resins & allied chemicals industries (bombay)...

PROJECT FEASIBILITY REPORT

RESINS & ALLIED CHEMICALS INDUSTRIES (BOMBAY) PVT. LTD.

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FOR

THE PROPOSED EXPANSION PROJECT

FOR THE MANUFACTURING OF

KETONIC RESINS

Category: 5(f)

OF

RESINS & ALLIED CHEMICALS INDUSTRIES

(BOMBAY) PVT. LTD.

Located at:

Plot No. C-1/46, 100 SHED AREA, GIDC, Vapi,

Dist- Valsad (Gujarat).



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Project prefeasibility report for obtaining prior Environmental Clearance in terms of provisions of

EIA Notification – 2006

1. EXECUTIVE SUMMARY:

No. Description Proposed Project Details

1 Name of project & Address

Resins & Allied Chemicals Industries (Bombay) Pvt. Ltd. Plot No: C-1/46, 100 shed area, G.I.D.C, VAPI. Pin Code: 396195 Dist. - Valsad (Gujarat)

2 Project Category 5 (f) of EIA notification – 2006.

3 Project capital cost Proposed : Rs.0.10 Crores

4 Products Name of product Production capacity, MT/month

Existing Proposed Total after expansion

Ketonic Resins 20 80 100

By Product (Resin Cake)

0 21.5 21.5

5 By-products Resin cake = 21.5 MT/month

6 Resource Requirement

Land 855 m2.

Water Source: GIDC water supply Existing: 19.60 KL/day Proposed: 16.37 KL/day Total after expansion: 35.97 KL/day

Electricity Source: DGVCL Power requirement: 60 HP DG set: 82.5 KVA. (In case of power failure only)

Fuel Natural Gas: 200 kg/day HSD for DG set: 15 lit/hr

Man power Operation phase – 20 nos.

7 Source of Pollution

Waste Water Generation

Existing: Industrial Effluent : 8.0 KL/day Sewage : 2.0 KL/day Proposed: Industrial Effluent : 16.52 KL/day Sewage : 0.5 KL/day Total after expansion: Industrial Effluent : 24.52 KL/day Sewage : 2.5 KL/day

Air Emission PM10 , PM2.5, SOx & NOx

Solid Waste Generation Hazardous waste: ETP sludge, Used Oil, Discarded containers/Bags/liners

8 Mode of Treatment

Waste water 1) Industrial Effluent:

High COD stream shall be treated in Primary Treatment unit and then sent to CMEE of Vapi Green Enviro Limited/ Own MEE for further treatment and disposal.



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Low COD stream shall be treated in Primary, Secondary & Tertiary Effluent Treatment Plant and finally drained to CETP drainage line.

2) Domestic effluent will be treated in septic tank/soak pit system.

Air Chimney with adequate height has been provided to Boiler and DG set.

Solid Waste Solid/hazardous waste will be collected, stored and disposed as per Hazardous Waste Management Rules.

2. INTRODUCTION OF THE PROJECT:

2.1. Introduction of the project and project proponent:

Name of the Project : Resins & Allied Chemical Industries (Bombay) Pvt. Ltd.

Location : Plot No: C-1/46, 100 shed area, G.I.D.C, VAPI. Pin Code: 396195 Dist.

- Valsad (Gujarat)

Introduction of the project proponent:

The company is a Private limited company and is promoted by Shri R. N. Mandal. The details

related to directors are given below:

Sr. No. Name of Directors Residential Address

1. Shri Ramanath Mandal Geetanjali, Plot No. 582, Khar Section, Ambernath Dist- Thane, Maharashtra.

2. Mrs. Sandhya Mandal

2.2. Brief description of the project:

2.2.1. Resins & Allied Chemical Industries (Bombay) Pvt. Ltd. is located in GIDC notified

industrial area falling under medium Scale category.

2.2.2. The unit is manufacturing Ketonic resins with production capacity 20 MT/month at

existing premises.

2.2.3. Now looking to the existing market conditions, the company proposed to enhance the

production capacity of the Ketonic Resins to 100 MT/month in the same premises

with the installed and additional plant machineries with required modifications.

2.2.4. Considering the Environment concerns the company proposed to manufacture the

Ketonic resins with improved technology which leads to decrease the effluent



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generation with respect to production capacity and hence there shall be no additional

load on existing ETP.

2.2.5. There shall be no process gas emission in existing as well as proposed expansion.

2.2.6. The company is also having the membership of TSDF site for disposal of solid waste

generated.

2.3. Need of the project:

2.3.1. At present company exports 95% of its production to Europe and US.

2.3.2. Expansion is needed to meet the growing export demand.

2.4. MARKET FEASIBILITY:

The existing unit is already engaged in the manufacturing of “Ketonic Resins” since 1981.

Presently, the product has a very good potential in the foreign markets as well as in the

domestic market hence the company proposes to increase its existing production capacity.

2.5. Employment Generation (Direct and Indirect) due to the project:

Details of Man power requirement are as under:

Existing : 11 Nos.

Proposed : 9 Nos.

Total after expansion : 20 Nos.

3. PROJECT DESCRIPTION:

3.1. PROPOSED PROJECT & APPLICABILITY OF EIA:

Category as per the amended EIA notification-2006: The existing and proposed expansion in

Ketonic Resins manufacturing is covered under the Category-5(f) – Synthetic Organic

Chemicals.

As per the EIA Notification the proposed expansion project is covered under category A.

3.2. Project Location:

Location: Plot No: C-1/46, 100 shed area, G.I.D.C, VAPI. Pin Code: 396195, Dist. - Valsad

(Gujarat)



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There is clustered of profuse large-scale, medium scale and small-scale industries, engaged

in manufacturing of various products, Bulk drugs, Organic pigments, Organic and Inorganic

Chemicals, Pharmaceuticals, Pesticides etc.

The GIDC area has a Disaster management cell set up by Vapi Industrial Association.

Common Effluent treatment plant and common hazardous waste disposal site is set up by

Vapi Waste & Effluent Management Co. Ltd. Vapi also having the drainage system for the

disposal of the treated effluent from individual industry to the CETP for further treatment

and disposal into the saline region of Damanganga River.

Location of project sit:



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Location map showing the Project site and inter-state boundary within 5 km radius



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LAYOUT OF THE PROJECT SITE:

SITE SELECTION:

The major reason for selection of the existing location was that the existing infrastructure &

resources can be availed for the expansion activities. Secondly, it falls in the GIDC notified

industrial area of Vapi and hence the required infrastructure and resources are readily

available.

The plot was allotted in the name of M/s. Resin & Allied Chemical Industries (Bombay) Pvt.

Ltd. in the year 1981. The copy of the GIDC plot allotment letter is enclosed as Annexure I.

3.3. Alternative Studies

No alternative site study has been done as the proposed project is located in notified

industrial area of GIDC, Vapi.



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3.4. Resource Requirement

3.4.1. Raw Material

Sr. No. Raw materials Quantity (MT/MT)

1. Formaldehyde 1.300

2. Cyclohexanone 0.780

3.4.2. Land Requirement

The total plot area of the unit is 855 m2 out of which 215 m2 of area is allotted for

Green Belt Area.

Area break up is mentioned in below table.

Particulars Area (m2)

Total Constructed Area 255

Total Gardening Area 215

Total Open Land Area 385

Total Plot area 855

3.4.3. Man Power

Details of Man power requirement are as under:

Existing : 11 Nos.

Proposed : 9 Nos.

Total after expansion : 20 Nos.

3.4.4. POWER AND FUEL REQUIREMENT

Power requirement:

The main power supply is provided by Dakshin Gujarat Vij Co. Ltd. The present total

connected load is 60 HP which will be sufficient for proposed expansion.

Fuel Requirement:

The company operates LDO fired Boiler (1 No) of 600 kg/hr capacity and uses

LDO as fuel for the same. Now the company proposes to switch over the fuel



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from LDO to Natural Gas with consumption of 100 kg/day. Hence after

proposed expansion, use of LDO shall be omitted in existing boiler.

Earlier the drying of finished product in Tray Dryer was carried out by steam

only. Now after proposed expansion, it is proposed to carry out the drying of

finished product in Tray Dryer by Flue gas of Natural Gas only, hence no

steam is required. Natural gas consumption for the drying shall be 100

kg/day.

D.G. set of 82.5 KVA is also installed and HSD is used as fuel. D.G Set is

operated only in case of power failure.

The details of fuel consumption are as under.

Sr. No.

Particulars Requirement

Source Existing Proposed

Total after expansion

1 Energy – Electricity, HP 60 0 60 Dakshin Guj. Vij Co. Ltd.

2 LDO for Existing Boiler (600 Kg/Hr.), lit/hr

25 -25 0 Local suplier

3 Natural Gas for boiler & drying, kg/day

100 100 200 Gujarat Gas Co. Ltd

4 HSD for existing D.G. Set (82.5 KVA), lit/hr

15 0 15 Local suplier

3.4.5. Water Requirement:

Sr. No.

Particular Water cons., KL/day


1 Domestic 2.00 1.00 3.00

2 Industrial

2.1 Processing + Washing 9.40 11.27 20.67

2.2 Boiler 2.10 0.00 2.10

2.3 Cooling 2.10 2.10 4.20

2 Subtotal Industrial 13.60 13.37 26.97

3 Others (Gardening) 4.00 2.00 6.00

4 Total (1+2+3) 19.60 16.37 35.97



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3.5. Product detail:

Sr. No.

Name of the Product Production Capacity, MT/Month


1 Ketonic Resin 20 80 100

By product

1 Resin Cake 0 21.5 21.5

4. MANUFACTURING PROCESS:

4.1. PROCESS TECHNOLOGY

The company is using the latest available process technology for the production. This

chapter includes the manufacturing process of the product, chemical reactions, and

material mass balance for the product.

4.2. MANUFACTURING PROCESS WITH CHEMICAL REACTION

4.2.1. Chemical Reaction:

HCHO +

Formaldehyde Cyclohexanone Ketonic Resin

4.2.2. MANUFACTURING PROCESS WITH CHEMICAL REACTION

A measured quantity of formaldehyde, cyclohexanone and water is taken in a closed

reaction kettle and mixed properly. A little quantity of catalyst is then added to initiate

the reaction and is allowed to continue until solid granules of ketonic resin are formed.

The whole mass is then washed with fresh water, filtered, dried and packaged in

paper/HDPE bags.

http://images.google.co.in/imgres?imgurl=http://upload.wikimedia.org/wikipedia/commons/thumb/3/3c/Cyclohexanone-2D-skeletal.png/100px-Cyclohexanone-2D-skeletal.png&imgrefurl=http://www.wielkaencyklopedia.com/pt/wiki/Cicloexanona.html&h=171&w=100&sz=3&hl=en&start=4&um=1&tbnid=Dr10zgkqFcVnnM:&tbnh=100&tbnw=58&prev=/images%3Fq%3Dcyclohexanone%26um%3D1%26hl%3Den%26sa%3DX



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4.2.3. Process Flow Chart with Mass Balance for Production of 1000 kg Ketonic Resin at

existing scenario:

MASS BALANCE:

Sr. No.

Input Quantity, kg Out Put Quantity, kg Remark

1 Formaldehyde 1300 Ketonic Resin 1000 PRODUCT

2 Cyclohexanone 792 Effluent water 12562 To ETP

3 Process Water 1600 Handling loss 30

4 Wash Water 10000 Evaporation loss 100

Total 13692 13692



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4.2.4. Process Flow Chart with Mass Balance for Production of 1000 kg Ketonic Resin

after proposed expansion:

MASS BALANCE:

Sr. No. Input Quantity, kg Out Put Quantity, kg Remark

1 Formaldehyde 1300 Ketonic Resin 1000 PRODUCT

2 Cyclohexanone 780 High COD stream 2835 MEE

3 Process Water 2520 Low COD stream 4100

4 Wash Water 3680 Resin cake 215 By Product

5 Handling loss 30

6 Evaporation loss 100

Total 8280 8280



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5. Water Environment:

5.1. Water management system includes water balance data, wastewater characteristics and

effluent treatment plant. The source of water is the GIDC Water Supply Department.

5.2. Water Consumption & effluent generation, KL/day:

WATER CONSUMPTION:

Sr. No.

Particular Water cons., KL/day


1 Domestic 2.00 1.00 3.00

2 Industrial


2.2 Boiler 2.10 0.00 2.10

2.3 Cooling 2.10 2.10 4.20



4 Total (1+2+3) 19.60 16.37 35.97

Effluent generation with segregation of effluent stream:

Sr. No.

Particular Effluent generation, KL/day


1 Domestic 2.00 0.50 2.50

2 Industrial


2.2 Boiler 0.00 1.00 1.00

2.3 Cooling 0.00 0.40 0.40



4 Total (1+2+3) 10.00 17.02 27.02

Segregation effluent stream

1 High COD stream to CMEE after Primary Treatment 8.00 1.45 9.45

2 Low COD to ETP 0.00 13.67 13.67

Effluent to ETP

1 Domestic 2.00 0.50 2.50

2 Industrial


2.2 Boiler 0.00 1.00 1.00

2.3 Cooling 0.00 0.40 0.40


3 Others (Gardening) 0.00 0.00

4 Total (1+2+3)Effluent to ETP 8.00 7.07 15.07



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5.3. Expected quality of untreated & treated effluent.

Sr. No.

Parameter Unit High COD stream to

CMEE

Low COD stream to

ETP

Treated effluent to Drainage

1 pH pH units 6.5-7.0 6.5-7.0 6.5-8.5

2 Colour Pt-Co scale 45-50 35-45 <25

3 Total Dissolved Solids (TDS) ppm 90000 1500-1800 1600-1900

4 Chemical Oxygen Demand (COD) mg/l 90000-130000 900-1000 700-800

5 Suspended Solids (SS) mg/l 600-800 90-95 70-80

5.4. Based on the quantity and characteristics of waste water generated as above, the existing

Effluent Treatment Plant is adequate to treat the effluent after proposed expansion.

The sewage generated shall be disposed into septic tank/soak pit of adequate

capacity.

The process effluent is proposed to segregate in High COD effluent stream and Low

COD effluent stream.

The High COD effluent stream shall be treated in Primary treatment and further sent

to Common MEE of Vapi Green Enviro Limited, Vapi/own MEE. The membership of

Vapi Green Enviro has already been obtained. Or the company also proposed to

install an own MEE for the treatment of High COD effluent. The condensate from

MEE shall be recycled/reuse for industrial purpose.

The Low COD effluent stream shall be treated in existing Effluent Treatment Plant

consists of Primary, Secondary & Tertiary Treatment Units.

The treated effluent from the ETP shall be drained in CETP drainage line to CETP,

Vapi.

The copy of the membership letter from Vapi Green Enviro Limited (Vapi Waste

Effluent Mgt. Co. Ltd.) – CETP is enclosed as Annexure II.



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5.5. Water balance Diagram at existing scenario, KL/day

5.6. Water balance Diagram after proposed expansion, KL/day



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5.7. Details of Effluent Treatment Plant:

5.7.1. PRIMARY TREATMENT:

UNITS: Oil & Grease removal Tank

Collection cum Neutralization / Reaction Tank

Primary settling and sludge removal

The effluent coming from the plant is initially passed through the Oil & Grease

removal system. The oil free effluent is then collected into the collection cum

reaction tank. In the collection cum reaction tank various chemicals like None Ferric

Alum, Caustic soda/acid and polyelectrolyte (coagulant) are added to ensure proper

settling which reduces the suspended solid concentration, color and COD in the

effluent. The treated effluent is then fed into the primary clarifier. Clear effluent

from primary settling tank is charged into the secondary treatment tank (Aeration

tank) and settled sludge is discharged into the sludge drying beds and leached of the

sludge drying beds is going back to collection tank.

5.7.2. SECONDARY TREATMENT (BIOLOGICAL TREATMENT)

UNITS : Aeration Tank

Secondary settling

The primary treated clear effluent is passed through the aeration tank where the

biodegradation of the organic matter is taken place in presence of active

microorganism and required Dissolved Oxygen level. During the biological treatment

BOD Value and COD Value are reduced. After the biological treatment (aeration

tank) the effluent with the biomass is passed through secondary settling tank where

biomass is settled and settled biomass is recycle back to aeration tank or if excess is

discharged into the sludge drying beds. And clear effluent is collected into the

holding tank.

5.7.3. TERTIARY TREATMENT

UNIT: Sand and Carbon Filter (Mixed bed)

After secondary treatment the effluent is passed through the mixed bed filter for

further reduction of COD Value, BOD Value and Color. Treated water is collected into



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the treated water tank above the roof. Finally the treated effluent confirming the

treated water discharge norms laid down by board is discharged into the

underground drainage to CETP for final treatment and disposal.

5.8. SCHEMATIC DIAGRAM OF EFFLUENT TREATMENT PLANT



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6. AIR ENVIRONMENT

6.1. The company operates LDO fired Boiler (1 No) of 600 kg/hr capacity and uses LDO as fuel

for the same. Now the company proposes to switch over the fuel from LDO to Natural Gas

with consumption of 100 kg/day. Hence after proposed expansion, use of LDO shall be

omitted in existing boiler.

6.2. Earlier the drying of finished product in Tray Dryer was carried out by steam only. Now

after proposed expansion, it is proposed to carry out the drying of finished product in Tray

Dryer by Flue gas of Natural Gas only, hence no steam is required. Natural gas consumption

for the drying shall be 100 kg/day.

6.3. D.G. set of 82.5 KVA is also installed and HSD is used as fuel. D.G Set is operated only in

case of power failure.

6.4. There shall be no process gas emission.

6.5. The details of fuel consumption are as under.



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6.6. Details of proposed flue gases stack, nature of emitted pollutants and system provided for air pollution control are mentioned in the following

table.

Sr. No.

Stack attached to Type of fuel

Fuel cons. Stack Ht., m

Emission Parameter

Permissible limit

Unit Existing Proposed Total after expansion

1 Boiler Capacity: 600 kg/hr

LDO, lit/hr or 25 -25 0 11 PM 150 mg/nm3

Natural gas, kg/day 100 0 100

2 DG set - 82.5 KVA HSD, lit/hr 15 0 15 11 SO2 100 ppm

3 Tray dryer Natural gas, kg/day 0 100 100 11 NOx 50 ppm



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7. Solid/Hazardous Waste

7.1. Hazardous waste will be generated from the Effluent treatment plant, D.G. Set and raw

material consumption. The company has adequate storage facility for the storage of waste.

7.2. The details of Hazardous waste generation and management are as under.

Sr. No.

Types of Waste

Category Source of

Generation

Quantity

Method of Disposal Existing Proposed

Total after

expansion

1 ETP Waste, MT/month

34.4 From ETP 0.5 0 0.5

Sent to TSDF Site of M/s. VWEMCL through Vapi Waste & Effluent Mgt. Co. Ltd. for final disposal

2 Discarded containers, Nos/month

33.3 Raw

material cons.

100 0 100

Returned back to the supplier / Sold to authorized scrap vendor.

3 Used Oil, lit/year

5.1 D.G. Set 100 0 100 Sold to registered refiners.



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8. WASTE MINIMIZATION AND CLEANER PRODUCTION

8.1. Waste minimization and Cleaner production after proposed expansion at overall scenario shall be as under.

Sr. No.

Particulars Existing After

proposed expansion

Diff. % Diff. Remarks

1 Ketonic Resin production, MT/month 20 100 80.00 400.00

2 Resin Cake as by product, MT/month 0 21.5 21.50 Waste minimization - By product recovery

3 Water consumption, KL/day 19.60 35.97 16.37 83.50 Cleaner production by reducing water requirement

4 Effluent generation, KL/day 10.00 27.02 17.02 170.17 Cleaner production by reducing effluent generation

5 Effluent stream segregation, KL/day

5.1 High COD 8.00 9.45 1.45 18.13 Cleaner production by segregation and treatment of effluent streams at source 5.2 Low COD 0.00 13.67 13.67 100.00

6 Water conservation by recycle/reuse, KL/day 0 3 3.00 100.00

7 Fuel Consumption

7.1 LDO, lit/hr 25 0 -25.00 -100.00 Cleaner production by switching over to cleaner fuel and omitting LDO

7.2 Natural gas, kg/day 100 200 100.00 100.00

7.3 HSD, lit/hr 15 15 0.00 0.00



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8.2. Waste minimization and Cleaner production after proposed expansion per MT of Ketonic Resin manufactured shall be as under.

Sr. No.

Particulars Existing After

proposed expansion

Diff. % Diff. Remarks

1 Resin Cake as by product, MT/month 0 0.215 0.22 Waste minimization - By product recovery

2 Water consumption, KL/day 0.98 0.36 -0.62 -63.30 Cleaner production by reducing water requirement

3 Effluent generation, KL/day 0.50 0.27 -0.23 -45.97 Cleaner production by reducing effluent generation

4 Effluent stream segregation, KL/day

4..1 High COD 0.40 0.09 -0.31 -76.38 Cleaner production by segregation and treatment of effluent streams at source 4.2 Low COD 0.00 0.14 0.14 100.00

5 Water conservation by recycle/reuse, KL/day 0 0.03 0.03 100.00

6 Fuel Consumption

6.1 LDO, lit/hr 1.25 0 -1.25 -100.00 Cleaner production by switching over to cleaner fuel and omitting LDO

6.2 Natural gas, kg/day 5 2 -3.00 -60.00

6.3 HSD, lit/hr 0.75 0.15 -0.60 -80.00



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9. HAZARDOUS CHEMICAL STORAGE & HANDLING:

Sr. No.

Hazardous chemicals Place of storage Storage facility

Mode of Transport

1. Formaldehyde Within the premises

Storage tank By road

2. Cyclohexanone Storage tank

10. NOISE AND ODOUR CONTROL

There is no major activity due to which noise is generated.

The industry has provided acoustic enclosure to the D.G. Set in order to minimize the

noise level.

There is no major generation of bad odor as process is carried out in closed reactors.

11. HEALTH AND SAFETY

The Industry has to be concerned about occupational health and safety among its work force as

the man power is the biggest assert to the industry. Some key safety measures implemented in

the plant and will be followed after proposed expansion.

Safety Training is provided to the employees.

Manual call bells for use in case of emergency are provided.

Emergency Control Room with emergency sirens is established.

Assembly point is provided.

Fire Extinguishers are provided.

First Aid Facility and training is provided.

Personal protective equipment are provided to employees.

Health checkup is organized at regular intervals.

Safety / Health records and MSDS are maintained.

12. RAIN WATER HARVESTING

The industry has decided to implement Rain Water Harvesting to prevent runoff and

help in ground water restoration. It is proposed to collect roof top water in pipes and

drain and which shall be used for recharging of ground water.



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A dedicated Storm water drain shall be provided throughout the site and divert all rain

water to water harvesting ponds without any contamination.

During rainy season, the rain water will be collected from roofs in underground tank and

the collected water will be used for process.

13. GREENBELT DEVELOPMENT

The company has allotted 25 % area for the greenbelt and proposes to utilize maximum open

land for green belt development. The industry proposes to plant different species and variety of

plants in the green belt area.

14. SITE ANALYSIS

14.1. CONNECTIVITY

The project location is well connected with road, rail and air route to transport raw

materials, machineries etc. and hence, it exhibits good potential for industrial growth.

The salient features mentioned below, indicate favorable conditions for industrial

development at the project location.

Particulars Details

Town Vapi – 4 km

Nearest City Valsad - 30 km

River/Streams River Damanganga - 2 km

Nearest Highway NH- 08 - 2 km

Nearest Railway Station Vapi Railway Station - 4 km

Nearest Airport Surat Airpot - 110 km

Tourist places None

Protected areas (National parks/ sanctuaries)

None within 10 km radial periphery

Nearest state boundary State boundary of Gujarat & Maharashtra

Defense installations No defense Installation.

Sites of Historical/ Archaeological Importance

No Sites of Historical/ Archaeological Importance

Densely Populated or built – up Area Vapi town

School/College Vapi town has primary, secondary, higher and CBSC schools as well as Engineering, Medical, Arts, and Commerce & Science colleges.

Hospital Hariya Hospital and private experts of every medicine are available in the area.



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15. CLIMATE DATA FROM THE SECONDARY SOURCE:

Climate Semi-Arid

Seismic Zone II

Maximum temperature, 0C 42 °C

Minimum temperature, °C 8.5°C

Relative Humidity Max.:- 89%; Min.:- 56%

Max Rain Period June to October

16. BUDGETARY PROVISION & PROJECT COST

The company has budgetary provision for the recurring expenses for environmental

issues while planning the allocation of funds during the annual budgetary planning.

The existing shed is sufficient for the proposed expansion. Plant and machinery for the

proposed expansion will be acquired and installed.

Environment Protection has also been considered in planning the Cost Projection. It

includes the installation of ETP for treatment of effluent. Green belt development is also

calculated.

Capital Cost for proposed expansion:

The proposed expansion is in existing premises only.

Cost of the proposed expansion shall be Rs. 10 lac only.

Recurring Cost for Environment Management per month

Sr. No.

Purpose Total Cost,

Rs. lacs

1 ETP (Operations and Maintenance) 0.25

2 Environment & Safety Mgt. System 0.15

3 Greenbelt Maintenance 0.10

4 Expenses for CETP & CSWP facilities 2.25

TOTAL : 2.75



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Conclusion:

As summarized in the above sections, it has been noticed that the proposed expansion project of

Ketonic Resins will not have any major impacts, which can lead to serious issues of environmental

pollution or any other hazards.

Considering the probability of impacts, Resins & Allied Chemicals Industries (Bombay) Pvt. Ltd.

shall plan adequate mitigation measures and EMP. Further, Resins & Allied Chemicals Industries

(Bombay) Pvt. Ltd. has also been planned to organize CSR programs, rainwater harvesting, energy

conservation, which will have considerable beneficial impacts. Looking to the employment

potentials and other allied development potentials, it has been noticed that the proposed project

will significantly help in improving social status of the region.



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Annexure I GIDC plot allotment letter



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Annexure II Membership letter from Vapi Green Enviro Limited



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