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PRE FEASIBILITY REPORT (PFR)

For

PRIOR ENVIRONMENTAL CLEARANCE

Environmental Impact Assessment for

Proposed Expansion of High Rubber Graft-

HRG (Rubber rich ABS) at Satnoor Plant,

Dist. Chindwara (MP)

Project Proponent:

M/s. Bhansali Engineering Polymers Ltd.

Environmental Consultant

QCI-NABET Accredited EIA Consultant for Synthetic Organic Industries (Sector 21), MoEF&CC (GOI) and NABL Recognized Laboratory

ISO 9001:2008, ISO 14001:2004, OHSAS 18001:2007 60, Bajiprabhu Nagar, Nagpur - 440 033, MS

Lab. & Consultancy: FP-34, 35, Food Park, MIDC, Butibori, Nagpur – 441122 Ph.: (0712) 2242077, 9373287475

Email: [email protected], [email protected] website: www.anaconlaboratories.com

Report No. ANqr /PD/20A/2017/101

July 2017

Pre-Feasibility Report

of 42 Anacon Laboratories Pvt. Ltd.

Contents 1.0 EXECUTIVE SUMMARY ................................................................................................................................ 3

2.0 INTRODUCTION ........................................................................................................................................... 5

3.0 PROJECT DESCRIPTIONS .............................................................................................................................. 7

4.0 SITE ANALYSIS ........................................................................................................................................... 16

5.0 PLANNING BRIEF ....................................................................................................................................... 18

6.0 PROPOSED INFRASTRUCTURE .................................................................................................................. 19

7.0 REHABILITATION AND RESETTLEMENT (R&R) PLAN ................................................................................. 20

8.0 PROJECT SCHEDULE & COST ESTIMATES .................................................................................................. 22

9.0 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS) ........................................................................... 22

Annexure I- Google Map ....................................................................................................................................... 23

Annexure II-Land Document ................................................................................................................................. 23

Annexure III-Factory Licenses ............................................................................................................................... 32

Annexure IV-CHW-TSDF Membership .................................................................................................................. 33

Annexure V-Consent to Operate .......................................................................................................................... 34

Annexure –VI – Water Balance ............................................................................................................................. 41



1.0 EXECUTIVE SUMMARY 1.1 Project Proponent: : M/s. Bhansali Engineering Polymers Ltd.

1.2 Location : M/s. Bhansali Engineering Polymers Ltd. (BEPL),

Bhansali Nagar, Near Satnoor Village,

Taluka – Sausar, District – Chhindwara,

Madhya Pradesh - 480108

Latitude: 21°30'48.0"N

Longitude: 78°50'33.2"E

(Figures 1 & 2)

1.3 Office (Regd.) : M/s. Bhansali Engineering Polymers Ltd.,

Unit No. 401, 4th Floor, Peninsula Heights,

C.D. Barfiwala Road, Andheri (West),

Mumbai, Maharashtra, India - 400058

Email: [email protected]

Phone: +22-26731779-84 Fax: +22-26731796

1.4 Name of

Promoter/Director

: Mr. B. M. Bhansali,

Promoter & Managing Director

1.5 Proposed Project :

Sr. Name of

product

Existing

Capacity

Proposed

Capacity

addition

Total capacity after

expansion

1. High Rubber

Graft -HRG

(Rubber rich

ABS)

15000

TPA HRG

35,000

TPA HRG

50,000 TPA HRG

1.6 Total Project Area : 35.775 Ha (Plant area 15.775 ha & Greenbelt 20 ha)

1.7 Water Requirement : Total Water Requirement – Existing 592 KLD, Proposed 1360 KLD

Total 1952 KLD after expansion. Final fresh water requirement

after recycling & reuse will be 1516 KLD.

1.8 Power Requirement : Presently, Electricity is sourced from Madhya Pradesh Poorva

Kshetra Vidyut Vitaran Co. by 33 KV dedicated supply line with 33

KV substation in the plant premises with 2 MVA ( 33 KV/440 V)

transformer. The contract demand is 1300 KVA. After the proposed

expansion, estimated contract demand will be 4000 KVA. It is

planned to install one more 2 MVA transformer in the sub-station to

meet the enhanced demand.

Since the process is continuous, it is necessary to ensure

uninterrupted power supply. Presently, 2 x 500 KVA + 1 x 1250

KVA DG sets are provided as emergency power supply which is

automatically switched on in case of power failure. It is planned to

install 4 x 1250 KVA DG sets to meet the enhanced demand. DG

will be in stand by mode.

Note - Present Grid supply is at 33 KV which is capable of catering to 5 MVA load which is adequate to meet increased demand

mailto:[email protected]



1.9 Number of Shift : Three Shift Basis ( Round the clock)

1.10 No. of Working Days : 365 Days

1.11 Total Cost of Project : 13270 Lacs

1.12 Man Power Utilization : Existing 187 persons Proposed 90

1.13 Means of Finance

: Entire funding for the project will be through internal accruals.

1.14 Schedule of

Implementation

: Particulars Implementation Date/Time

Period

Commercial Production

will be started

After 12 months from Receipt of

Environmental Clearance

1.15 Environment Consulting

Organization

: Anacon Laboratories Pvt. Ltd.

HO: 60, Bajiprabhu Nagar, Nagpur - 440 033, MS. Ph.: (0712) 2242077 Lab. & Consultancy: FP-34, 35, Food Park, MIDC, Butibori, Nagpur – 441122 Mob.(CONSULTANCY): +91-9372960077

Email: [email protected] website: www.anaconlaboratories.com



2.0 INTRODUCTION 2.1 Identification of project and project proponent

Company Background

M/s. Bhansali Engineering Polymers Limited (BEPL) was incorporated in the year 1986. The

company was promoted by Shri B. M. Bhansali, a first generation entrepreneur. BEPL was the first

company in India to start manufacturing Quality Acrylonitrile Butadiene Styrene (ABS) resins using

foreign technology. The plant at Satnoor has been setup in technical collaboration with Sumitomo

Chemical Engineering Co. Limited / Sumitomo Nagautuck Limited, Japan. With an expected turnover

of 1000 Crores by 2017 and current workforce of 450 dedicated employees (BEPL has two plants in

India - Satnoor plant, Madhya Pradesh and Abu road Rajasthan), BEPL has a vision to progress

positively towards consolidating its leadership position in the domestic market.

2.2 Brief Description and Nature of the Project

ABS is a ter-polymer manufactured by compounding (blending) High Rubber Graft resin-HRG

(Rubber rich ABS) with Styrene, Acrylonitrile resin (SAN). While HRG can be manufactured through

Emulsion Polymerisation route only, SAN can be manufactured through Emulsion polymerisation or

Bulk polymerisation or Suspension polymerisation routes. However, the cheapest route is to

manufacture SAN through Bulk polymerisation route.

After opening of the Indian economy in 1990 onwards, the ABS market was getting dominated by

cheaper imports. Therefore, it was deemed expedient to modify the technology and bring the

manufacturing cost down at competitive level with imports. Hence, the technology of manufacturing

ABS was revamped to manufacture High rubber graft (HRG) with polybutadiene rubber content from

57 to 60 % through Emulsion polymerisation route. And subsequently dilute HRG with SAN

manufactured through bulk polymerisation route. Thereafter compound (blend) HRG and SAN to

bring high rubber concentration/content down to 15 to 25 % to manufacture various saleable grades

of ABS at import price parity level, conforming to the performance requirement by customers in

automotive, consumer durables and telecommunication products etc.

The entire HRG manufactured at BEPL Satnoor plant is being dispatched/delivered to BEPL Abu

road plant. The activities pertaining to manufacture of SAN and compounding with HRG are being

carried out at Abu road unit of BEPL which was acquired in the year 2003 from Greaves Limited.

EXISTING AND PROPOSED EXPANSION PRODUCTION DETAILS

2.3 Need for the project and its importance to the country and/or region

BEPL is manufacturing ABS Polymers since 1990, Requirement of the ABS is increased in India

owing to the growth in the Indian middle class expenditure in home appliances and automobiles,

which is driving the core demand for ABS. ABS have been witnessing healthy growth due to its wide

ranging usage in consumer electronics, appliances and automotive sectors. In current market

scenario, almost all the Refrigerator manufacturers have shifted to ABS from HIPS for refrigerator

Liners, hence the demand for ABS will continue to remain vibrant witnessing phenomenal jump

therein.

Sr.

No

Name of product Existing Capacity Proposed

Capacity addition

Total capacity

after expansion

2. High Rubber Graft -HRG

(Rubber rich ABS)

15000 TPA HRG 35,000 TPA HRG 50,000 TPA HRG



As of now in India there only two manufacturers of the ABS polymers and BEPL has share of approx.

70000 TPA in the Indian market and there is import of ABS of approximately 150000 TPA. Today’s

India’s total market demand is 3,00,000 TPA. Hence, BEPL deems it expedient to quickly expand the

capacity to conserve outflow of foreign exchange.

2.4 Demand-Supply Gap

There are only two manufacturing companies in India which produce ABS and are not able to cater to the whole demand of ABS in India, so the deficit in supply is fulfilled through imports.

The demand for ABS in India is largely dependent on two sectors namely Appliance and Automobile which account for nearly 85% of consumption. The Appliance sector contributes to nearly 45% of demand while Automobile accounts for 40% of demand. Hence the demand variance in the above sector directly influence the consumption of ABS.

There is a huge opportunity for company to exploit the growing market and to substitute import of ABS.

2.5 Imports vs. Indigenous production

The typical nature of ABS business in India is exposed to the risk of Foreign exchange fluctuations as

the key raw materials i.e. Styrene monomer & Acrylonitrile monomer are import dependent, as there

is no indigenous producer for the same. The only raw material which is indigenously available is

Butadiene monomer which contributes only 16% to 17% out of the total raw material composition.

2.6 Export possibility

HRG powder manufactured at Satnoor plant is sent to BEPL’s Abu Road unit for production of ABS.

2.7 Domestic/ Export Markets

As of now in India there only two manufacturers of the ABS polymers and BEPL has share of approx. 70000 TPA in the Indian market and there is import of ABS of approximately 150000 TPA. Today’s India’s total market demand is 3,00,000 TPA. 2.8 Employment Generation (Direct and Indirect) due to the project

The project will be having overall positive impact. It will generate direct & indirect employment to

around ~90 persons.



3.0 PROJECT DESCRIPTIONS

3.1 Type of project including interlinked and interdependent projects, if any.

HRG manufactured at Satnoor plant is sent to Abu road plant for captive consumption to produce

ABS which is sold in the market. The Abu road plant of BEPL is dependent on Satnoor plant of BEPL

and has obtained environmental clearance for production of ABS.

3.2 Location (map showing general location, specific location and project boundary and

project site layout) with coordinates.

Details about the Project area are presented in Table 1.

TABLE 1 DETAILS ABOUT THE PROJECT AREA

Plot No. M/s. Bhansali Engineering Polymers Ltd. (BEPL), Bhansali Nagar, Near Satnoor Village, Taluka – Sausar, District – Chhindwara, Madhya Pradesh - 480108

Toposheet No. 55K/14; 55K/15

Geo-coordinates Latitude: 21°30'48.0"N; Longitude: 78°50'33.2"E

The index map is presented in Figure 1, Location map showing 10 km radius of study area shown in

Figure 2 and layout plan is given in Figure 3.



FIGURE 1: INDEX MAP

Figure 1: LOCATION MAP SHOWING

Project Site:

M/s. Bhansali Engineering

Polymers Ltd.

Madhya Pradesh



FIGURE 2: STUDY AREA MAP

(10 KM RADIAL DISTANCE FROM THE PROJECT SITE)



FIGURE 3: LAYOUT PLAN



3.3 Details of alternate sites considered and the basis of selecting the proposed site,

particularly the environmental considerations gone into should be highlighted.

Total 35.775 Hector land was allotted by Revenue Department to BEPL in 1988 for establishing the

plant. The proposed expansion will be carried out in the existing premises of the plant and there is no

requirement of acquiring additional land. Hence no alternative site is examined by project proponent.

3.4 Size or Magnitude of Project.

The plant is established in total 35.775 Hector land including manufacturing area and green belt and

other infrastructure. There is no requirement of additional land for proposed expansion.

3.5 Project description with process details

Manufacturing process:

HRG Resin manufacturing is done utilizing Emulsion Polymerization Technology transfer from M/s.

Sumitomo Naugatuck Co. Ltd and Sumitomo Chemical Engineering Co. Ltd., Japan.

The process of manufacturing of HRG is divided into following steps;

1. Chemical mixing

2. Polymerisation

i. Polymerisation of Butadiene to Polybutadiene (PBDE)

ii. Agglomeration

iii. Polymerisation of Graft

3. Master Batch Scaling

4. Flocculation

5. Filtration

6. Drying

1. CHEMICAL MIXING :

Different chemical solutions required for emulsion polymerisation are prepared in this section. These

solutions are tested by Quality Assurance Department and after clearance, used in polymerisation

process.

2. POLYMERISATION

i. Polymerisation of Butadiene to Polybutadiene (PBDE)

Butadiene from storage tanks is scrubbed with NaOH solution to reduce its TBC content as TBC

inhabits the rate of polymerisation. Scrubbed Butadiene is taken into the reactor alongwith water

and other required chemicals / chemical solutions. Temperature of the mixture is increased to 65

°C. The reaction takes place at 65 Deg. C and under a pressure of about 5.0 - 9.5 kg/sq.m.

Turbidity (TB) of PBDE is controlled by staggered addition of emulsifier as TB has direct bearing

on particle size of PBDE. As the reaction proceeds, reaction temperature is increased gradually to

75 °C. After completion of the reaction, the latex is stripped off unreacted butadiene and stored in

specified storage tanks.

ii. Agglomeration

PBDE latex acts as a colloidal solution having charge (both + ve & - ve). This SPS latex is taken

in reactor & agitator speed kept 10 rpm. After that ABSNA solution is added & agitator speed kept

Sr.

No

Name of product Existing Capacity Proposed

Capacity addition

Total capacity

after expansion

1. High Rubber Graft-HRG

(Rubber rich ABS)

15000 TPA HRG 35,000 TPA HRG 50,000 TPA HRG



20 rpm. ABSNA solution is a strong electrolyte (polar & non polar) which disperse the charges of

SPS latex. With ABSNA SPS latex is agitated for 30 min. & PH checked comes about 11.5. Now

agitator rpm reduced to 10 & 3% H3PO4 acid solution dosing started with flowrate 0.85 lit/hr till PH

of latex comes < 4.0. H3PO4 acid aggregates the molecules of PBDE latex (partial coagulation) &

Turbidity increases. Cut off H3PO4 solution feeding at PH <4.0 & 10% KOH solution feeding

started at the flow rate of 0.47 lit/hr. KOH neutralize the added quantity of acid but turbidity as it is.

Cut off KOH feeding at PH >11.0 & agitator RPM increased to 20 rpm for half an hour. Then

Agglo latex transferred to latex storage after receiving results from QC. Dept. This latex is used

for production of GRAFT latex.

iii. Polymerisation of Graft

In polymerisation of graft, polybutadiene is used as backbone on to which a mixture of styrene

and acrylonitrile in fixed proportion (blended liquid monomer or BLM) is grafted Polybutadiene

alongwith water and other chemicals is added to the reactor. The mixture is heated to 65 °C and

emulsifier and BLM are continuously added in fixed proportion to the reactor. Reaction occurs

under vacuum. Here degree of polymerisation plays an important role which is governed by

turbidity measurement. The polymer lattices contains rubber domain i.e. polybutadiene and plastic

part i.e. polymer of styrene and acrylonitrile.

3. MASTER BATCH SCALING

Different Graft lattices are blended in fixed proportion as per the recipe for obtaining the desired

properties of final product. Antioxidants and colour stabilizers are added to this blend to inhibit

polymer oxidation, which would otherwise degrade the polymer. The blended is agitated for 2

hours for thorough mixing.

4. FLOCCULATION

Flocculated slurry is taken on to a vacuum belt filter where the water part is separated as filtrate

and the resin powder particles, after washing, are fed to dryer for drying.

5. FILTRATION

Flocculated slurry is taken on to a vacuum belt filter where the water part is separated as filtrate

and the resin powder particles, after washing, are fed to dryer for drying.

6. DRYING

The resin powder cake from belt filter contains about 40% moisture which is reduced to less than

20% in flash dryer using hot air at 95 - 100 °C and less than 0.9% in fluidised bed dryer using

hot water and hot air at 95 - 100 °C. The dried powder is stored in specified resin bin.



FIGURE 4: HRG MANUFACTURING PROCESS FLOW DIAGRAM

BUTADIENE

STORAGE

STYRENE

STORAGE

ACRYLONITRILE

STORAGE

PBDE

STRIPPING

PBDE

REACTOR

GRAFT

REACTOR

GRAFT LATEX

STORAGE

MASTER BATCH

PREPARATION

DRYING

BUTADIENE

SCRUBBING

CHEMIMIX

SOLUTION

PBDE

LATEX

STORAGE

FLOCCULATION

FILTRATION

POWDER

PACKING

AGGLOMER-

ATION

FLARE

STACK



3.6 Raw material required along with estimated quantity, likely source, marketing area of

final product/s, Mode of transport of raw Material and Finished Product.

Estimated raw materials quantity, mode of transportation is given in Table 2.

TABLE 2

ESTIMATED RAW MATERIAL QUANTITY

Sr.

No.

Raw

Material

Quantity

required for

15000 TPA

capacity

Quantity

required for

35000 TPA

capacity

Total Quantity

required for

50000 TPA

capacity

Mode of

transport

Source

1. Butadiene 8460.9 19742.1 28203.1 by road IOCL

2.

Styrene 4834.8 11281.2 16116.0

by road

from port

Imported

3.

Acrylonitrile 1813.1 4230.5 6043.5

by road

from port

Imported

4. Total 15108.8 35253.8 50362.6

3.7 Resource optimization/ recycling and reuse envisaged in the project, if any, should be

briefly outlined.

By adopting continuous improvement in technology and process, the reduction in process waste

generation will be achieved.

Plant has a pilot plant for carrying in-house R&D.

By proper and efficient handling of raw materials, wastages of raw materials will be reduced.

3.8 Environmental and Infrastructural Aspects

Availability of water its source, Energy/ Power requirement and source:

3.8.1 Availability of water and its source:

Water is sourced from Water Resource Department (WRD). BEPL has already taken requisite

permissions for drawl of water from Kanhan river through Jack well situated near Sawanga Village.

Pipeline network has been already established. Total fresh water requirement will be 1516 m3/day for

proposed expansion.

Please refer Annexure – VI Water Balance for further details.

3.8.2 Energy/ Power requirement and source:

Presently, Electricity is sourced from Madhya Pradesh Poorva Kshetra Vidyut Vitaran Co. by 33 KV

dedicated supply line with 33 KV substation in the plant premises with 2 MVA ( 33 KV/440 V)

transformer. The contract demand is 1300 KVA. After the proposed expansion, estimated contract

demand will be 4000 KVA. It is planned to install one more 2 MVA transformer in the sub-station to

meet the enhanced demand.

Since the process is continuous, it is necessary to ensure uninterrupted power supply. Presently, 2 x

500 KVA + 1 x 1250 KVA DG sets are provided as emergency power supply which is automatically

switched on in case of power failure. It is planned to install 4 x 1250 KVA DG sets to meet the

enhanced demand.

Sr. Particular Existing Proposed Total

1. Contract demand 1300 KVA 2700 KVA 4000 KVA

2. Connected Load 2975 KW 5950 KW 8925 KW




3. DG Sets (Plant) 1x1250 KVA;

2x500 KVA

4x1250 KVA 5x1250 KVA;

2x500 KVA = 7250 KVA

4. DG Set (Pump

house)

1x62.5 KVA No 1x62.5 KVA

Note – Present Grid supply is at 33 KV which is capable of catering to 5 MVA load which is adequate

to meet increased demand. MPPKVVCL permission for enhanced capacity will be submitted during

EIA presentation.

DG sets are kept standby mode only.

Fuel Requirement:

Coal is supplied from WCL, Savner through E-auction. LPG & HSD is procured from

IOCL/BPCL/HPCL as per requirement.


1. Coal 30 Tonns/day 70 Tonns/day 100 Tonns/day

2. HSD As per requirement

3. LPG 40 kg/day 80 kg/day 120 kg/day

3.9 Quantity of wastes to be generated (liquid and solid) and scheme for their

Management/disposal

3.9.1 Wastewater generation & management plan

The wastewater generation from the proposed plant will be 1078 m3/day. . The industrial effluent will

be treated in proposed effluent treatment plant. The industry shall reuse the treated effluent in order

to reduce the fresh water requirement.

Please refer Annexure – VI Water Balance for further details.

3.9.2 Effluent Treatment scheme

Liquid waste effluents is treated in the existing wastewater treatment plant (ETP). The entire ETP will

be upgraded for enhanced load and to suit discharge norms. Recycling options will be explored to

conserve water. Sewage will be treated in STP.

Zero discharge norms will be followed.

3.9.3 Solid/hazardous waste generation and Management plan

Presently, the solid/hazardous waste is being sent to Pithampur TSDF site, 480 kms away from the

plant. BEPL is exploring the possibility of disposing of the solid waste for brick manufacturing/

proposed fly ash based product cluster near Koradi thermal Power station, Nagpur which is just 45

kms away from the Satnoor plant. In this respect, necessary permissions will be obtained.

3.9.4 Stack details and air pollution measures

Presently, requirement is met by 320 Nm3/hour capacity flare stack having LPG fired burner tip. It is planned to install 640 Nm3/hour capacity new flare stack to meet the requirement of additional production. Boiler stack of 30 m height is connected through cyclone & bag filters for air pollution control. DG sets are equipped with stacks as per CPCB norms.



4.0 SITE ANALYSIS 4.1 Connectivity.

The plant is located near Satnoor village on State Highway No. 250 (Nagpur – Chinddwara).

The site is well connected with Road/Rail/Airport. The details are as follows:

Nagpur Railway Station ~48.00 Km, SSE

Nagpur Airport ~52 Km, SSE

4.2 Land Form, Land use and Land ownership.

Total 35.775 Hector land was allotted by Revenue Department to BEPL in 1988 for establishing the

plant. The proposed expansion will be carried out in the existing premises of the plant and there is no

requirement of acquiring additional land. Hence no alternative site is examined by project proponent.

The details regarding the breakup of the land for the various activities of the proposed project is as

follows (Tables 3)

TABLE 3

AREA STATEMENT

Sr. No. Description Existing Area in Sq. M. Proposed Area in Sq. M.

1. Utility area 1887.7 3469.42

2. Admin Building 2640 0

3. Storage 911.1 300

4. Process area 6008 2904

5. ETP Area 11803 As per requirement

6. Green belt 200000 0

7. Roads 19535 0

8. Other 114965.2 0

9. Total (Existing + Proposed ) 357750 M2

4.3 Topography of the project area

The site is situated on hilly terrain. The project site lies at the Latitude: 21°30'48.0" N & Longitude:

78°50'33.2" E on the Topo sheet No. 55K/14; 55K/15. The site specific Topography is shown in study

area map.

4.4 Existing land use pattern (agriculture, non-agriculture, forest, water bodies

(distance from HFL to the river), CRZ. In case of notified industrial area, a copy of Gazette

Notification should be given:-

The proposed expansion will be carried out in the existing plant premises. The land is already

converted for industrial use. Land documents are enclosed as Annexure-III.

There is no forest, national park, wild life sanctuary, eco sensitive areas in surrounding 10 Km from

the plant boundary. CRZ is not applicable to the project.

Existing infrastructure

Existing facilities are sufficient for 15000 TPA HRG production. Photographs are attached in following

Figure 5.



FIGURE 5: PROJECT SITE PHOTOGRAPHS



5.0 PLANNING BRIEF 5.1 Planning concept (type of industries, facilities transportation Town and Country

Planning Development authority Classification.

Type of Industry

HRG resin manufacture (As per EIA notification dated 14 September 2006 and subsequent

amendments, this project falls under schedule No. 5 (f) Manufacturing of Synthetic organic chemical

Industry)

Town and Country Planning Development authority Classification

The proposed project falls under Gram panchayat Satnoor village. Adequate road facilities are

already available for transportation of raw materials as well as finished products.

5.2 Population Projection

The proposed expansion will be providing employment to 90 people in addition to existing 187 people

directly and indirectly. Since the proposed plant is located in the Chhindwara district in which trained

manpower are readily available, therefore the employment will be given mostly to local people, so

there will not be any substantial increase in the population of local villages. However, due to increase

economic growth, the local youth will be benefited with respect to employment.

5.3 Land use planning (breakup along with green belt etc.)

The total land area is 35.775 hectors and the greenbelt is already developed on 20 hector area of the

total land.

The breakup of the land for the proposed project is given in Table 4 above.

5.4 Assessment of Infrastructure Demand

The basic infrastructure (Connective roads, Water resource vicinity) required for the proposed

expansion is available at the project site as the industry has existing unit. Apart from that the

additional infrastructure will be developed by the company as per the requirement.

5.5 Facilities Availability

Major basic facilities are available for the proposed project. Road, electricity, water, transportation

facility etc. are well developed in the surrounding area. The major new facilities required to be set for

the proposed project will be installation of process equipment at site within the premises along with all

the necessary infrastructures like additional storage tanks and equipment sheds etc.



6.0 PROPOSED INFRASTRUCTURE

6.1 Industrial Area (Processing Area)

The proposed expansion will be carried out in the existing plant premises. The total land area is

35.775 hectors and the greenbelt is already developed on 20 hector area of the total land as given in

land use statement (Table 4).

6.2 Residential Area (Non Processing Area)

There is no residential area proposed in the plant premises.

6.3 Green Belt

The total land area is 35.775 hectors and the greenbelt is already developed on 20 hector area of the

total land which constitutes more than 50%.

6.4 Social Infrastructure

The project area lies within the district of Chhindwara. There is no requirement to build any social

infrastructure within the proposed plant area. The management of M/s. BEPL is already running a

public school (Nursary to class 10th) as social service.

6.5 Connectivity (Traffic and Transportation Road, Rail/Metro/Waterways etc.).

The proposed project is situated near Satnoor village on Nagpur- Chhindwara highway. The site is

well connected with Road/Rail. The details are as follows:

Sawanga Railway Station ~2.83 Km, E

Nagpur Railway Station ~48.00 Km, SSE

Nagpur Airport ~52 Km, SSE

6.6 Drinking Water Management (Source & Supply of water)

Drinking water is sourced from Kanhan River near Sawanga village.

6.7 Sewerage system

Additional infra-structural services including water supply, sewage, drainage facilities and

electrification will be made for proposed expansion. Currently domestic sewage is treated in septic

tanks and treated water is used for irrigation within plant. No wastewater will be discharged on land.

Process wastewater will be treated in ETP and reused and recycled. STP is proposed and treated

water will be used for cooling tower. Zero discharge norms will be followed.

6.8 Industrial Waste/ Solid Waste Management

The industrial wastes generated in the form of solid wastes, and hazardous wastes will be collected,

segregated and disposed off as per CPCB guideline.

Presently, the solid/hazardous waste is being sent to Pithampur TSDF site, 480 kms away from the

plant. BEPL is exploring the possibility of disposing of the solid waste for brick manufacturing/

proposed fly ash based product cluster near Koradi thermal Power station, Nagpur which is just 45

kms away from the Satnoor plant. In this respect, necessary permissions will be obtained.



7.0 REHABILITATION AND RESETTLEMENT (R&R) PLAN

7.1 Policy to be adopted (Central/ State) in respect of the project affected persons

including home oustees, land oustees and landless laborers (a brief outline to be

given).

The proposed project does not have any directly displaced persons, as land acquisition is not

involved. There are also no land oustees or project affected persons or home oustees, thus R&R plan

is not applicable here. However, the priority for employment will be given to local persons living in the

adjoining villages. In addition to this, company will continue to contribute for the welfare of the people

of local surrounding under company’s CSR policy.

DETAILS OF CORPORATE SOCIAL RESPONSIBILITY:

CSR Programs

The policy outlines the Company’s strategy to bring about a positive impact on society through activities/ programs relating to Health, Happy Childhood, Education, Employment, Hunger eradication, Environmental Sustainability, Promoting Gender Equality, Gender upliftment for deserving sections of society, Sports Promotion etc.

Monitoring

CSR committee authorized by board of directors will monitor CSR activities and proper utilization of

funds. The CSR committee will be fully authorized to delegate appropriate authority to any employee

of the company for properly carrying out CSR activities.

Environment Impacts and Measures

Schematic representations of the feasibility drawing which give information of EIA purpose:

S. No. Particulars Impacts Remediation Proposed

1. Change in

land use.

There will be change in land

use on permanent basis due

to installation of machineries

and equipment.

The proposed expansion will be carried

out adjacent to existing structure. No

additional land is required for the

proposed expansion.

Water is sourced with permission of

Water Resource Department (WRD)

from Kanhan River near Sawanga

village. No groundwater will be

abstracted for the project activities

hence, and natural recharge of

groundwater level will not be affected

through proposed project activities.

2. Transportation

of material

The existing network of

transport gets pressurized

The proposed activity will marginally

increase in Traffic density. The project

site is adjacent to state highway thus,

infrastructural facilities/road accessibility

are already developed.

3. Gaseous and

Particulate

Emission to

The

atmosphere

Air quality All necessary steps will be followed to

minimize the emission from point sources

as well as line sources. Thus the

standards of Stack Emission and Ambient

Air quality will be maintained as per

prescribed limits.



S. No. Particulars Impacts Remediation Proposed

4. Discharge of

effluent

Impact of water quality. Zero discharge is proposed.

5. Withdrawal of

ground /

surface water

Availability of ground/surface

water is affected.

Water is sourced from Kanhan river, no

ground water will be abstracted for the

project activities hence, and natural

recharge of groundwater level is not

affected through project activities.

Permission regarding drawl of river water

is granted from Water Resource

Department.

6. Operation of

equipment

and vehicles

likely to

generate

noise.

Impact on human health due

to excess noise level beyond

permissible level.

All the process equipment will be installed

on anti-vibration pad with sufficient

provisions to minimize generation of

noise. The high noise generating

equipment like generator will be enclosed

with noise suppressing enclosures.

The buildings as well as boundary wall

and green belt will ensure the attenuation

of noise outside the boundary within the

prescribed limits.

7. Fire Hazard

due to storage

of fuel etc.

Risk to the surrounding

habitation.

Necessary precautions to prevent fire and

all the provisions to control fire shall be

provided.

8. Employment

to outsiders

Socio-economic disparity with

local community

Priority of employment will be given to

local people, as already sufficient

qualified and trained local youth area

available.

9. Cultural impact Local population feels

isolated

The promoters proposed to employ local

masses in the project hence no such

impact on cultural diversity is likely to take

place.

10. Disposal of

solid and

hazardous

wastes

Create odorous problem,

nuisance condition related to

the disposal of solid wastes.

Deterioration of soil,

productivity pollution in

ground water/surface water

due to leaching and surface

runoff.

Domestic wastes will be segregated for

organics and Inorganics. Organic wastes

will be used for composting and

inorganics for approved vendors.

Disposal of hazardous wastes will be

done as per hazardous wastes handling

and disposal rule.



8.0 PROJECT SCHEDULE & COST ESTIMATES SCHEDULE FOR APPROVAL AND IMPLEMENTATION

Proposed Project

The project will start only after obtaining Environmental Clearance and other statutory permissions.

Project will be completed in 12 months after getting all the regulatory approvals.

8.2 Estimated project cost along with analysis in terms of economic viability of the project.

The proposed project cost is estimated to be Rs. 13270 Lacs.

9.0 ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS)

9.1 Financial and social benefits with special emphasis on the benefit to the local People

Including Tribal Population, If Any, in the Area.

On overall assessment of the project with consideration of technical and financial aspects, it is

concluded that the proposed expansion is technically feasible and financially viable. There are

only two manufacturing companies in India which produce ABS and are not able to cater to the

whole demand of ABS in India, so the deficit in supply is fulfilled through imports. BEPL deems it

expedient to quickly expand the capacity to conserve outflow of foreign exchange.

Project will create direct & indirect employment opportunities within the surrounding region. Unit will use

good faith efforts to employ local people from the nearby villages depending upon the availability of

skilled & un-skilled man-power surrounding the project site. The project will continue to benefit socio-

economic benefits for the society with Company’s employment and CSR activities.



ANNEXURE I- GOOGLE MAP



ANNEXURE II-LAND DOCUMENT



Annexure III-Factory Licenses



ANNEXURE IV-CHW-TSDF MEMBERSHIP



ANNEXURE V-CONSENT TO OPERATE

ANNEXURE –VI – WATER BALANCE

EXISTING WATER BALANCE PROPOSED WATER BALANCE FINAL WATER BALANCE

Sr.

No.

Water Uses Water

Required

(m3/d)

Waste

Water

Generation

(m3/d)

Evaporation

Losses/Process

Consumption

(m3/d)

Reuse /

Recycle

Water

Required

(m3/d)

Waste

Water

Generation

(m3/d)

Evaporation

Losses/Process

Consumption

(m3/d)

Reuse /

Recycle

Water

Required

(m3/d)

Waste

Water

Generation

(m3/d)

Evaporation

Losses/Process

Consumption

(m3/d)

Reuse /

Recycle

Initial Raw

Water

Requirement

592 1360 1952

I Multi Directional Filter (MDF)

Raw Water treat before uses

20 Nil 572*

Raw Water treat before uses 46 Nil 1314*

Raw Water treat before uses

66 Nil 1886*

This 572* m3/day Multi Directional Filter (MDF) treated is using in

different purposes in the plant, details are shown below. This 1886* m

3/day Multi Directional Filter

(MDF) treated is using in different purposes in the plant, details are shown below.

A Different use 92 215 307

i Water hydrant 3 1.5 1.5 7 3.5 3.5 10 5 5

ii ETP 36 34 2 84 79 5 120 113 7

iii Flore cleaning 45 30 15 75 70 35 150 100 50

iv Land scaping 8 Nil 8 19 Nil 19 27 Nil 27

B DM Water 308 719 1027

i Cation+Anion +Mixed Bed Filter

308 23 Nil 285* 719 54 Nil 665* 1027 77 Nil 950*

ii Polymerization & Flocculation

285* 195 30 eva.+60 Steam

60 665* 455 70 eva.+140 Steam

140 950* 650 100 eva.+200 Steam

200

C Industrial Water

161 376 537

I Softener 161 6 Nil 155* 376 14 Nil 362* 537 20 Nil 517*

This 155* m3/day soft water is generated are using in various

process. This 362* m

3/day soft water is generated are

using in various process. This 517* m

3/day soft water is generated are

using in various process.



ii Hydro get cleaning

4 3 1 4 9 7 2 9 13 10 3 10

iii Cooling tower 66 11 55 11 155 26 129 26 221 37 184 37

iv Boiler 85 Nil 85 Nil 198 Nil 198 Nil 283 Nil 283 Nil

D Domestic

Use

11 8 3 8 4 3 1 3 15 11 4 11

Total

592 331.5 260.5 23 (8-

Reuse*

+ 15-

Recycle)

1360 746.5 613.5 38 (3-

Reuse*

+ 35-

Recycle)

1952 1078 874 58 (11-

Reuse* +

47-

Recycle)

Initial Fresh Water

requirement 592 m

3/day

1360 m

3/day

1952 m

3/day

Out of 1078 [432 evaporation losses in ETP & Sludge Drying bed and 190 will use in green belt, (No change)] Recycle in process: 1078-432-190=456 finally treated by RO and RO Permeate 436 will Recycle in process where as Ron reject 20 will send again in ETP. In this way daily water intake will reduce by 1952-436=1516

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