effluent (2.09
KLD) generated from boiler, cooling & scrubber will be allow in ETP-2 for
primary treatment to remove organic matter, VOC etc. From ETP – 2, 0.5
KLD treated water will be sent to CETP of M/s. ETL for further treatment and
final disposal. Unit has valid CTO/CCA. And remaining treated water (27.23
KLD) will be sent to In-house MEE from where water will be concentrated to
recover salt and condensed water. Condensed water will be allowed in RO
Plant. RO Reject water will be allowed to inlet of MEE for further treatment
and RO Permeate water will be reuse in washing, cooling, scrubber and
boiler. Hence, proposed expansion will be ZLD
-
Clearly mention about final disposal
D-5 Treatment facilities
For Domestic waste water: 1.05 KLD
Capacity of STP: Not Applicable (Domestic Water < 10 KLD)
For Industrial waste water: Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case
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of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.
In-house ETP 1 (High COD Stream) of Capacity 25.00 KLD will be installed having Primary
Treatment (pH Adjustment).
In-house ETP 2 (Low COD Stream) of Capacity 30.00 KLD will be installed having Primary
Treatment.
In Hose MEE of Capacity 2 m3/h
Quality of Effluent-High COD Stream – Existing
Quality of Raw Effluent – After Expansion
Quality of Effluent-High COD Stream (24.84 KLD) – After Expansion
Quality of Effluent-Low COD Stream (27.23 KLD)
NOTE: *Due to efficient removal of solvent in stripper. # Considering mixing of domestic, Low COD Stream & Solvent Free Effluent Stream with low COD effluent (11% dilution). ** Due to efficient removal of Organic matter in primary treatment.
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Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention
and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
Not Applicable. Unit will maintain ZLD for proposed expansion project.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
Domestic effluent shall be sent to ETP along with Low COD industrial effluent.
Industrial effluent generated from manufacturing process and other ancillary operation will be
allowed segregated in two different stream: Low COD and High COD
High COD stream of effluent (24.84 KLD) will be allow into ETP-1 for primary (neutralization)
treatment and then sent to solvent stripper to remove mixed solvent. After than solvent free
effluent (24.59 KLD) will be mixed with domestic effluent (1.05 KLD) & Low COD stream of
effluent (1.84 KLD) generated from boiler, cooling & scrubber will be allow in ETP-2 for
primary treatment to remove organic matter, VOC etc. From ETP – 2, 0.5 KLD treated water
will be sent to CETP of M/s. ETL for further treatment and final disposal. Unit has valid
CTO/CCA. And remaining treated water (27.23 KLD) will be sent to In-house MEE from where
water will be concentrated to recover salt and condensed water. Condensed water will be
allowed in RO Plant. RO Reject water will be allowed to inlet of MEE for further treatment and
RO Permeate water will be reuse in washing, cooling, scrubber and boiler. Hence, proposed
expansion will be ZLD
D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility (CF) (For waste water treatment)
CETP: M/s ETL, Ankleshwar.
Membership of Common facility (CF) mentioning total capacity, consented quantity,
occupied capacity and spare capacity and norms of acceptance of effluent from
member unitsin-line with the direction given by GPCB vide Letter No.
GPCB/P-1/8-G (5)/550706 dated 08/01/2020.
Unit has membership form M/s. ETL for wastewater disposal letter no
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ETL/ANK/2009/519 dated 01/08/2009
D-7 Simplified water balance diagram with reuse / recycle of waste water
(Existing and Proposed)
WATER BALANCE DIAGRAM (EXISTING – As Per CCA))
FOR EXISTING PRODUCTS AFTER EXPANSION
E AIR
E-1 Brief Note on fuel based Heat energy requirement and worst case
scenario thereof:
Electric power requirement for project is 125 KVA. After expansion, One D. G. Set of capacity
100 KVA will be installed.
After Expansion, boiler of Capacity 1.5 TPH will be installed.
Maximum steam required from Steam Boiler will be around 1200 kg/hr.
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Fuel Requirement:
Existing: Solid – Steam Coal – 0.3 MT/Day
Additional: Gaseous – Natural Gas - 3000 m3/Day Or Solid – Briquettes of Bio Coal – 5.5
MT/day
E-2 Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the
MOEFCC‘s OM vide dated 31.10.2019)
Existing & Proposed
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions
i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
EXISTING
1. Furnace 30.0 m Steam
Coal
0.3
MT/day
PM, SO2,
NOX
Adequate stack
height provided
PROPOSED
2. Boiler (Capacity: 1.5 TPH )
30.0 m
Natural Gas OR
3000
m3
/day
PM, SO2,
NOX
Adequate stack height will be
provided
Briquettes of Bio Coal
5.5 MT/Day
PM, SO2,
NOX
Multi Cyclone Separator +
Water Scrubber
3.
D. G. Set (Stand by) (Capacity: 100 KW
7.0 HSD 27 Lit/h PM, SO
2,
NOX
Adequate stack height will be
provided
E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
Existing & Proposed
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emissions
i.e. Air Pollutants (SO2, HCl, Cl
etc.)
Stack/Vent Height (meter)
Air Pollution Control Measures (APCM)
EXISTING
1 Reactor HCl/ Cl2 30.0
Two Stage Water Scrubber followed by Alkali Scrubber
PROPOSED
2 Reaction Vessel (Product No. 6, 7 Process: Sulphonation#)
HCl 20.0 Two Stage Water Scrubber followed by Alkali Scrubber
3 Reaction Vessel (Product No. 3, 5, 6, 7, 8 Process: Sulphonation)
SO2 20.0 Two Stage Alkali Scrubber
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4 Reaction Vessel (Product No. 6 Process: Amination)
NH3 20.0 Two Stage Water Scrubber
5 Reaction Vessel (Product No. 1, 4, 7 Process: Nitration)
NOx 20.0
Adequate Stack Height will be provided
Note:
Details of gaseous raw materials used in proposed project
No any Gaseous RM will be used
Estimation of process gas emission (Product wise and Total)
Sr. No.
Product No. Type of
emission Max. Emission
(MT/Day)
1. 3 SO2 0.08
2. 5 SO2 0.09
3. 6
SO2 1.35
HCl 1.03
NH3 0.01
4. 7 SO2 0.51
HCl 0.03
5. 8 SO2 0.01
Requirement of the scrubbing media (KL per Day) considering solubility (Product wise
and Total)
Sr. No.
Type of emission Name of Scrubbing Media Requirement of
Scrubbing media (Kl/Day)
1. HCl Two Stage Water Scrubber
followed Alkali Scrubber 2.40
2. SO2 Two Stage Alkali Scrubber 3.16
3. NH3 Two Stage Alkali Scrubber 0.02
Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its
sound management in HW matrix.
Sr. No.
Type / Name of Hazardous waste
Specific Source of generation (Name
of the Activity, Product etc.)
Total Quantity (MT/Year)
Management of HW
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1. Sodium Sulfite (25- 41 %)
Scrubber
(Product No. 3, 5, 6, 7, 8)
1624.08
Collection, Storage, Transportation (through GPS mounted vehicle) and Disposed by selling to authorized end user whom have valid permission from GPCB as per Haz. Waste Rule-9
-
E-4 Fugitive emission details with its mitigation measures.
Raw materials will be stored in isolated storage area and containers will be kept tightly closed. To
minimize fugitive emission, powder material will be allowed in a vessel through closed loop while
liquid material will be charged through closed pipeline.
Manufacturing activity will be carried out in closed reactors / vessels and regular checking and
maintenance of the same will be carried out to avoid any leakages.
Transportation of raw materials & products will be carried out by trolley within premises and
minimum manual material handling will be carried, so the fugitive emission due to process activity
and material handling will be minimized.
To minimize fugitive emission due to vehicle movement, regular water sprinkling will be carried out
on road and paved road will be maintained.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
Note:
Priorities for HW Management: Pre-processing, Co-Processing,
Reuse/Recycle within premises, Sell out to actual users having Rule-9
permission, TSDF/CHWIH.
Quantification of hazardous waste shall be based on mass balance and
calculations shall be incorporated in EMP details separately.
Disposal to scrap vendors/vendors/traders is not allowed
F-1 Hazardous waste management matrix
Existing & Proposed
Sr. no.
Type/ Name of
Hazardous waste
Specific Source of generation(Name of
the Activity, Product etc.)
Category and
Schedule as per
HW Rules.
Quantity (MT/Annum)
Management of HW Existing
Proposed
Total
1 Process
Waste Process 13.20 0.18 - 0.18
Collection, Storage,
Transportation &
Disposal at TSDF
BEIL
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2
Empty
Barrels /
Container
s / Liners
contamin
ated with
hazardou
s
chemicals
/ Wastes
Raw
Materials
&
Finished
Products
33.1
(Sch. I) - 40.00 40.00
Collection, Storage,
Transportation
(Through GPS
Mounted Vehicles)
and Disposal by
selling to registered
recycler approved by
GPCB / CPCB /
reuse within
premises
3 ETP
Sludge
Effluent
Treatme
nt Plant
35.3
(Sch. I) - 81.89 81.89
Collection, Storage,
Transportation
(Through GPS
Mounted Vehicles)
and Disposal at
TSDF site – for
secured landfill
4 MEE Salt MEE
Plant
35.3
(Sch. I) - 317.45
317.4
5
Collection, Storage,
Transportation
(Through GPS
Mounted Vehicles)
and Disposal at
TSDF site – for
secured landfill
5 Used or
Spent Oil
D. G. Set
&
Machiner
y
5.1
(Sch. I) - 2.50 2.50
Collection, Storage,
Transportation
(Through GPS
Mounted Vehicles)
and Disposal by
selling to Registered
Re-refiners approved
by GPCB / CPCB
/reuse for lubrication
6 Spent
Solvent
Process
(Product
No. 1, 6,
7)
28.6
(Sch. I) - 5702.46
5702.
46
Collection, storage,
recovered through
in-house distillation
and 100 % reuse
within premises in
(Product No. 1, 6, 7)
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7 Mixed
Solvent Stripper
28.6
(Sch. I) - 90.00 90.00
Collection, Storage,
Transportation
(through GPS
mounted vehicle)
and Disposed by
selling to authorized
end user whom have
valid permission from
GPCB as per Haz.
Waste Rule-9
8 Distillation
Residue
Process
Distillatio
n
(Product
No. 1, 6,
7)
20.3
(Sch. I) - 36.36 36.36
Collection, Storage,
Transportation
(Through GPS
Mounted Vehicles)
and Disposal for
incineration for
existing quantity and
proposed quantity
will be sent for co-
processing
9
Sodium
Bisulfate
(20 –
30%)
Process
(Product
No, 5)
28.1
(Sch. I) - 797.34
797.3
4
Collection, Storage,
Transportation
(through GPS
mounted vehicle)
and Disposed by
selling to authorized
end user whom have
valid permission from
GPCB as per Haz.
Waste Rule-9
10 Sodium
Sulfite
Scrubber
(Product
No. 3, 5,
6, 7, 8)
28.1
(Sch. I) - 1624.08
1624.
08
Collection, Storage,
Transportation
(through GPS
mounted vehicle)
and Disposed by
selling to authorized
end user whom have
valid permission from
GPCB as per Haz.
Waste Rule-9
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11
Dil. HCl
Solution
(10 -
25%)
Scrubber
(Product
No. 6, 7)
28.1
(Sch. I) - 739.32
739.3
2
Collection, Storage,
Transportation
(through GPS
mounted vehicle)
and Disposed by
selling to authorized
end user whom have
valid permission from
GPCB as per Haz.
Waste Rule-9
12
Liquor
Ammonia
(10 –
25%)
Scrubber
(Product
No. 6)
28.1
(Sch. I) - 12.12 12.12
Collection, Storage
and
entire 100% quantity
will be reuse in
process
(Product No. 6)
13
Off
Specificati
on
Products
Mfg.
Process
(Batch
Failure)
28.4
(Sch. I) -- 1.00 1.00
Collection, Storage,
Transportation
(Through GPS
Mounted Vehicles)
and Disposal co-
processing
-
F-2 Membership details of TSDF, CHWIF etc.
(For HW management)
Details of Membership letter no. & Date with spare capacity of the Common Facility.
Unit has taken membership for TSDF site of M/s. BEIL. Ankleshwar dated 03/08/2009.
Unit has obtained NOC membership for TSDF & co-processing site of M/s. BEIL. Ankleshwar
for proposed waste generation.
F-3 Details of Non-Hazardous waste & its disposal
(MSW and others)
Sr. no.
Type/Name of Other wastes
Specific Source of generation (Name of the Activity, Product etc.)
Quantity (MT/Annum)
Management of Wastes
Existing Proposed Total
1 Fly Ash Boiler & APCS
-- 198.00 198.00
Collection, Storage, Transportation (through GPS mounted vehicles) & Disposal by selling to Cement /Brick manufacturing unit/ Local road contractor.
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Sr. No.
Type of Waste Source of
Generation
Category of
Waste Disposal
1. Concrete and Bricks material
Proposed construction
activity
C & D Waste
Temporary store, reuse to increase plinth level and in road area
Steel, glass, wood To be sell local scrap vendor
2. Domestic Waste (Food waste, Plastic, Paper etc.)
Employees working in the
premises
MSW Collected in separate bin and disposed to bin of GIDC.
3. Industrial Waste (Glass wool [Insulating Material, Scrap])
Steam Pipe & Vessels
ISW Sell to local scrap vendor
4. Industrial Waste (Wooden pellets)
From Raw Material
&Product storage area
ISW Sell to local scrap vender
5. E-waste Entire Plant E-waste Collection, Storage and disposal to GPCB authorized E-Waste Management facility
G Solvent management, VOC emissions etc.
G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse
of recovered Solvents etc.
In-house solvent recovery plant will be installed and recovered solvent will be again
reused in process and residue will be disposed for co-processing.
Type of solvents % recovery % Losses
Air Water Haz
Ethylene DiChloride 97.57 0.1215 0.243 1.8225
Meta dichloro benzene 98.65 0.0675 0.135 1.0125
Methanol 96.5 0.175 0.35 2.625
Methylene Dichloride 97.88 0.106 0.212 1.59
Toluene 98.93 0.0535 0.107 0.8025
G-2 Brief Note on LDAR proposed:
LDAR programs will be done by Instrument monitoring and Physical inspection.
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Physical inspections will be done for heavy liquids below the vapor pressure thresholds.
Physical inspections rely on the visual detection of dripping liquids.
In In addition to LDAR program, following safety measures will be taken to prevent losses of
solvent in atmosphere;
To achieve more than 95% recovery, unit will provide vacuum distillation, double
condensers with second condenser using chilled water as cooling media. The
condensers shall be provided with sufficient Heat Transfer Area and residence time
for maximum recovery.
VOC detectors will be installed to detect any solvent leakages during storage and
handling.
In warding, storage and consumption of solvents in various products shall be
measured through Level Transmitters and Load cells weighing systems resp. The
quantity at each stage shall be reconciled periodically to arrive at Losses.
Periodic monitoring of work area will be carried out to check the fugitive emission.
G-3 VOC emission sources and its mitigation measures
Source: VOCs generation will be from storage and usage of raw materials.
VOC analysers will be provided to detect any solvent leakages during storage and handling.
Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to
prevent leakages and thus minimizing the fugitive emissions of VOCs.
Entire process will be carried out in the closed reactors with proper maintenance of pressure
and temperature.
Ensure minimum number of flanges, joints and valves in pipelines.
Proper preventive maintenance of roofs and seals for tanks
Monitoring and preventive maintenance of valves, flanges, joints, etc.
VOC detectors will be installed to detect any solvent leakages during storage and handling.
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Justification of Reuse of solvent
Name of Solvent Total requirement Total quantity of solvent recovered
Ethylene DiChloride 33.00 32.20
Meta dichloro benzene 237.41 234.20
Methanol 2750.00 2653.75
Methylene Dichloride 2104.85 2060.23
Toluene 172.70 170.85
H SAFETY details
H-1 Details regarding storage of Hazardous chemicals
(For tank storages only including spent acid and spent solvent tanks)
-
Sr. no Name of Chemical Capacity of
Tank
Number of
Tanks
Hazardous
Characteristi
cs of
Chemical
-- -- -- -- --
Brief note on storage of Hazardous chemicals in Tanks
Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels,
Carboys, Bags etc.
Safety Precaution for storage & Handling of Methanol:
Methanol is Flammable. Vapors may form explosive mixtures with air. Vapors may travel to
source of ignition and flash back. Containers may explode when heated. Vapors may form
explosive mixtures with air.
Keep in a dry, cool and well-ventilated place. Keep Tank tightly closed in a dry and well-
ventilated place. Keep away from heat and sources of ignition. Proper and sufficient fire
fighting arrangement will be provided in and around the storage.
Avoid contact with skin and eyes. Do not breathe vapors or spray mist. Remove all sources of
ignition. Use only non-sparking tools.
Wash hands before breaks and immediately after handling the product. Keep away from open
flames, hot surfaces and sources of ignition.
To avoid ignition of vapors by static electricity discharge, all metal parts of the equipment
must be grounded. Take precautionary measures against static discharges. Adequate
earthing shall be provided during unloading & its transfer.
Safety Precaution for Storage & Handling of Acetic Anhydride:
Acetic Anhydride is a highly corrosive chemical and contact can severely irritate and burn the
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skin and eyes with possible eye damage. Breathing Acetic Anhydride can irritate the nose,
throat and mouth. High concentration can cause severe lung damage with coughing. It can
cause skin allergy.
Store in tightly closed drum in a cool, dry and well-ventilated area. Keep away from
heat/sparks/open flames/hot surfaces. Keep away from water.
Safety shower and eye washer will be provided nearby storage area.
Personnel working with Acetic Anhydride should be trained on its proper handling and
storage. Proper personal protective equipment such as gloves, safety goggles and face mask
shall be provided.
Safety Precaution for Storage and Handling of Liquid Ammonia:
Avoid contact with skin and eyes. Avoid inhalation of vapour or mist.
Store in cool place. Keep container tightly closed in a dry and well-ventilated place.
Containers which are opened must be carefully resealed and kept upright to prevent leakage.
Storage area have cross air ventilation, no direct sun light, storage temp. below 40 deg. C.
Safety Precaution for Storage & Handling of Nitric Acid
Nitric acid will be stored in Drum. Storage Drum will be stored away from the process plant.
During handling of nitric acid, adequate PPE‘s will be provided to worker like chemical safety
glasses, a face shield for splash protection, gloves etc.
Tanker unloading procedure will be prepared and implemented. The unloading area should
be built in such a way that acid from leaks, spillage and overflow will be collected and led to a
safe place.
The hose material and the couplings used for unloading must not react with nitric acid (for
example, bronze couplings are unsuitable).
Caution note and emergency handling procedure will be displayed at unloading area and
trained all operators.
NFPA label will be provided.
Safety shower, eye wash with quenching unit will be provided in storage area.
Vehicle drivers who transport nitric acid by road must carry the protective equipment which is
specified in the TREM card for road traffic, readily available in the vehicle.
Safety details of Hazardous Chemicals:
Type of
Hazardous
Chemicals
Safety measures
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Explosive Standard Operating procedure shall be made for before Gas
charging into reactor and after completion of reaction
SOP will be prepared and operators will be trained for the
same..
Safety valve and Rupture disc will be provided on reactor.
Safe Catalyst charging method will be adopted.
Flame arrestor will be provided on vent line of reactor and it will
be extended above the roof level.
Static earthing and electric earthing (Double) will be provided.
Gas detector will be installed for early detection of gas leak.
Toxic and
Corrosive
Storage area have cross air ventilation, no direct sun light,
storage temp. below 40 deg. C.
Containers which are opened must be carefully resealed and
kept upright to prevent leakage.
Charging in reactor shall be carried out through vacuum pump.
Avoid contact with skin and eyes. Avoid inhalation of vapour or
mist. during handling using protective gloves/ protective
clothing/ eye protection / face with proper respiratory
protection. Proper label and identification board /stickers will be
provided in the storage area. Safety showers and eye wash
stations will be installed near the storage area.
Flammable Keep in a dry, cool and well-ventilated place. Keep Tank tightly
closed in a dry and well-ventilated place.
Keep away from heat and sources of ignition. Flammables
area.
Avoid contact with skin and eyes. Do not breathe vapors or
spray mist. Remove all sources of ignition. Use only non-
sparking tools.
Wash hands before breaks and immediately after handling the
product. Keep away from open flames, hot surfaces and
sources of ignition.
To avoid ignition of vapors by static electricity discharge, all
metal parts of the equipment must be grounded. Take
precautionary measures against static discharges.
Dyke wall will be provided at tank storage area.
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Applicability of PESO : Will be taken
H-2 Types of hazardous Processes involved and its safety measures:
(Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)
-
Type of
Process
Safety measures including Automation
Nitration
process
Nitration will be done in closed S.S vessels.
Nitric acid will be used for nitration process. Nitric acid is an
extremely corrosive acid capable of causing severe chemical
burns very rapidly. Because of the hazards posed by nitric acid, it
is important to take safety measures whenever handling it.
In our nitration process, exothermic reaction will be controlled by
adequate dosing of reaction chemicals in a fixed time (not short
duration) having adequate cooling water circulation in jacket of
reaction vessels. Thus, any energy generated due to exothermic
reaction will be controlled by external cooling circulation and
therefore vessels will not be pressurized.
The nitration reaction will be controlled by systematic cooling
design to withdraw the energy evolved.
Adequate pressure relief valve will be provided for each vessels
having pressure release capacity will be kept below -3 kg/cm2than
that of reaction vessels.
Exothermic
Reaction
Exothermic reaction will be controlled by adequate dosing of reaction
chemicals in a fixed time (not short duration) having adequate cooling
water circulation in jacket of reaction vessels. Thus, any energy
generated due to exothermic reaction will be controlled by external
cooling circulation and therefore vessels will not be pressurized.
H-3 Details of Fire Load Calculation
-
Total Plot Area: 5000.00 Sq. meter
Area utilized for plant activity: 430.00 Sq. meter
Area utilized for Hazardous Chemicals
Storage:
100.00 Sq. meter
Number of Floors: G + 2
Water requirement for firefighting in KLD : 5652Ltr
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Water storage tank provided for firefighting in
KLD:
Existing: 50000 Ltr Proposed: 150000 Ltr
Details of Hydrant Pumps: 2
Nearest Fire Station : Fire Station,
Ankleshwar GIDC:
2.25 km
Applicability of Off Site Emergency Plan: Will be Prepared
-
H-4 Details of Fire NOC/Certificate:
Unit will take fire NOC after getting EC
H-5 Details of Occupational Health Centre (OHC):
-
Number of permanent Employee : 10
Number of Contractual person/Labour : 19
Area provided for OHC: 30 Sq. m.
Number of First Aid Boxes : 20
Nearest General Hospital : General Hospital, Ankleshwar 0.50 km
Name of Antidotes to be store in plant : Diazem – 1 mg/Kg.(Intravenous)
Epinephina, Efidrine, Ethanol, Milk of
Magnesia, Soda Water, Castor Oil,
Soframycine, Hydrocortisone (200 mg at
every 4 hrs.). Milk of Magnesia, Ascorbic
acid for eye injury; Paracetamol for Gastric
damage effect.
During the meeting dated 17.12.2020, the project was appraised based on the information furnished in
Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.
Project proponent (PP) and Technical expert of PP, M/s. Envirocare Technocrats Pvt. Ltd remains
present during video conference meeting.
Committee noted that the proposal is for expansion project in GIDC Ankleshwar. Unit is having valid CCA
of the Board for existing plant. Committee noted that self certified compliance report of CCA is submitted
by the unit. PP submitted details regarding area adequacy. Source of water is GIDC. Product profile
along with end use discussed in depth. Committee insisted for R & D production capacity in Kg/Month
and PP later on submitted revised product profile with mentioning R & D product capacity-100 Kg/Month.
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Committee noted that PP has submitted undertaking regarding there is no legal court case and public
complaint against unit. PP informed that two Show cause notice (SCN) issued by GPCB in last three
years and compliance reply of SCN presented by the unit. Looking to plot area and existing inorganic
production plant and proposal of new API products, Committee insisted for submit revised layout plan
with mentioning separate existing and proposed production plant and floor wise emergency stair case in
different location of plant area which is later on submitted by PP.
Committee noted that PP has submitted waste water management and industrial effluent will be
segregated. High COD stream will be passed treated in ETP-1 and then mixed with low COD stream for
further treatment. Low COD stream along with treated high COD stream will be treated in ETP -2 and
partly treated effluent will be sent to CETP of M/s ETL for further treatment and rest of treated effluent
will be evaporated in in-house MEE.MEE condensate will be further treated in RO Plant. Committee
asked for compliance of Direction under section 18(1) (B) ,PP informed that waste water discharge
quantity is not increase after expansion and also mentioned quality of waste water discharge with stage
wise reduction of BOD, COD, Ammonical nitrogen and TDS in ETP and MEE.
PP submitted that they have proposed boiler and DG set. Fuel used will be Natural gas or bio coal for
boiler. MCS and water scrubber as APCM proposed for bio coal fired boiler. Committee insisted for
adequate stack height for coal fired furnace and PP later on submitted revised stack height of 30 meter
for coal fired furnace. Two stage scrubbers will be provided as APCM with each process reactor stack.
PP submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.
Upon asking regarding provision of fire hydrant network and proposed fire extinguishers details, PP has
addressed the Site Plan/layout plan with provision of fire hydrant network, periphery road with entry and
exit separately, proposed fire extinguishers details adequate fire water reservoir and fire load calculation.
Committee noted that PP has addressed fire evacuation plan, worker‘s safety and occupational Health
centre (OHC) and process hazard and its safety control measures. Committee noted that PP presented
details of auto control system like PLC with SCADA system. Committee insisted for provision of Proximity
suit & Trolley pump and provides the Fire water Storage tank capacity of 200 KL and PP later on
submitted revised fire water tank and fire extinguisher details.
Committee deliberated on storage and safety aspects of hazardous chemicals, green belt area, EMP,
CER, LDAR and solvent recovery etc.
Committee found submission of project proponent satisfactory.
After detailed discussion, Committee unanimously decided to recommend the project to SEIAA,
Gujarat for grant of Environment Clearance
SPECIFIC CONDITIONS:
1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon‘ble Supreme Court of
India in Civil Appeal no. 8478/2020 regarding operation of the Hon‘ble NGT orders dated 10/07/2019
& 14/11/2019.
2. PP shall comply conditions of any subsequent amendment or expansion or change in product mix,
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after the 30th March 2021, considered as per the provisions in force at that time as mentioned in the
Notification vide S.O. 1223 (E) dated 27/03/2020 and S.O. 3636 (E) dated 15/10/2020.
3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients (API) as
per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any subsequent
amendments.
4. PP shall submit six monthly compliance report of Environmental Clearance without fail and the same
shall be critically assessed by the regulatory authority.
5. GPCB shall ensure compliance of direction under section 18 (1) (b) of the Water (Prevention and
Control of Pollution) act, 1974 issued by CPCB regarding compliance of wastewater disposal from
common ETP and also that the pollution load is not increased in the CPA/SPA for the compliance of
Hon‘ble NGT order.
6. PP shall use natural gas for utilities preferably but in case use of other fuel, PP shall put properly
designed APCM with regular/periodic stack monitoring system to ensure that there shall be no
increase in pollution load for the compliance of directives of Honorable NGT.
7. Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB directions to all
SPCB vide letter no. B-29016/04/06PCI-1/5401 dated 05/02/2014 for effluent discharge and air
emission as per pollutants discharge/emission from respective project and an arrangement shall also
be done for reflecting the online monitoring results on the company's server, which can be
assessable by the GPCB/CPCB on real time basis. [For Small/Large/Medium (Red Category) &
Whichever (Air emission & Effluent discharge) is applicable].
8. Wastewater shall be fed to MEE only after providing adequate treatment in such a way that no
pollutant get air borne during evaporation to avoid adverse impact on Human Health & Environment.
9. The PP shall develop green belt [2010 m2 inside plant premises i.e. 40.09 % of total plot area] as per
the undertaking submitted before SEAC. Green belt shall be developed with native plant species that
are significant and used for the pollution abatement as per the CPCB guidelines. It shall be
implemented within 3 years of operation phase in consultation with GPCB.
10. Domestic wastewater generation shall not exceed 1.05 KL/day for proposed project and it shall be
treated in ETP. It shall not be disposed off in soak pit and septic tank.
11. Close loop solvent recovery system with adequate condenser system shall be provided to recover
solvent vapours in such a manner that recovery shall be maximum and recovered solvent shall be
reused in the process within premises.
12. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB
guidelines. LDAR Logbooks shall be maintained.
13. The unit shall submit the list of authorized end users of hazardous wastes along with MoU signed
with them at least two months in advance prior to the commencement of production. In the absence
of potential buyers of these items, the unit shall restrict the production of the respective items.
14. Unit shall obtain all required permissions from the Narcotics Control Bureau for manufacturing,
storage and handling of Acetic Anhydride & any such chemicals.
15. Safety and Health:
a) PP shall obtain PESO permission for the storage and handling of hazardous chemicals. (If
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applicable)
b) PP shall provide Occupational Health Centre (OHC) as per the provisions under the Gujarat
Factories Rule 68-U.
c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the concern
authority as per the prevailing Rules / Gujarat Fire Prevention and Life Safety Measures Act,
2016.
d) Unit shall adopt functional operations/process automation system including emergency
response to eliminate risk associated with the hazardous processes.
e) PP shall carry out mock drill within the premises as per the prevailing guidelines of safety and
display proper evacuation plan in the manufacturing area in case of any emergency or
accident.
f) PP shall install adequate fire hydrant system within premises and separate storage of fire
water and foam for the same shall be ensured by PP. Also PP shall provide alarm system in
nearby fire station for emergency of any fire in plant area.
g) PP shall take all the necessary steps for control of storage hazards within premises ensuring
incompatibility of storage raw material and ensure the storage keeping safe distance as per
the prevailing guidelines of the concerned authority.
h) PP shall take all the necessary steps for human safety within premises to ensure that no any
harm is caused to any worker/employee or labor within premises.
i) Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.
j) Unit shall provide water sprinkler in Ammonia storage area.
k) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam
pouring system etc. to restrict cascade fire emergency in solvent tank farm.
l) Unit shall provide safety valve and rapture disc, as well as auto dump or auto quenches/,
suppresses system for nitration reaction vessel safety.
11. SIA/GJ/IND2/57519/2020 M/s. Krimson Polymers LLP
Survey No. 67/2/Paiki, 2 Plot No.1, Shika
rpur, Ta: Bhachau, Dist:
Kutchh
Screening and scoping
Category of the unit: 5(f)
Project status: New
This office has received an application vide their online proposal no. SIA/GJ/IND2/57519/2020 dated
17/11/2020 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for
preparation of EIA/EMP report.
Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
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This is a new unit and proposes for manufacturing of synthetic organic chemicals as tabulated below,
Sr.
No.
Name of the
Products
CAS no. /CI
no.
Quantity
MT/Month
End-use of the products
1 Chloranil 118-75-2 20
In chemical Industries and
in Textile Industries for
printing and dyeing.
2 Carbazole 86-74-8 10
3 Pigment Violet 23 6358-30-1 20
4 Pigment Red 122 980-26-7 20
5 Pigment Yellow 138 30125-47-7 20
Total 90
The project falls under Category B1 of project activity 5(f) as per the schedule of EIA Notification 2006.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020.
Project proponent and technical expert of PP, M/s. Enviro Fluid Consultants remains present during
video conference meeting dated 17/12/2020.
Committee noted that this is Greenfield project at Survey No. 67/2/Paiki 2, Plot no. 1, Village: Shikarpur,
Taluka: Bhachau, District: Kutch. Unit is located outside Notified area.
Committee noted that prefeasibility report (PFR) for proposed synthetic organic chemical product is
prepared by M/s. Enviro Fluid Consultants and they are not accredited as per the Amended EIA
Notification videS.O.648 (E) dated 03/03/2016.
Committee took a note of Minutes of meeting of EAC, MoEF&CC (IA Division-Industry-2 Chemical
sector) dated 24/11/2020. MoEF &CC has insisted on QCI/NABET accredited consultants. While
examining the B1 category of applications, it has refused to consider/entertain the proposals which were
not prepared by QCI/NABET accredited consultants.
In view of the above and after deliberations, it is felt that SEAC shall not consider/entertain Terms of
Reference(ToR) application as it is a part of EIA preparation for B1 category wherein prefeasibility report
prepared by consultant, not accredited with QCI/NABET as per the Amended EIA Notification
videS.O.648 (E) dated 03/03/2016.
After detailed discussion, Committee unanimously decided to defer the project and consider the
same in one of the upcoming meeting of SEAC after satisfactory submission of following details:
1. Prefeasibility report for proposed project shall be prepared by EIA consultants having accreditation
with QCI/NABET as per the Amended EIA Notification vide S.O.648 (E) dated 03/03/2016.
2. Status of EIA Consultant for accreditation with QCI/NABET as per the Amended EIA Notification
vides S.O.648 (E) dated 03/03/2016 for proposed project.
12. SIA/GJ/IND2/55602/2020 M/s. Umiya Enterprise
Plot No. 131, GIDC Talod, Ta. Talod, Dist.
Sabarkantha
Screening and scoping
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Category of the unit: 5(f)
Project status: New
This office has received an application vide their online proposal no. SIA/GJ/IND2/55602/2020 dated
21/10/2020 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for
preparation of EIA/EMP report.
Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
This is a new unit and proposes for manufacturing of synthetic organic chemicals as tabulated below,
Sr. No.
Name of Product CAS No. Quantity
MT/Month Final Application
of Product
1. Reactive Yellow HE4G 59112-78-6
45
Most suitable for dyeing of cellulosic fibers like cotton, flax, viscose rayon, acetate and jute, Applicable on Leather and Paper coloration.
2. Reactive Yellow H7GL 61969-35-5
3. Reactive Yellow HE6G 77907-38-1
4. Reactive Yellow ME4GL 129898-77-7
5. Reactive Golden Yellow HR 35642-64-9
6. Reactive Golden Yellow MERL
93050-80-7
7. Reactive Green HE4BD 61931-49-5
8. Reactive Red HE3B 61951-82-4
9. Reactive Red HE7B 61931-52-0
10. Reactive Red HE8B 71870-80-5
11. Reactive Red ME4BL 93050-79-4
12. Reactive Red ME6BL 125830-49-1
13. Reactive Orange ME2RL 79809-27-1
14. Reactive Orange HER 91261-29-9
15. Reactive Orange 2R 42986-20-1
16. Reactive Magenta HB ---
17. Reactive Violet C4R 12237-11-5
18. Reactive Black B 17095-24-8
19. Direct Black 168 85631-88-5
20. Direct Red 12B 5001-72-9
21. Acid Red 97 61901-18-6 Acid dyes are used to dye protein fibers such as wool, angora, cashmere, and silk, as well the milk protein fiber called Silk Latte, the soy protein fiber called Soy Silk, and the synthetic polyamide fiber nylon in textile industries.
22. Acid Blue 113 33351-05-1
23. Acid Blue 193 12392-64-2
24. Acid Brown 75 8011-86-7
25. Acid Brown 282 12219-65-7
26. Acid Brown 365 63641-88-3
27. Acid Brown 355 60181-77-3
28. Acid Black 194 61931-02-0
The project falls under Category B1 of project activity 5(f) as per the schedule of EIA Notification 2006.
The proposal was considered in the SEAC video conference meeting dated 17.12.2020.
Salient features of the project including Water, Air and Hazardous waste management as below.
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Sr.
no.
Particulars Details
A
A Total cost of Proposed Project
(Rs. in Crores):
1.10 Crores
B Total Plot area ( sq. meter) 1000 Sq. m.
Green belt area
( sq. meter)
120 Sq. m. (12 %) & remaining 21%
green belt area will be develop in
GIDC area after obtaining permission
of association.
C Employment generation 10
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Water Supply
Status of permission from the concern authority. ---
ii Water consumption (KLD)
Category
Quantity
KLD
Remarks
(M) Domestic 1.0
(N) Gardening 1.0
(O) Industrial
Process 9.0
Washing 1.0
Boiler 2.0
Cooling 1.0
Industrial Total 13.0
Total (A + B + C) 15.0
1) Total water requirement for the project: 15.0 KLD
2) Quantity to be recycled: 8.3 KLD
3) Total fresh water requirement: 6.7 KLD
(Total water requirement = Fresh water + Recycled water)
15.0 = 6.7 + 8.3
iii
Waste water generation (KLD)
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Category Waste water
KLD
Remarks
(I) Domestic 0.8
(J) Industrial
Process 10.5
Washing 1.0
Boiler 0.2
Cooling 0.1
Total Industrial waste
water
11.8
Total [A + B] 12.6
-
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
In house ETP (Primary) & RO Plant
Treatment scheme including segregation at source.
Total Industrial Wastewater generation will be 11.8 KLD and will be send to ETP Plant. After
treated effluent will be send to RO plant. RO Permeate water 8.3 KLD will be reuse for industrial
activity and RO rejected water 3.5 KLD will be send to common spray dryer at Chhatral
Environment Management System Pvt. Ltd. Dhanot for spray drying.
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control
of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
No CETP discharge
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
Unit will achieve zero liquid discharge by discharge proposed effluent to common spray dryer.
v Mode of Disposal & Final meeting point
Domestic:
Send to Modular STP Plant & treated effluent will send to CEMSPL for spray
drying
Industrial:
Total Industrial Wastewater generation will be 11.8 KLD and will be send to ETP
Plant. After treated effluent will be send to RO plant. RO Permeate water 8.3
KLD will be reuse for industrial activity and RO rejected water 3.5 KLD will be
send to common spray dryer at Chhatral Environment Management System Pvt.
Ltd. Dhanot for spray drying.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of
CF
Chhatral Environment Management System Pvt. Ltd. Dhanot
Membership of Common facility (CF)
(For waste water treatment)
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Chhatral Environment Management System Pvt. Ltd. Dhanot
vii Simplified water balance diagram with reuse / recycle of waste water
viii Reuse/Recycle details (KLD)
Total reuse KLD
Source of waste
water for reuse
with quantity in
KLD (From where
it is coming)
Application
area with
quantity in KLD
(Where it is
used)
Characteristics of waste
water to be reused
(COD, BOD, TDS etc.)
(mg/L)
Remarks
regarding
feasibility to
reuse i.e.
8.3 KLD Reuse Industrial
Activity
COD – 24
BOD – 6
TDS - 100
--
E Air
i Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
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-
Sr.
no.
Source of
emission
With
Capacity
Stack
Height
(meter)
Type
of
Fuel
Quantity
of Fuel
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air
Pollution
Control
Measures
(APCM)
1
Steam Boiler (800
Kg/Hr)
11 Bio-Coal
1.7 SPM SOX NOX
Cyclone Separator
followed by wet
scrubber
2
Hot Air Generator
(1.5 Lacks KCal)
11 Bio-Coal
0.5 SPM SOX NOX
Cyclone Separator
followed by bag filter
ii Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
- There will be no process gas emission from proposed manufacturing activity.
iii Fugitive emission details with its mitigation measures:
As below:
Fugitive emission will due to the leakages in pump, storage container, material transferring, and packing. Mitigation measures: • Proper storage of raw materials, products and fuels • Ensuring closed feeding and sampling. • Establishing SOPs for start-up, shut down and maintenance operational procedure
• Regular work place and ambient air quality monitoring will be done. F Hazardous wastes
(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules
2016.
i
Sr. no.
Type/Name of Hazardous waste
Specific Source of generation (Name of the Activity, Product etc.)
Category and Schedule as per HW Rules.
Quantity (MT/Annum)
Management of HW
1 ETP Sludge
Effluent Treatment Plant
35.3 15 Collection, Storage, Transportation, Disposal at TSDF Site.
2 Used or Spent Oil
Lubricants from Machinery
5.1 0.05
Collection. Storage, Transportation & Disposal by selling to Registered Recycler.
3 Empty Barrels/ From Raw 33.1 5.0 Collection. Storage,
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Containers/ Liners contaminated with hazardous chemicals waste
Material/ Production Section
reuse for packing of ETP waste or sale to Authorized Recycler
4
Fly Ash From Utilities -- 15600
Collection, Storage, Transportation, Disposal at Brick Manufacturing Unit.
-
ii Membership details of TSDF, CHWIF etc.
(For HW management)
We will applied.
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
STP Waste
0.3 MT/ Year & its use as manure in
the premises.
G Solvent management, VOC emissions etc.
---
i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.
(Details in Table Format)
---
ii VOC emission sources and its mitigation measures
Not Applicable
H Details regarding storage of Hazardous chemicals
Storage details Name of major
Hazardous chemicals
Remarks
Storage tanks Sulphuric Acid (2.9) Hydrochloric Acid (5.5)
---
Drum/Barrel storage Acetic Anhydride (2.1) Sodium Hydroxide (4.4) Ammonia (0.4)
---
Applicability of PESO :
Due to less storage quantity PESO was not applicable.
Technical presentation submitted by PP was considered during SEAC meeting dated 17/12/2020.
Project proponent and technical expert of PP, M/s. Bhagwati Enviro Care Pvt. Ltd remains present during
video conference meeting dated 17/12/2020.
Committee noted that this is Greenfield project at GIDC Talod. PP mentioned that water supply source
will be GIDC water supply.
Consultant is having QCI/NABET accreditation certificate of consultant for sector 5(f) for preparation of
EIA/EMP report.
PP presented layout plan for proposed project and plot allotment letter of proposed project. Committee
deliberated at length regarding GIDC Talod establishment and is of year before 2006.
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PP mentioned that total effluent will be treated in ETP units and then will be sent to common spray dryer
facility of M/s. Chhatral Enviro Management System Pvt. Ltd for evaporation.
PP mentioned that they have proposed bio coal fired steam boiler and Hot air generator. Committee
insisted for adequate stack height and APCM for boiler in place of cyclone separator. PP has submitted
Hazardous Waste Matrix as per Hazardous Waste Rules – 2016. Committee insisted for submission of
notarized undertaking for adoption of automization process for critical process, obtain Fire NOC
certificate and provision of Occupational health centre (OHC) within premises.
After detailed discussion, Committee decided to recommend the project to SEIAA, Gujarat for
grant of Terms of Reference.
Considering the above project details, after detailed discussion, the terms of reference (ToR)
were prescribed as below and as per the standard TOR for the Synthetic Organic Chemical
projects recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and
approved by SEIAA in its 12th meeting dated 16/09/2017 for the EIA study to be done covering 10
Km radial distance from the project boundary.
1. Submit membership certificate of common spray dryer facility with mentioning booked
quantity, occupied quantity, spare capacity and inlet norms for acceptance of effluent as per
GPCB letter dated 08/01/2020.
2. Submit adequate APCM and stack height for bio coal fired boiler and Hot air generator.
3. Details of three year greenbelt development program including annual budget, types &number
of trees to be planted, area under green belt development [with map], budgetary outlay; along
with commitment of the management to carry out the tree plantation activities outside the
premises at appropriate places in surrounding area. Notarized undertaking regarding
development of green belt within premises (Minimum 14500 Sq. m i.e. 33.33 % of the total
plot area) as per the commitment before SEAC. Green belt shall be developed with native
plant species that are significant and used for the pollution abatement as per the CPCB
guidelines.
4. Fund allocation for Corporate Environment Responsibility (CER) for various activities therein.
The details of fund allocation and activities for CER shall be incorporated in EIA/EMP report.
The entire activities proposed under CER shall be part of Environment Management Plan
(EMP) as per the MoEF&CC‘s OM no. F. No. 22-65/2017-IA.III dated 30.09.2020.
5. Explore the use of renewable energy to the maximum extent possible. Details of provisions to
make the project energy-efficient through of energy efficient devices and adoption of modes of
alternative eco-friendly sources of energy like solar water heater, solar lighting etc. Measures
proposed for energy conservation.
6. Status of all the applicable rules, acts, regulation, clearances in a tabular form.
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7. Adoption of automization process like DCS/PLC including emergency response to eliminate
risk associated with the hazardous processes, fire safety certificate / Fire No-Objection
certificate (NOC) from the concern authority as per the prevailing Rules / Gujarat Fire
Prevention and Life Safety Measures Act, 2016 and provision of Occupational health
Centre(OHC) within premises.
8. Submit technical justification regarding spent sulphuric acid is not mentioned in Hazardous
waste matrix as per Hazardous waste Rules‘2016.
The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs
available in the MoEFCC‘s sector specific EIA Manual for ‗Synthetic Organic Chemical Industry‘ shall be
considered as generic TORs for preparation of the EIA report in addition to all the relevant information
as per the generic structure of EIA given in Appendix III in the EIA Notification, 2006.
Further Project Proponent may be advised to submit final EIA Report with EC application within 100
days from the date of issuance of this ToR to expedite processing of Environment Clearance application.
The project proponent shall have to apply for Environmental clearance through online portal
http://environment clearance.nic.in/ along with final EIA report.
The meeting ended with a vote of thanks to the chair. ***
Minutes approved by:
1. Shri Akshay Kumar Saxena, Chairman, SEAC
2. Dr. S. C. Pant, Vice Chairman, SEAC
3. Dr. M. N. Patel, Member, SEAC
4. Shri D. C. Chaudhari, Member, SEAC
5. Shri J. K. Vyas, Member, SEAC
6. Shri Anand Zinzala, Member, SEAC
7. Shri B. M. Tailor, Member, SEAC
8 Shri A. V. Shah, Secretary, SEAC
…..