Akzo Nobel India Ltd.

January 2017

Pre - feasibility Report

For

Akzo Nobel India Ltd.

Plot E-18, 19, 20 & C-61(Part), MIDC Mahad,Dist:Raigad-402302
Maharashtra, India.

EIA Consultant

M/s. SADEKAR ENVIRO ENGINEERS PVT. LTD.

QCI – NABET accredited EIA consultancy for schedule 5(f) Cat.-‘A’

Certificate No – NABET/EIA/1518/RA 020
NABL Accredited Laboratory, Valid up to 29.06.2018
Lab. Recognized by MoEF& CC, GOI, Valid up to 2.01.2019
Certified by ISO 9001:2008 & BS OHSAS 18001:2007

310, Dempo Towers, EDC Patto, Panaji, Goa state, India. PIN: 403001
Email :sadekarenviro@rediffmail.com / prs@sadekarenviro.com
Web site:-www.sadekarenviro.com Telephone :0832-2437048/2437164
 Akzo Nobel India Ltd. January 2017

Table of Content

Sr. Title Page no.

1 Executive summary 3
2 Introduction of the project 4
3 Description of Project 6
4 Site Analysis 15
5 Planning 19
6 Proposed infrastructure 20
7 Rehabilitation and resettlement 22
8 Project schedule and cost estimation 22
9 Analysis of proposal 22

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1. Executive summary

Salient Features of Project

Name & Address of Company M/s Akzo Nobel India Limited.
Plot E-18, 19,20 & C-61(Part), MIDC Mahad,Dist:Raigad-
Maharashtra, India. PIN: 402302
Schedule of project as per EIA 5(f)
Notification, 2006
Category of Project 'B1'
Total Plot Area Existing, Proposed, Total,
Components sq. m. sq. m. sq. m.

Total plot Area 86478 0 86478

Built up area 8345.7 2002 10347.7
Parking area 2271.8 406.63 1865.1
Green belt 29995 0 29995

Production details Existing capacity: 1997.3 MT/Y

Proposed capacity: 3124.2 MT/Y
Total capacity: 5121.5 MT/Y
By-product: 1296 MT/Y
Water Requirement of Project Existing water requirement : 350 CMD
Total water requirement as after expansion : 640 CMD
Effluent generation Existing Effluent Generation: 233CMD
Proposed Effluent Generation: 263 CMD
Total : 496 CMD
The treated effluent will be discharged to Mahad CETP.
Effluent treatment ETP consisting Primary and secondary treatment by SBR.
ETP Details A salt recovery system will be provided to recover salt from
high TDS stream. 700 CMD ETP consisting primary
treatment with SBR is provided. Additional 250 CMD
capacity SBR will be installed for expansion.
Power Requirement Existing Power Load: 1375 KW
Proposed Power Load: 475 KW
Total Power Load:1850 KW
Source: MSEDCL
Boiler Details Proposed – 2 units of 850 kg/ hr capacity
Fuel requirement HSD : 135 L/hr for D.G.
LDO/ FO: 834 kg/day for boiler
D.G. Set 500 KVA (existing)
Scrubber Existing : 1 unit of alkali scrubber having 40 cum/h fan
capacity , 25 cum/hr water circulation capacity.
Proposed: 1 alkali scrubber of 50 cum/hr capacity
Man power Exiting : 80 employees
Proposed: 40employees
Total: 120 employees
EMP cost (Rs.) 132 Lakh
Project Cost (Rs.) Total: 2404.2 Lakh.

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2. Introduction of the project

2.1 Identification of Project Proponent:

Akzo Nobel India manufactures and markets a wide range of coatings and specialty chemicals.
Around 1,780 people work in the six production facilities, two state-of-the-art research
laboratories and 75 warehouses across India; its retailers are an impressive 8500 and growing.
It attracts some of the best talent in the country, with the ANI workforce comprising people
who are dedicated, highly motivated and determined to succeed.
“A key enabler of our growth strategy is the merger of three Indian subsidiaries of Akzo
Nobel N.V. with Akzo Nobel India. The assets and operations of Akzo Nobel Coatings India,
Akzo Nobel Car Refinishes India and Akzo Nobel Chemicals (India) are now part of our
Company. Hence Akzo Nobel India has the platform and the portfolio to leverage the power
of ‘One Akzo Nobel’ and realise its vision for the future.
So where does the Company see itself, in the future? The targets have been defined—and
ambition is to secure leading position in market segment. And in this passage to accelerated
growth, the Company sees itself upholding all relevant standards of corporate governance,
ethics, sustainability and other pressing issues that dominate world space today.

2.2 Description of project:

The proposed production capacity expansion project of specialty chemicals will be established
at existing production facility. The existing production capacity is 1997.34 MT/year which is
to be expanded up to 5121.5 MT/year. The expansion will be done by installation of additional
equipment in the production unit. Total cost for expansion will be 2404.2 Lakh rupees.

2.3 Expansion need and importance to country:

The company is manufacturing specialty chemicals which are used as precursor in polymer
industry. Due to technology development and market need the demand of any specific
specialty chemical fluctuates as desired raw material for polymers. The company wishes to
capture this higher demand of its products, so that it can supply the specialty chemicals as per
market needs.

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2.4 Demand supply gap:

The major sales of its products are presently in domestic market and if demand exist the
company exports the products. In future the company expected that there is higher need for
some of its products in domestic markets. To capture this opportunity company is expanding
its production capacity of specialty chemicals.
2.5 Import/ export scenario:

India’s polymer industry is major supplier of different types of polymer products globally.
Company’s products are used as initiator in polymer industry. The major supply of its
products is in domestic market and in future it will be the same as demand of its products is
higher. The higher production will be an import substitution for specialty chemicals. This also
leads to generate revenue from domestic market and the company’s clients can manufacture
their products at very competitive price

2.6 Human resources:

Presently company employs about 80 skilled and unskilled employees at its existing unit in
three shifts. In proposed expansion additional 40 employees will be needed.

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3. Description of Project
3.1 Project type

The project is production capacity expansion project of specialty chemicals.

3.2 Location

Company is located at Plot no. E-18, 19, 20 & C-61(Part), MIDC Mahad,District Raigad-
402302. Company has valid consent to operate from Maharashtra Pollution Control Board
for manufacturing of specialty chemicals.

3.3 Details of alternate sites considered

The expansion will be carried out on existing plant. The existing plot area is 86478 sq. m.
which is adequate for the expansion. All other facilities required for production are also
available at plant site therefore no alternate site has been considered for the expansion.

3.4 Size of operation

The exiting production capacity of the unit is 1997.3 MT/year, which will be increased up to
5121.5 MT/year of specialty chemicals. By products of 1296 MT/year will also be produced
after expansion.

3.5 Project description with process detail.

 Production Details

The existing and proposed capacities of products are given in table below.
Existing Proposed Total
Name of Products
(MT/Y) ( MT/ Y) (MT/Y)
Organic Peroxides 3420
1197 2222
(Pure) Total
Refilling/ blending of
800 902 1702
Metal Alkyls (Pure)
Total 1997.3 3124.2 5121.5
By products
Sodium chloride salt -- 1296 1296

The manufacturing process of organic peroxides and stage wise mass balance of
manufacturing of organic peroxide (Trigonox EHPW-60) is explained below.

Details of Manufacturing Process:

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ORGANIC PEROXIDE

The raw materials are dosed into the Stirred Reactor, wherein the reaction occurs under
conditions of controlled temperature. At the end of the reaction, the stirrer is stopped and the
reaction mixture allowed to separate as a product layer and an aqueous layer. The aqueous
layer is then sent to salt recovery. The residual raw material in the product layer is removed by
different aqueous and buffer solution washes. After separation and draining of all there
washes, the product layer is transferred to the Drying Vessel. In the Drying Vessel, dissolved
water present in the product layer is removed by drying over magnesium sulphate.
Subsequently, the product is transferred to a Dilution Tank where it is diluted by solvents to
the required final concentration. From the Dilution Tank, the product is drained into suitable
packaging containers. In the case of a solid product, the product from the Dilution Tank is
transferred to a Drum Flaker and the solid flakes collected are stored in suitable packaging
containers. Final products are stores in refrigerated store rooms at temperature ranging from -
20 C to 10 C depending on the Product.

Mass balance:

MASS MASS
INPUT OUTPUT
(kg) (Kg)

STAGE: 1

Chilled water 700.0 VAPOUR LOSS to 0.0

scrubber
Dequest 2060S 0.79 REACTOR 101 EMISSIONS 0.0
NaOH 25% 5.01 VOL. 3.2 CU. M EFFLUENT 0.0
TEMP: 25 ºC REACTION MASS 705.8
PRESSURE: 1 atm.

TOTAL 706 TOTAL 706

STAGE: 2

H2O2 70% 139 VAPOUR LOSS to 0.0

scrubber
STAGE 1 706 Raw Material EMISSIONS 0.0
MASS Addition
EFFLUENT 0.0
REACTION MASS 844

TOTAL 844 TOTAL 844

STAGE: 3

2-EHCF 935 VAPOUR LOSS to 14.0

REACTION 1
scrubber

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 Akzo Nobel India Ltd. January 2017

NaOH 25% 689 EMISSIONS Nil

STAGE 2 844 Nil
MASS EFFLUENT
REACTION MASS 2455

TOTAL 2469 TOTAL 2469

STAGE: 4

STAGE 3 2455 VAPOUR LOSS 0

MASS
Raw Material
NaOH 25% 48 EMISSIONS 0
Addition
EFFLUENT 0.0
REACTION MASS 2503

TOTAL 2503 TOTAL 2503

STAGE: 5

STAGE 4 2503 VAPOUR LOSS 0

MASS
Chilled water 450 Wash EMISSIONS 0
EFFLUENT 0
Reaction Mass 2953

TOTAL 2953 TOTAL 2953

STAGE: 6

STAGE 5 2953 VAPOUR LOSS 0

MASS
Separation and
EMISSIONS 0
Drain
EFFLUENT 2243
Reaction Mass 710

TOTAL 2953 TOTAL 2953

STAGE: 7

VAPOUR LOSS 0
STAGE 6 710 Product Transfer to EMISSIONS 0
MASS Emulsification
Vessel R201 EFFLUENT 0
Reaction Mass 710

TOTAL 710 TOTAL 710

STAGE: 8

Soft Water 3300 VAPOUR LOSS 0

Reactor 101 EMISSIONS 0
Wash/Rinse EFFLUENT 3300
Reaction Mass 0

TOTAL 3300 TOTAL 3300

STAGE: 9

Chilled water 210 Reactor R 201 VAPOUR LOSS 2.1

Methanol 140 Temperature +15 to EMISSIONS 0

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Berol 08 3.6 -5 ºC EFFLUENT 0

Ethapol XS 19.5 Pressure: 1 atm
Solution
Preparation REACTION MASS 371

TOTAL 373 TOTAL 373

STAGE: 10

STAGE 8 371 VAPOUR LOSS

MASS 0
Product Transfer
Product from 710 EMISSIONS
from R101 and
Stage 7 0
Emulsification
EFFLUENT 0
REACTION MASS 1081

TOTAL 1081 TOTAL 1081.0

STAGE: 11

STAGE 9 VAPOUR LOSS

MASS 1081 0
Chilled water 95 Product Dilution EMISSIONS 0
EFFLUENT 0
REACTION MASS 1176

TOTAL 1176 TOTAL 1176

STAGE: 12

STAGE 10 VAPOUR LOSS

MASS 1176 0
T202 Transfer and
EMISSIONS 0
Packout
EFFLUENT 0
REACTION MASS 1176

TOTAL 1176 TOTAL 1176

STAGE: 13

Soft Water 3300 VAPOUR LOSS 0

Reactor 201 and EMISSIONS 0
T202 Wash/Rinse EFFLUENT 3300

TOTAL 3300 TOTAL 3300

3.6 Raw material details

The raw material details are given in following table. Existing raw material use is 2283.2 MT/
year. After expansion it will be 10,021.38 MT/ year.

Sr. Name Existing Proposed Total Source Means of

No. MT/year MT/year MT/year of Transportation
Material

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 Akzo Nobel India Ltd. January 2017

1 2-Ethyl hexyl 420.0 0.0 420.0 Local Road

chloroformate
2 Pivaloyl chloride 24.0 92.0 116.0 Local Road
3 Benzoyl chloride 30.0 134.0 164.0 Local Road
4 Isopropyl 18.0 0.0 18.0 Imported Sea
chloroformate
5 Isododecane 18.0 302.0 320.0 Imported Sea
6 RAV 7AT 60.0 0.0 60.0 Imported Sea
7 Magnesium sulphate 12.0 14.0 26.0 Imported Sea
8 Sodium chloride 180.0 355.9 535.9 Local Road
9 Sodium bicarbonate 6.0 0.0 6.0 Local Road
10 Sodium 12.0 23.1 35.1 Local Road
metabisulphite
11 Sodium sulphate 2.4 0.0 2.4 Local Road
12 Tert.buty 420.0 696.4 1116.4 Imported Sea
hydroperoxide 70 %
13 Hydrogen peroxide 70 96.0 290.5 386.5 Local Road
%
14 Acetic acid 12.0 5.3 17.3 Local Road
15 Sulphuric acid 12.0 100.0 112.0 Local Road
16 Sodium hydroxide 420.0 1955.3 2375.3 Local Road
(30%)
17 Potasium hydroxide 18.0 8.5 26.5 Local Road
18 2-EHCL 96.0 130.0 226.0 Local Road
19 Neo deconoyl chloride 54.0 0.0 54.0 Local Road
20 Methanol 78.0 285.2 363.2 Local Road
21 1,1,3,3 tetra methyl 54.0 0.0 54.0 Imported Sea
butyl Hydroperoxide
22 Methyl ethyl ketone 12.0 57.2 69.2 Local Road
23 Alcotex 12.0 0.0 12.0 Imported Sea
24 Isopar H 12.0 320.0 332.0 Imported Sea
25 Toluene 96.0 268.0 364.0 Local Road
26 Na2CO3 solid 1.0 0.0 1.0 Local Road
27 Dequest 2060 S 0.6 7.5 8.1 Imported Sea
28 Dimethylphthalate 42.0 28.7 70.7 Local Road
29 Isobutyryl Chloride 12.0 1108.0 1120.0 Local Road
30 Acetyl acetone 12.0 1.0 13.0 Imported Sea
31 Ethapol 12.0 79.0 91.0 Imported Sea
32 Diethylene Glycol 30.0 1.4 31.4 Local Local
33 Spirdane D60 0.0 350.0 350.0 Imported Sea
34 Berol 0.0 2.4 2.4 Local Road
35 HCL 30% 0.0 490.0 490.0 Local Road
36 Isononanoyl Chloride 0.0 195.0 195.0 Imported Sea
37 Cyclohexanone 0.0 12.0 12.0 Imported Sea
38 Isononanoic Acid 0.0 5.0 5.0 Imported Sea
39 Calcium Carbonate 0.0 150.0 150.0 Local Road
40 Silica 0.0 45.0 45.0 Local Road
41 TBA 0.0 25.0 25.0 Imported Sea
42 Diisopropanol 0.0 100.0 100.0 Imported Sea

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Benzene
43 Sodium Perchlorate 0.0 50.0 50.0 Local Road
44 DHP 0.0 50.0 50.0 Imported Sea
Total 2284 7737.38 10021.38

3.7 Resource optimization ( recycle/ reuse)

 A salt recovery plant is proposed to recover valuable salt from effluent stream. The part
quantity of recovered salt will be utilized in manufacturing process or will be sold as
byproduct i.e.1296 MT/year sodium salts. The remaining quantity i.e. 144 MT/Y would
be disposed through the CHWTSDF.

3.8 Availability of water, energy fuel

Sr. Particular Existing After expansion

(Total)
1 Water 350 CMD 640 CMD
Supply from : MIDC
2 Energy 1375 KW 1850 KW
3 Fuel
HSD for D.G. set 135 L/ hour Same as existing.
500 KVA
Boiler -- 834 kg/day
LDO/ FO

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Water balance calculations for expansion unit

as
per
CTO EFFLUENT, CMD
,
COMPONEN CM
T D CONSUMPTION, CMD LOSS, CMD RECYCLE, CMD DOMESTIC PROCESS
Existin Propose Tota Existin Propose Tota Existin Propose Tota Existin Propose Tota Existin Propose Tota
g d l g d l g d l g d l g d l

Domestic 55 5 5 10 1 1 2 0 0 0 4 4 8 0 0 0
Process 635 235 235 470 5 5 10 0 0 0 0 0 0 230 230 460

Cooling tower 100 10 10 20 7 7 14 0 0 0 0 0 0 3 3 6

Boiler 0 0 40 40 0 0 0 0 10 10 0 0 0 0 30 30
Gardening 100 100 0 100 100 0 100 0 0 0 0 0 0 0 0 0
Total 890 350 290 640 113 13 126 0 10 10 4 4 8 233 263 496

Water requirement as per valid CTO : 890 CMD

Present water consumption: 350 CMD

Water consumption after expansion: 640 CMD

Effluent generation after expansion: 496+8 = 504 CMD

 Akzo Nobel India Ltd. January 2017

3.9 Quantity of waste to be generated

1. Hazardous waste

Particulars Category Existing Proposed Total, Method of

Sr. TPA TPA TPA Disposal
No

1 Alkali residue 12.2 20.0 -- 20.0 CHWTSDF

2 Chemicals containing
residue from 33.1 2.4 2.6 5.0 CHWTSDF
decontamination
3 Used/ spent oil MPCB
5.1 2.4 2.4 4.8 authorized
recycler
4 CHWTSDF/
MPCB
Spent Solvents 20.2 12.0 12 24 authorized
recycler

5 Discarded containers CHWTSDF /

barrels/liners/ plastic MPCB
33.3 120 nos. 120 nos. 240 nos.
bags/ PPE etc authorized
recycler
6 Chemical sludge from
34.3 7.2 6.8 14 CHWTSDF
wastewater treatment
7 Evaporation Salt
37.2 - 144 144 CHWTSDF
(NaCl)

2. Non hazardous waste

Particulars Existing, Proposed Total, TPA Method of Disposal

Sr. No TPA

Plastic waste, 120 24 144 Sale to MPCB

1 plastic wrappers, approved scrap
scrap dealers

3. Effluent generation:

Domestic effluent generation: 8 CMD

Process effluent: 460 CMD

Cooling tower blowdown: 6 CMD

Boiler blowdown: 30 CMD

Total Effluent generation after expansion: 496 CMD. The domestic and process effluent is

treated in 700 CMD ETP consisting of primary treatment and sequencing batch reactors as
 Akzo Nobel India Ltd. January 2017

secondary treatment. A salt recovery system of 21 CMD capacity will be provided to

recover salt from high TDS effluent stream. One additional SBR of 250 CMD capacity is

proposed.

3.10 Schematic Representation of the Feasibility Drawing of EIA

RESOURCE CONSUMPTION POWER CONSUMPTION

(WATER)

RAW MATERIAL

PRODUCTION ACTIVITY

WASTE FINISHED PRODUCTS

GENERATION

POLLUTION
ABATEMENT EMPLOYMENT MARKET

CLEAN
ENVIRONMENT ECONOMY

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4. Site Analysis
4.1 Connectivity
The project is located in Mahad industrial area which is easily accessible from Mumbai- Goa
highway, further connecting to the project site by internal access roads developed by MIDC.
Nearest Railway Station: Veer, approximately at a distance of 18 km.
Nearest Airport: Chatrapati Shivaji International Airport approximately at a distance of 166
km.
Location and Access
The industrial area is centrally located and easily accessible through all modes of transport.
Road: The entire industrial area is well connected by internal roads.
Available Road Network: Mumbai – Goa highway (NH 66) at a distance of approximately 4
km from the project site.

4.2 Land Form, Land use and Land Ownership

The Project location & the surrounding environs being located in the notified industrial area
prevails industrial land use form.

Area details:
Existing, Proposed, Total,
Components sq. m. sq. m. sq. m.

Total plot Area 86478 0 86478

Built up area 8345.7 2002 10347.7
Parking area 2271.8 406.63 1865.1
Green belt 29995 0 29995

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PLOT LAYOUT
 Akzo Nobel India Ltd. January 2017

4.3 Topography:
The co-ordinates of the project site are 18° 6'43.11"N and 73°29'27.24"E. The toposheet 47
F/8 is given below to show the topography of surrounding area.

Akzo Nobel India Ltd.

Plot E-18, 19,20 & C-61(Part),
MIDC Mahad,Dist:Raigad
Toposheet no. : 47 F/8
 Akzo Nobel India Ltd. January 2017

4.4 Existing infrastructure

The existing manufacturing facility has all adequate infrastructure required for production.
The manufacturing plant building, utility building, paved internal roads, electrical sub station,
storage yard, ETP etc. the plot layout is given below to show exact location of infrastructure
available in the unit.

4.5 Soil classification

The soils in the area are formed from the Deccan Trap which is predominating rock formation
with small out crops of Laterite at a few places in the Poladpur taluka. The soils are medium
black and black soil which can be further grouped as Forest, Varkas, Rice, Khar or Saline,
Coastal Alluvium and Laterite as per the location and topographical situation.

4.6 Climatic data from secondary sources

The climate in proposed area is characterized by hot summer and general dryness throughout
the year except the south west monsoon season.

Climate Classification: Project site features a semi arid climate. In rainy season the climate is
very humid.

Temperature: annual average max. Temperature is 32°C and min. temperature is 17 °C

Rainfall: The analysis of long term rainfall data indicates that normal annual rainfall over the
district ranges from 2200 mm to more than 3000 mm in the plains and it is above 5000 mm in
the hills. The average rainfall around Mahad area is 3360 mm in rainy season.

4.7 Social infrastructure available:

The unit is in Mahad MIDC area. Social infrastructure is available near Mahad MIDC.

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5. Planning Brief
5.1 Planning concept:
 The expansion work will be started after receiving environmental clearance. The time
schedule and planning of expansion will be determined after discussion with architect and
civil contractors.
 The Mahad MIDC have adequate road network and water will be provided by MIDC,
therefore company will not be relied on ground water in the MIDC area.
 Electricity is provided by MSEDCL. No additional power transmission lines are required.
 The construction material is available locally and it will be transported through road
network.

5.2 Population projection:

As per the 2011 census data, the Mahad region have 1,80,191, of which 88,734 are males and
91,457 are females. Total 19,044 population is lied in 0-6 year age group. According to census
data total literates are 1,31,981.
The data published by census India 2011, shows that density of Raigad district for 2011 is 368
people per sq. km. It is assumed that due to proposed project minor migration of skilled labour
in the region is expected after commissioning of the project.

5.3 Land use planning:

The expansion will be carried out at existing site at Mahad MIDC. The land is acquired by
MIDC and the land use will be industrial type. No cultivated land or forest land will be
utilized for the proposed unit.

5.4 Assessment of Infrastructure demand

The major physical infrastructure like road, water supply is provided by Mahad MIDC. The
electricity will be supplied by MSEDCL by means of continuous feeder substation.
The industrial infrastructure will be constructed after grant of EC. The need of social
infrastructure is not presently envisaged.

5.5 Amenities:
Basic amenities like road, electricity, process water will be available at site. The drinking
water will be provided by further purification of process water by RO purification unit. In the
plant personal hygiene facilities will be provided to workers as per the rule.

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6. Proposed infrastructure
6.1 Industrial area
The proposed expansion of Akzo Nobel India Ltd. will be carried out at existing
manufacturing site at Plot E-18, 19,20 & C-61(Part), MIDC Mahad.

6.2 Residential area

The unit is specialty chemicals manufacturing unit and situated at notified Mahad MIDC area
therefore there will be no need of residential infrastructure.

6.3 Green belt

Total 29,995 sq. m. green belt area is provided in the plant. The proposed expansion will not
required any clearance of green belt within the premise therefore the area of green belt will
remain same after expansion.

6.4 Social infrastructure:

The project site is approximately 8 km from Mahad city. All basic social infrastructure
facilities are available in the study area.

6.5 Connectivity
The site can be accessed by national highway and connecting state highway from Mahad to
Solamkund village. The Mahad MIDC have excellent internal and connecting road network
therefore no additional connectivity infrastructure will be constructed.

6.6 Sewerage system

The internal storm water drains are provided in the plant which are connected to MIDC sewer
network. The existing sewage generated from the daily activities is mixed with effluent and
presently treated at ETP of 700 cu. m capacity. The treated effluent is discharged to CETP,
Mahad.

6.7 Industrial waste management

The effluent generated from existing production activities is treated at ETP of 700 CMD
capacity, consisting primary as well as secondary treatment. The treated effluent will be
discharged to CETP, Mahad.

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6.8 Solid waste management

The hazardous waste is presently segregated as per category in schedule I of “Hazardous and
Other Wastes (Management and Transboundary Movement) Rules, 2016” and it is stored in
the demarcated area. The hazardous waste is disposed through CHWTSDF or it is sold to
MPCB authorized re-processing vendors.

6.9 Power requirement/ supply/ source

For proposed expansion, total 475 KW electrical load will be required. the final power load
will be 1850 KW.

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7. Rehabilitation and resettlement:

The unit will be established in notified industrial area of Mahad MIDC. No rehabilitation and
resettlement will be envisaged.

8. Project schedule and cost estimation

It is proposed that the project will be commissioned after 12 months from grant of EC. The
cost estimation is presented in CA certificate attached as annexure 1.

9. Analysis of proposal :
 Proposed production activity will provide employment to the local residents, resulting
financial and social benefits of the nearby people.
 Indirect employment will be generated by the proposed unit like canteen, transportation
facilities to workers.
 The export will result in generation of foreign exchange to the country.

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Annexure 1: CA certificate

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