prefeasibility report for godavari bio-refineries...

P r e f e a s i b i l i t y R e p o r t f o r P r o p o s e d S p e c i a l i t y C h e m i c a l P l a n t b y

GO DA V A RI C EL LU LO S I CS L TD

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CONTENTS

1.0 EXECUTIVE SUMMARY ................................................................................................. 4

2.0 INTRODUCTION OF PROPOSED PROJECT .................................................................. 8

2.1 Project Proponent ............................................................................................................. 8

2.2 Nature of the Project ........................................................................................................ 8

2.3 Need of the Project ........................................................................................................... 9

2.4 Demand – Supply Gap & Import Vs Indigenous Production ........................................ 10

2.5 Employment Generation ................................................................................................ 10

3.0 PROJECT DESCRIPTION ................................................................................................ 11

3.1 Type of Project ............................................................................................................... 11

3.2 Location of Project : ....................................................................................................... 11

3.3 Alternative Site ............................................................................................................... 13

3.4 Size of Operation ............................................................................................................ 14

3.5 Products & Manufacturing Process ................................................................................ 14

3.5.1 Sorbic Acid / Potassium Sorbate.................................................................................. 16

3.5.3 Acetaldehyde................................................................................................................ 18

3.5.4 Crotonaldehyde ............................................................................................................ 19

3.5.5 Ethyl Acetate ................................................................................................................ 20

3.5.6 3 Methoxy Butanol ...................................................................................................... 21

3.5.7 Cellulose Acetate ......................................................................................................... 22

3.5.8 Cellulose Acetate Butyrate .......................................................................................... 22

3.5.9 Microcrystaline Cellulose ............................................................................................ 24

3.5.10 Acetophenone ............................................................................................................ 25

3.5.11 Acetonitrile ................................................................................................................ 26

3.5.12 Phenyl Ethyl Alcohol ................................................................................................. 27

3.6 Raw Materials ................................................................................................................ 28

3.7.1 Land ........................................................................................................................ 30

3.7.2 Water ....................................................................................................................... 31

3.7.3 Electricity ................................................................................................................ 32



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3.7.4 Fuel .............................................................................................................................. 32

3.7.5 Manpower .................................................................................................................... 32

3.7.6 Utility ........................................................................................................................... 33

3.8 Waste to be generated .................................................................................................... 34

3.8.1 Sewage .................................................................................................................... 34

3.8.2 Effluent ................................................................................................................... 34

3.8.3 Air Emission ........................................................................................................... 36

3.8.4 Solid/Hazardous Waste ........................................................................................... 37

3.8.5 Noise ....................................................................................................................... 38

3.9 Purpose of EIA Study ..................................................................................................... 38

4.0 SITE ANALYSIS .............................................................................................................. 39

4.1 Connectivity ................................................................................................................... 39

4.2 Land form & Land Use .................................................................................................. 39

4.3 Topography .................................................................................................................... 40

4.4 Existing Infrastructure (Social/Commercial) ................................................................. 40

4.5 Soil Classification .......................................................................................................... 41

4.6 Climatic data from secondary sources ........................................................................... 41

5.0 PLANNING BRIEF ........................................................................................................... 41

5.1 Population Projection ..................................................................................................... 41

5.2 Land use Planning .......................................................................................................... 42

5.3 Amenities / Facilities ...................................................................................................... 42

6.0 PROPOSED INFRASTRUCTURE ................................................................................... 42

7.0 REHABILITATION & RESETTLEMENT (R&R) PLAN: ............................................. 43

8.0 PROJECT SCHEDULE & COST ESTIMATION: ........................................................... 43

8.1 Project Schedule ............................................................................................................. 43

8.2 Cost Estimation .............................................................................................................. 43

9.0 ANALYSIS OF PROPOSAL: ........................................................................................... 44

9.1 Financial & Social Benefits............................................................................................ 44



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LIST OF TABLE

TABLE 1.1 : PROJECT SUMMARY ........................................................................................................ 5

TABLE 1.2 : PROPOSED PRODUCTS .................................................................................................. 15

TABLE 1.3 : RAW MATERIAL REQUIREMENT ..................................................................................... 28

TABLE 1.4 : LAND BIFURCATION ...................................................................................................... 30

TABLE 1.5 : WATER CONSUMPTION .................................................................................................. 31

TABLE 1.6 : WASTEWATER GENERATION........................................................................................... 35

TABLE 1.7(A) : FLUE GAS EMISSION ................................................................................................ 36

TABLE 1.7(B) : PROCESS EMISSION .................................................................................................. 36

TABLE 1.8 : SOLID/HAZARDOUS WASTE GENERATION & MANAGEMENT ............................................ 37

TABLE 1.9 : ENVIRONMENTAL SETTINGS ........................................................................................... 40

TABLE 1.10 : PROPOSED INFRASTRUCTURE ...................................................................................... 42

TABLE 1.11 : PROJECT COST ........................................................................................................... 44

LIST OF FIGURE

FIGURE 1.1: LOCATION OF ATALI VILLAGE & KEY MAP OF GCL .................................................. 12

FIGURE 1.2 : GOOGLE IMAGE OF PROPOSED PLANT BY GCL .......................................................... 13



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1.0 EXECUTIVE SUMMARY

Somaiya Group is one of the old and well established Industrial houses in India. The Somaiya Group was

founded and promoted by Late Shri. Karamshibhai Jethabhai Somaiya (Padmabhushan) and developed

and steered by his son, Late Dr. Shantilal Karamshibhai Somaiya, was incorporated in 1939 and has been

contributing to the industrial development of India for more than six decades.

Somaiya Group has plants located in the states of Karnataka and Maharashtra & has diverse interests in

Sugar, Power, Industrial Alcohol, Heavy Organic Chemicals, Specialty Chemicals, Bio-fertilizers &

Agricultural Research. It manufacturers more than twenty products from renewable resources, thereby

forming an entire Value Chain right from Sugar Cane to Sugar to other value added products like Power,

Ethanol, Bio-fertilizers, alcohol based chemicals including speciality chemicals.

Somaiya Group has decided to have a multi-product facility in Gujarat and as a part of implementation of

management decision a company ―GODAVARI CELLULOSICS LTD.‖ was form in the year 2011 for

production of speciality chemicals.

The pre-feasibility report includes a brief introduction of the company, need and justification of the

project, manufacturing process description, required and available resources, proposed Environment

Management Systems, land-use and proposed infrastructure, project schedule and cost.

GCL has engaged Eco Chem Sales & Services, Surat (NABET Accredited consultant by QCI) as their

Environmental Consultant to conduct the EIA studies for obtaining Environmental Clearance (EC) for the

proposed venture at Atali Village. Proposed project at a glance is mentioned in table 1.1.



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Table 1.1 : Project Summary

S.

No. Description Proposed Project Details

1. Name of project Environmental clearance for proposed manufacturing of Speciality

Chemicals plant by Godavari Cellulosics Ltd.

2. Project Site R.S. No: 142, 151, 152, 153/1, 154, 155, 156, 157, 158, 159, 160,

PCPIR notified industrial area, Village – Atali, Tal-Vagra, Dist – Bharuch,

Gujarat

3. Project Category 5(f) Category ―B‖ of EIA notification.

4. Capital Cost Rs. 250.00 Crores

5. Products

S.No. Product Quantity

in MTPM

1 Sorbic Acid/Potassium Sorbate 425

2 1, 3 Butylene Glycol 325

3 Acetaldehyde 575

4 Crotonaldehyde 425

5 Ethyl Acetate 825

6 3 Methoxy Butanol 325

7 Cellulose Acetate 825

8 Cellulose Acetate Butyrate 425

9 Microcrystaline cellulose 250

10 Acetophenone 825

11 Acetonitrile 825

12 Phenyl Ethyl Alcohol 425

Total 6475

6. Raw Materials Ref. Section –3.6

7. Resource Requirement

(i) Land Total plot area – 319655 m2 (Out of 319655.00 m

2 area approx. 168194 m

2



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S.


will be utilized for proposed project and remaining 151461 m2 area will be

kept open for future use.)

(ii) Water Source: GIDC Reservoir

Construction phase:

Domestic – 7 KLD

Construction activities and curing – 13 KLD

Operation phase :

Industrial – 1422 KLD

Domestic – 35 KLD

Gardening – 10 KLD

In addition to above treated STP water will be used.

(iii) Electricity Proposal to set steam back pressure turbine of capacity 3x3 MWH.

Backup power Gujarat State Electricity Board

Electricity: 33KVA, 50 Hz, back up 2 nos. of D.G. Set (250 KVA)

(iv) Fuel Imported Coal – 130 TPD

Furnace Oil – 300 LPD

(v) Man power Construction Phase: 150 Nos.

Operation Phase: 755 Nos.

(vi) Utility Coal fired Steam Boiler – 30 TPH (2 Nos.)

Cooling Tower – 300 m3/Hr. (5 Nos.)

Air Compressor – 450 CFM

Thermic Fluid Heater – 5 Lakh Kcal/Hr.

Incinerator – 5 KL

Steam Back Pressure Turbine – 3x3 MWH

RO Plant – 1356 KL (4 Nos.)

MEE (1) – 414.5 KL (4 Nos.)

MEE (2) – 388 KL (4 Nos.)



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S.


8 Source of Pollution

(i) Wastewater

Generation

Effluent – 1357 KLD

Sewage – 28 KLD

(ii) Air Emission From Heater & Boiler and D.G. Set

PM : <150 mg/Nm3

SO2 : < 100 ppm

NOx : <50 ppm

From Process Emission

HCl : < 20 mg/Nm3

NH3 : 175 mg/Nm3

(iii) Solid/Haz.

Waste Generation

STP sludge, Used Oil, Discarded Containers, Incineration Ash, MEE Salt

Spent Catalyst

9 Treatment Facility

(i) Wastewater The low COD/TDS streams of liquid effluent will be treated in an

effluent treatment plant having primary, secondary and tertiary

treatment facility.

The high COD/TDS streams of liquid effluent will be treated in multi

effect evaporators.

Treated effluent from ETP will further treated in RO plant to achieve

the ZERO effluent liquid discharge.

(ii) Air Air pollution control device such as cyclone separator, Bag filter, Alkali

Scrubber etc. shall be provided to achieve GPCB norms.

(iii) Solid Waste Collection, storage and disposal of solid/hazardous waste to be carried out

as hazardous waste management rules.

10 Resource Recovery

(i) Water The condensate from MEE and RO permeate water will be reused

back in to the cooling tower.

Treated sewage coming out of STP shall be used for toilet flushing and



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S.


greenbelt development.

(ii) Solvent Solvent recovery shall be done and reused back to process.

The solid, liquid and gaseous wastes from the proposed plant will be disposed-off in an environmentally

acceptable manner. Process effluents will be properly treated in adequate effluent treatment plant and

treated wastewater will be recycled back to process for reuse. Proper precaution will be taken and

adequate green belt will be developed to keep noise level within prescribed limit. Adequate measure has

been contemplated to ensure least pollution from the proposed project.

2.0 INTRODUCTION OF PROPOSED PROJECT

2.1 Project Proponent

The Somaiya group is involved in various area such as sugar and its allied products, alcohol and bulk

organic chemicals, specialty chemicals and now diversified there interest to have a multi-product facility

for manufacturing different range of chemicals i.e. Heavy Organic Chemicals, Specialty Chemicals,

Bio-fertilizers & Agricultural Research in Gujarat. Godavari Cellulosics Ltd. (GCL) is belonging to

Somaiya Group.

Godavari Bio-refineries Ltd. (GBL) – a flagship company of Somaiya group is being run by Shri Samir

Somaiya - present Chairman and Managing Director of company and his professional team. GBL has very

big and modern sugar mill fully integrated with Distillery plant and Cogeneration plant. It is among the

top ten Sugar complexand a pioneer in manufacture of Alcohol based Chemicals and specialty chemicals

in India.

2.2 Nature of the Project

Proposed project is Greenfield project to be developed at R.S. No. 142, 151, 152, 153/1, 154, 155,

156, 157, 158, 159, 160, PCPIR notified industrial area, Village – Atali, Tal-Vagra, Dist – Bharuch of

Gujarat state. Various speciality chemicals as mentioned in section – 3.5 to be manufactured after

obtaining environmental clearance from SEAC, Gandhinagar. Proposed project is fall under 5(f) category

―B‖ of EIA notification.



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2.3 Need of the Project

The chemical industry in India is witnessing a structural change and companies are realigning their

strategies and consolidating themselves to face stiff competition from global companies. The high speed

of economic reforms and a GDP growth, there are bright prospects for the chemical industry and specialty

chemicals strives to be a part of this growth by keeping itself updated with the state-of-the-art

technologies for it's portfolio of products. Following pie chart shows world consumption of specialty

chemicals by type:

Figure: Consumption of Speciality Chemicals – 2014

In 2014, the world’s five largest specialty chemicals segments—specialty polymers, construction

chemicals, industrial and institutional cleaners, electronic chemicals, and surfactants—had a market share

of about 37%; the 10 largest segments accounted for 61% of total annual specialty chemicals sales. The

specialty chemicals industry is now trying to improve its margins by implementing price increases to

compensate for higher R&D, energy, and raw material costs. The specialty chemicals business is in

transition. Historically, North American, Western European, and Japanese firms have dominated this

business. However, with trade liberalization, the spread of process technology, the breakdown of

numerous economic barriers, the rapid growth of the newly industrialized Asian economies and rising

standards of living in many developing countries, the center of gravity of the global chemical industry is

shifting toward the Middle East, where cheap petrochemical feed stocks are available, and toward Asia,

where labor costs are low and economic growth is high. During 2014 – 19, volume consumption of

specialty chemicals is expected to increase at close to 4% on a global basis. In general, the emerging



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markets offer more dynamic prospects for the specialty chemicals industry because of rising consumer-

driven economies and industrialization. Proposed specialty chemical plant will further induce secondary

industrialization based on their respective derivatives and generate the employment directly and

indirectly. In view of above chemical market scenario, project proponent proposes a plant to manufacture

specialty chemical at PCPIR, Dahej to spread the company business, increase tune over as well as to

provide better service to local peoples.

2.4 Demand – Supply Gap and Import vs Indigenous Production

Indian Specialty Chemicals poised to be $ 80-100 billion industry by 2020. Asia-Pacific region now

is nearly 42 % of the global market for chemicals.

India is emerging as manufacturing and export hub for specialty chemicals. Key advantages include

re-engineering capabilities and relatively low cost of production.

Innovation and Scale will be the key differentiators, going forward.

The continuous growth of chemical sector saw demand – supply gap and some times, molecules are

not available both for the domestic and export market. Like the many other products, specialty

chemical are made in India and exported to all the European Countries as well as other countries.

Continuous growth of exports and increase in the Indian market demand off set the local

competitions.

Some manufacturing capacities cleared for the manufacture are neither installed nor operated. Some

products are not available at the peak demand time of the local season.

To support the above projections, promoters have propelled to set up new manufacturing facility in

PCPIR.

2.5 Employment Generation

There are possibilities to generate employment during the construction as well as operation phase of the

proposed project. Local skilled and semi-skilled workers will be hired during construction phase, thus no

need to provide housing facility to workers. 150 nos. of people will get direct employment during

construction phase.



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Technical staff for plant operation, general staff for administrative work and other ancillary services i.e.

Security, O&M contractor and maintenance services will required during operation phase. 755 nos.

people (staff + contractor) will get direct and indirect employment during this phase.

3.0 PROJECT DESCRIPTION

3.1 Type of Project

Proposed project is Green field project to be developed by Somaiya group in PCPIR notified industrial

area. All the industrial infrastructure facility is being available at PCPIR to support proposed

development.

3.2 Location of Project

Godavari Cellulosics Ltd. (GCL) is belonging to Somaiya Group and decided to set an industrial plant at

R.S. No. 142, 151, 152, 153/1, 154, 155, 156, 157, 158, 159, 160, PCPIR notified industrial area, Village

– Atali, Tal-Vagra, Dist – Bharuch, Gujarat. For development of proposed industrial plant, GCL has

procured 3,19,654.75 m2 from PCPIR authority. Location of Atali village and Key map and

Google image of proposed project site is depicted as figure 1.1 & 1.2 respectively. Proposed

project coordinate is as under:

Latitude : 22042’52.93’’ N

Longitude : 72042’16.09‖ E



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Figure 1.1: Location of Atali Village & Key map of GCL



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Figure 1.2 : Google Image of proposed plant by GCL

Layout plan showing complete manufacturing facility, greenbelt area, treatment facility, parking, entry

and exit gate etc. is attached as Annexure – 1 with ToR application. Proposed project is located in

PCPIR notified industrial area. National park, Reserve forest, Biosphere reserves, Wild life sanctuary,

Archaeological place, Eco sensitive area etc. are not located within the 10 Km radius of the proposed

project.

3.3 Alternative Site

A suitable site must be found for a new/green field project, and the site and equipment layout planned

accordingly. Provision must be made for the ancillary buildings and services needed for plant operation;

and for the environmentally acceptable disposal of effluent/emission/waste. Many factors must be

considered when selecting a suitable project site. The principle factors to consider are given below:

Distance between project site and potential marketing area.

Availability of Raw materials and utilities i.e. water, fuel, power,

Transport facility,

Supply of labour,

Availability of suitable land and climate,



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Environmental impact and waste disposal,

Local community considerations,

Political and strategic considerations.

PCPIR notified industrial area have all required infrastructure for industrial development as well as it full

fills all the above factors, thus project proponent has decided to develop a specialty chemical plant within

PCPIR and no other alternative site study has been conducted.

3.4 Size of Operation

Project proponent proposes to manufacture specialty chemicals with production capacity of 259 MTPD.

Product wise quantities are incorporated in section – 3.5 of prefeasibility report.

3.5 Products & Manufacturing Process

GCL has observed that there are good scopes in speciality chemicals sector and there will be demand for

these sectors perennially. GCL aims to engage in R&D and entering new markets in order to make new

products and derive the maximum value from feedstock by adopting modern machineries, equipments and

process technologies, with emphasis on waste minimization techniques.

List of proposed products/by-products and intermediate products to be manufactured by GCL is

mentioned in table – 1.2.



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Table 1.2: Proposed Products

S. No. Name of Products Quantity in

MTPM

1. Sorbic Acid / Potassium Sorbate 425

2. 1, 3 Butylene Glycol 325

3. Acetaldehyde 575

4. Crotonaldehyde 425

5. Ethyl Acetate 825

6. 3 Methoxy Butanol 325

7. Cellulose Acetate 825

8. Cellulose Acetate Butyrate 425

9. Microcrystaline cellulose 250

10. Acetophenone 825

11. Acetonitrile 825

12. Phenyl Ethyl Alcohol 425

TOTAL 6475

Manufacturing process of various speciality chemicals, chemical reaction and mass balance for

production of one tone of proposed product is mentioned below:



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3.5.1 Sorbic Acid / Potassium Sorbate

Sorbic acid is basically reaction of croto and ketene, Ketene can be generated internally

involving reaction of acetic acid cracking and then condensation reaction with crotonaldehyde to

make Sorbic Acid.

Chemical Reaction:

Process Block Diagram:

Reaction 1 CH3COOH CH2=C=O + H2O

Name Acetic Acid Ketene Water

Mol.wt 60 42 18

Reaction 2 CH2=C=O + CH3CH=CHCHO CH3CH=CHCH=CHCOOH

Name Ketene Crotonaldehyde

Mol.wt 42 70

Reaction 3 CH3CH=CHCH=CHCOOH + KOH CH3CH=CHCH=CHCOOK + H2O

Name

Sorbic

Acid Potasium Hydroxide Potassium Sorabte Water

Mol.wt 112 56 150 18

Sorbic Acid

112

Acetic Acid

Crude Sorbic Acid

Reaction 1TEP (Catalyst)

Ketene Reaction 2Catalyst

Crotonaldehyde

Pure Sorbic Acid

Waste water

PurificationWater

Water to ETP

Crude Sorbic Acid Potasium Sorbate



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3.5.2 1, 3 Butylene Glycol (1,3 BG)

1, 3 Butylene Glycol is basically produced by hydrogenation of acetaldol and acetaldol is

produced from acetaldehyde. Aldol used for 1,3 Butylene Glycol production is 60 % purity &

according to that consumptions norms are evaluated .

Chemical Reaction:

Process Block Diagram :

Reaction 2 CH3CHO CH3CHOHCH2CHO

Name Acetaldehyde

Mol.wt 88

Reaction 2 CH3CHOHCH2CHO + H2 C4H10O2

Name Hydrogen

Mol.wt 2

Acetaldol

88

1,3 BG

9088

Acetaldol

Process Block Diagram -

AcetaldehydeReaction 1

CondensationAcetaldol Reaction 2

Hydrogenation

Hydrogen

crude 1, 3 BG Distillation Final Product

Waste WaterWater to ETP



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3.5.3 Acetaldehyde

Acetaldehyde can be prepared by the partial oxidation of ethanol, in an exothermic reaction.

This process typically is conducted over a silver catalyst at about 500–650 °C

Chemical Reaction:

Process Block Diagram :

Reaction C2H5OH + 1/2 O2 CH3CHO + H2O

Name Ethanol Oxygen Water

Mol.wt 46 16 18

Acetaldehyde

44

Ethanol Reaction 1

AIR

Acetaldehyde

Water

PurifiCation Distillation

Waste Water Water to ETP



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3.5.4 Crotonaldehyde

Crotonaldehyde is produced by the aldol condensation of acetaldehyde: Its main application is as

a precursor to fine chemicals. Sorbic acid, a food preservative, and trimethylhydroquinone, a

precursor to the vitamin E, are prepared from crotonaldehyde.

Chemical Reaction:


Reaction 2 CH3CHO CH3CHOHCH2CHO

Name Acetaldehyde

Mol.wt 88

Reaction 2 CH3CHCHCHO + H2O

Name Crotonaldehyde Water

Mol.wt 70 18

Acetaldol

88

CH3CHOHCH2CHO

Acetaldol

88

Acetaldehyde Reaction 1 Acetaldol Reaction 2 Crotonaldehyde

Water

Purification

Waste Water to ETP



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3.5.5 Ethyl Acetate

Ethyl acetate is synthesized in industry mainly via the classic Fischer esterification reaction

of ethanol and acetic acid. The reaction can be accelerated by acid catalysis and the equilibrium

can be shifted to the right by removal of water.

Chemical Reaction:


Reaction CH3COOH + C2H5OH CH3COOC2H5OH + H2O

Name Acetic acid Ethanol Water

Mol.wt 60 46 18

Ethyl Acetate

88

Acetic AcidReaction Ethyl Acetate

Water

Ethanol

Purification




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3.5.6 3 Methoxy Butanol

Crotonaldehyde and methanol reacts and produces 3 methoxy butyraldehyde then

hydrogenationg of 3 methoxy butyraldehyde forms 3 methoxy butanol.

Chemical Reaction:


Reaction 1 CH3CH=CHCHO + CH3OH CH3CH-O-CH3CH2CHO

Name Methanol

Mol.wt 32

Reaction 2 CH3CH-O-CH3CH2CHO + H2

Name Hydrogen

Mol.Wt 2

3-Methoxy butyraldehyde

102

Crotonaldehyde

70

CH3CH-O-CH3CH2CH2OH

3-Methoxy butyraldehyde 3 MB

102 104

CrotonaldehydeReaction 1 3 Methoxy Butanol

HydrogenMethanol

Purification

Water To ETP

Reaction 2



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3.5.7 Cellulose Acetate

Cellulose acetate is the acetate ester of cellulose. Acetate is derived from cellulose by

deconstructing wood pulp into purified fluffy white cellulose. In order to get a good product,

special qualities of pulps - dissolving pulps - are used. The cellulose is then reacted with acetic

acid and acetic anhydride in the presence of sulfuric acid.

Chemical Reaction:


Reaction 1 C6H7O2(OH)3 + 3C4H6O3 C6H7O2(O2CCH3)3 + 3CH3COOH

Name Cellulose Acetic Anhydride Acetic Acid

Mol.wt 162 102 60

Wt. Balance 162 306 180

Reaction 2 C6H7O2(O2CCH3)3 + 0.6 H2O C6H7O2(OH)2(O2CCH3) +

Name Cellulose Triacetate Water

Mol.wt 288 18

wt. Balance 288 10.8

0.6CH3COOH

262.8 36

Cellulose Triacetate

288

288

Cellulose acetate

262.8 60

Acetic Acid

H2SO4

Catalyst

Mg(CH3COO)2

Catalyst

Reactor 1Cellulose

Acetic anhydride

Reactor 2Hydrolysis

Water

Cellulose Acetate

Acetic AcidAcetic Acid

Neutralisation

Water

Waste Water



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3.5.8 Cellulose Acetate Butyrate

Cellulose acetate butyrate is the acetate ester of cellulose. The cellulose is then reacted with

acetic acid and butyric anhydride in the presence of sulphuric acid. In order to get a good

product, special qualities of pulps - dissolving pulps - are used.

Chemical Reaction:


Reaction 1 C6H7O2(OH)3 + 3 (C6H11O3) C17H26O8 + 2.5 CH3COOH + 0.5 CH3CH2CH2-COOH

Name Cellulose Acetic Butyric anhydride Cellulose Acetate Butyrate Acetic Acid

Mol.wt 162 130 358 60

Wt. Balance 162 390 358 150

Butyric Acid

88

44

H2SO4

Catalyst

Reactor 1Cellulose

Butyric anhydride

Reactor 2Hydrolysis Cellulose Acetate Butyrate

Acetic Acid

Neutralisation

Water

Acetic AcidButyric Acid

Waste Water

To ETP



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3.5.9 Microcrystaline Cellulose

A naturally occurring polymer, it is comprised of glucose units connected by a 1-4 beta

glycosidic bond. These linear cellulose chains are bundled together as microfibril spiralled

together in the walls of plant cell. The crystalline region is isolated to produce Microcrystalline

Cellulose

Chemical Reaction:


Reaction: C6H7O2(OH)3 C6H7O2(OH)3

Name Cellulose Hydrochloric acid Microcrystalline Cellulose

Mol.wt 162 36.5 162

6 HCL

ReactorCellulose

HCl

Microcrystaline Cellulose



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3.5.10 Acetophenone

The liquid phase oxidation of ethyl benzene to acetophenone by oxygen or air was investigated

in semi batch reactor using salt of cobalt and manganese which will be soluble in the reaction

medium

Chemical Reaction:


Reaction C6H5CH2CH3 + O2 C8H8O + H2O

Name Ethyl Benzene Oxygen Acetophenone Water

Mol.wt 106 32 120 18

Ethyl BenzeneReaction Acetophenone

Water

Oxygen

Purification




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3.5.11 Acetonitrile

Acetonitrile produces by reaction of acetic acid and ammonia forms acetamide, and acetamide

converted to acetonitrile by applying heat which forms water simultaneously

Chemical Reaction:


Reaction CH3COOH + NH3 CH3 CN + 2 H2O

Name Acetic Acid Ammonia Acetonitrile Water

Mol.wt 60 17 41 36

Acetic Acid Reaction Acetonitrile

Water

Ammonia

Purification




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3.5.12 Phenyl Ethyl Alcohol

Styrene reacted with hydrogen paraoxide with the presence of hydrocloric acid forms styrene

oxide and water then hydrogenation of styrene oxide with the presence of sodium hydroxide

forms a phenyl ethyl alcohol.

Chemical Reaction:


Reaction 1 C6H5 CH=CH2 + H2O2 C8H8O + H2O

Name Styrene Hydrogen Peroxide Styrene Oxide Water

Mol.wt 104 34 120 18

Reaction 2 C8H8O + H2 C8H10 O

Name Styrene Oxide Hydrogen Phenyl Ethanol

Mol.Wt. 120 2 122

HCl

NaOH

StyreneReaction 1

HClPhenyl Ethyl Alcohol

Water

Hydrogen Paraoxide

Reaction 2NaOH


H2

Purification



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3.6 Raw Materials

Raw materials to be required for proposed project has been estimated based on operation of similar type

of plant as well as proposed plant design data. Detail of raw material consumption for proposed plant is

summarized in table 1.3.

Table 1.3: Raw Material Requirement

S.N

o.

Products Raw Material Quantity in Source of Supply Mode of

Transport Ton/Ton

of Product

MTPM

1.

Sorbic Acid /

Potassium

Sorbate

Acetic Acid 1.09 463.25 GNFC/Dahej port

(Imported)

By Road Tanker

Crotonaldehyde 0.77 327.25 GBL SAK By Road Tanker

TEP Catalyst 0.002 0.909 Searchchem Jagadia HDPE Drum

Na2CO3 0.15 63.75 Domestic By Road

Commercial HCL 0.50 212.5 Domestic By Road

Toluene 0.225 95.625 Domestic By Road Tanker

Potassium

Hydroxide

0.400 170 Domestic By Road

Ammonia gas 0.007 2.975 Domestic Road Tanker/

HDPE Drum

2. 1, 3 Butylene

Glycol

Acetaldehyde 1.29 419 GBL SAK/In-house By Road Tanker

or

Acetaldol 60% 2.200 715 GBL SAK/In-house By Road Tanker

Catalyst 0.0045 1 Domestic By Road

Hydrogen 0.65 211 Domestic By Hydrogen trolly

3. Acetaldehyde Ethyl Alcohol 1.20 690 Domestic/ Dahej port

(Imported)

By Road Tanker

4. Crotonaldehyde Acetaldehyde 1.39 591 GBL SAK/Inhouse By Road Tanker

5. Ethyl Acetate

Ethyl Alcohol 0.71 586 Domestic/Dahej

port(Imported)

By Road Tanker

Acetic Acid 0.820 677 GNFC/Dahej

port(Imported)

By Road Tanker

6. 3 Methoxy

Butanol

Crotonaldehyde 0.94 306 GBL SAK/Inhouse By Road Tanker

Methanol 0.38 124 GNFC/Dahej

port(Imported)

By Road Tanker



29 | P a g e

S.N

o.

Products Raw Material Quantity in Source of Supply Mode of

Transport Ton/Ton

of Product

MTPM


Caustic Soda 0.02 7 Domestic By Road

7. Cellulose

Acetate

Cellulose 0.84 693 Domestic/Imported By Road

Acetic Anhydride 1.59 1312 Domestic By Road Tanker

H2SO4 Catalyst 0.15 124 Domestic By Road Tanker

Sodium Acetate 0.25 206 Domestic By Road

8.

Cellulose

Acetate

Butyrate


Acetic Anhydride 0.11 47 Domestic/Imported By Road Tanker

Butyric Anhydride 2.26 961 Imported By Road Tanker

H2SO4 Catalyst 0.03 13 Domestic By Road

Manganese Acetate 0.009 4 Domestic By Road

9. Microcrystaline

cellulose


Hydrochloric Acid 0.02 5 Domestic By Road Tanker

10. Acetophenone Ethyl Benzene 1.35 1114 Domestic/Imported By Road


11. Acetonitrile

Acetic Acid 1.71 1411 GNFC-Domestic/

Imported

By Road

Ammonia 0.51 421 Domestic By Road Tanker

Benzene 0.02 17 Domestic By Road

12. Phenyl Ethyl

Alcohol

Styrene 1.16 493 GBL SAK/Inhouse By Road Tanker

Hydrogen

Peroxide(50%)

0.91 387 Domestic By Road Tanker


Caustic Soda(50%) 0.81 344 Domestic By Road

HCl(32%) 1.220 519 Domestic By Road



30 | P a g e

3.7 Resource Requirement

Various resources like land, utility, power, fuel, water, manpower etc. will be utilized for carry out

production activities. Simply production is converting resources into finished product.

3.7.1 Land

GCL has procured 319655.00 m2 land from PCPIR to develop the complete industrial infrastructure for

propose speciality chemical project. Proposed project will be set on R.S. No: 142, 151, 152, 153/1, 154,

155, 156, 157, 158, 159, 160. Out of 319655.00 m2 area approx. 168194 m

2 will be utilized for proposed

project and remaining 151461 m2 area will be kept open for future use. Construction of admin building,

plant building, Raw material storage area, finished products storage area, utility area, treatment facility,

parking, fire hydrant and other ancillary amenities shall be undertaken within the plot area. Proposed

project will be developed in accordance with local development plan and used for industrial purpose.

Land possession and NA is already available with project proponent. Bifurcation of plot area is mentioned

in table 1.4.

Table 1.4: Land Bifurcation

S. No. Description Area in m2

1. Production plant 16040

2. Raw material storage 2500

3. Chemical storage 1000

4. Common utility area 7988

5. Common Central facility area 6702

6. Greenbelt area 55850.51

7. Open space for future use 151461

8. Internal Road 11000

9. Loading/unloading area 33687

10. Parking area 32986.49

11. Rain water harvesting 440

TOTAL 319655



31 | P a g e

3.7.2 Water

Proposed project is located in PCPIR notified industrial estate, having all basic amenities for water,

power, transport etc. Water requirement for proposed project will be fulfilled by GIDC. Project proponent

has already made to application to GIDC to obtained permission for withdrawal of proposed water.

Bifurcation of daily water consumption during construction and operation phase is described below in

table 1.5.

Construction Phase:

Domestic – 7 KLD

Construction activities, curing and Dust suppression – 13 KLD

Operation Phase:

Domestic – 35 KLD

Industrial – 1422 KLD

Gardening – 10 KLD

Table 1.5: Water Consumption

S.No. Activities

Water

consumption

in KLD Remarks

1. Domestic 35 Fresh water

2. Industrial Use

Process 776 Fresh water and water generated in process

Washing 199 Fresh water

Boiler 433 Fresh water and condensate recovery water

Cooling 14 Fresh water, MEE condensate and RO permeate water

3. Other

Gardening 38 Fresh water (10 KLD) and treated STP water (28 KLD)

Total (1+2+3) 1467



32 | P a g e

3.7.3 Electricity

Construction Phase:

Diesel operated construction equipments and machineries will be used during construction phase. Two

nos. of D. G. set of capacity 250 KVA each will be kept as a stand-by arrangement used during power

interruption.

Operation Phase:

Source: Proposal to set steam back pressure turbine of capacity 3x3 MWH.

Electricity: 11/33KVA, 50 Hz

Backup Power: Proposal to set steam back pressure turbine of capacity 3x3 MWH.

Two nos. of D. G. set of capacity 250 KVA each

3.7.4 Fuel

Imported Coal – 130 TPD for Boiler (Indonesia)

Furnace Oil – 300 LPD for Heater (from local supplier)

HSD – 20 Ltr./hr. (from local supplier as and when required)

3.7.5 Manpower

Construction Phase: Local construction workers will be employed from surrounding area during this

phase. It is estimated that 150 Nos. of Local workers (skilled and semiskilled) will get direct employment

during construction phase.

Operation Phase: An industrial plant normally runs in three shifts and at full rated plant capacity.

Technical and non-technical personnel will be required for manufacturing unit, utility unit, O&M of plant,

security, admin etc. it is estimated that 755 Nos. of man power including contractor workers will be

required during operation phase.



33 | P a g e

Plant wise bifurcation of skilled, unskilled and technical person to be required is described as under,

S. No. Description Employee Total

Skilled/

Technical

Unskilled

1. Sorbic Acid/Potassium Sorbate 25 40 65

2. 1,3 Butylene Glycol 20 40 60

3. Acetaldehyde 15 10 25

4. Crotonaldehyde 15 20 35

5. Ethyl Acetate 25 40 65

6. 3 Methoxy Butanol 25 40 65

7. Cellulose Acetate 30 85 115

8. Cellulose Acetate Butyrate 20 35 55

9. Microcrystalline Cellulose 20 50 70

10. Acetophenone 25 50 75

11. Acetonitrile 25 40 65

12. Phenyl Ethyl Alcohol 20 40 60

TOTAL 265 490 755

3.7.6 Utility

The requirement of utilities for the proposed project has been estimated based on plant operation

capacity.

Coal fired Steam Boiler – 30 TPH x 2 nos.

Cooling Tower – 300 m3/Hr. x 5 nos.

Air Compressor – 450 cfm

Thermic Fluid Heater – 5 Lakh Kcal/Hr.

Incinerator – 5 KL

Steam Back Pressure Turbine – 3x3 MWH

RO Plant – 1356 KL (4 nos.)

MEE (1) – 414.5 kl (4 nos.)

MEE (2) – 388 kl (4 nos.)



34 | P a g e

3.8 Waste to be generated

It is envisage that due to proposed project activity various wastes to be generated which are described as

under:

3.8.1 Sewage

Construction Phase: Sewage will be expected to generate due to domestic activities of workmen and

staff personnel during construction phase as well as operation phase. On site sanitation facilities will be

provided to construction workers. Separate arrangement of sanitation facility for female workers. It is

estimated that approx. 6 KLD sewage generated during construction phase, which will sent to soak pit

through septic tank.

Operation Phase: Sewage quantity of 28 KLD will be generated and it shall be treated in adequately

designed sewage treatment plant of capacity 35 KLD. Treated sewage from the STP will be reused for

greenbelt development, while sludge from STP will be used as manure in greenbelt area within plant

premises.

3.8.2 Effluent

Effluent generated from the manufacturing process and other ancillary operation will be treated in

adequate newly constructed effluent treatment plant of capacity 1250 KLD followed by incinerator, R.O.

plant and two nos. of MEE. It is estimated that 1356 KLD effluent will be generated and treated in ETP

and MEE.

Description of Effluent treatment facility is as under,

Low COD/Low TDS waste stream will be generated from utilities, process, washing, contaminated

steam condensate etc. COD is less than 10000.

High COD/TDS waste stream will be effluent from process containing miscible solvents & other

organics having COD in between 10000 to 100000.

Low COD/Low TDS streams will be treated in ETP having primary, secondary and tertiary treatment

facility. Treated effluent will further pass through RO plant. RO permeate will be recycled back to

cooling tower while RO reject will be treated in MEE(1).

High COD/High TDS stream will be passing through stripper. After removal of harmful traces from

the said stream it will be treated in MEE(1) along with RO reject. MEE(1) is followed by ATFD for



35 | P a g e

further treatment of waste stream. Condensate from ATFD will send back to low COD stream. Waste

traces from stripper will be burnt in an incinerator.

Mother liquor from various process will be filtered and then treated in MEE(2) followed by spin flash

dryer. Condensate from MEE(2) will be recycled back to cooling tower.

Overall condensate from MEE (1) and MEE (2) as well as RO permeate will be totally recycled back to

cooling tower. There shall not treated effluent discharge from plant premises. Hence proposed project is

ZERO LIQUID DISCHARGE industry. Details of wastewater generated from proposed project are

mentioned in table 1.6.

Table 1.6: Wastewater Generation

S. No. Activities Wastewater Generation (KLD)

1. Domestic 28

2. Industrial Use

Process 379

Washing 199

Utilities (Boiler and CT

blow down)

369

MEE 409

Total (2) 1356



36 | P a g e

3.8.3 Air Emission

Air emission (flue gases stack and process emission), nature of emitted pollutants and system provided

for air pollution control in proposed plant is mentioned in table 1.7

Table 1.7(a): Flue Gas Emission

S. No. Description Proposed Flue Gas Emission

1. Stack Attached to FBC Boiler Thermic Fluid Heater

2. Stack Height (m) 35 15

3. Stack Dia (mm) 1000 500

4. Fuel & its consumption Imported Indonesian

Coal – 130 TPD

Furnace Oil – 300 LPD

5. Nature of Pollutants PM, SO2, NOx PM, SO2, NOx

6. Emissions control

system

Cyclone Separator

Bag filter

Alkali Scrubber

Not required as FO is used as fuel.

7. Permissible Limit PM : 150 mg/Nm3

SO2 < 100 ppm

NOx <50 ppm

PM : 150 mg/Nm3

SO2 < 100 ppm

NOx <50 ppm

Table 1.7(b): Process Emission

S. No. Description Proposed Process Emission

1. Vent attached to Scrubber

2. Vent length (m) 3

3. Vent Dia (mm) 300

4. Nature of Pollutants HCl, NH3, VOC

6. Permissible Limit HCl : < 20 mg/Nm3

NH3 : 175 mg/Nm3



37 | P a g e

3.8.4 Solid/Hazardous Waste

All the solid/hazardous wastes to be generated at the end of manufacturing process or waste treatment

process will be stored on impervious floor having roof, boundary wall and leachate collection as well as

transfer facility. Management of wastes shall be done as per HW (Management, Handling and Trans

boundary Movement) Third Amendment Rules, 2010 of Environment Protection Act, 1986.

Solid/hazardous waste generated from various plants of GCL is mentioned in table 1.8.

Table 1.8: Solid/hazardous Waste Generation & Management

S.

No.

Solid/Hazardous Waste

Name Category Source Quantity Storage Area Disposal/Management

Hazardous Waste

1. Used Oil 5.1 From

machine/

D.G. set

0.3

KLPM

Stored at waste

storage area in

drums

Collection, Storage &

Selling to authorized

recycler

2. Discarded

Containers

33.1 Raw

material

storage and

from utility

750 nos.

per month

Stored at waste

storage area on

pellet

Collection, Storage &

Selling to GPCB

approved scrap dealer.

3. Incineration

Ash

37.2 Incinerator 0.4

MTPM

Stored at waste

storage area on

pellet

Collection, Storage,

Transportation &

Disposed at TSDF site

4. Process

waste MEE

Salt

26.1 MEE 250

MTPM

Stored at waste

storage area on

pellet


Transportation &

Disposal at TSDF site

5. Spent

Catalyst

26.5 Process

plant

0.05

MTPM

Stored at waste

storage area in

drums


Transportation &

Disposal at TSDF site

Solid Waste

1. STP sludge -- STP 7 MTPM Stored at waste

storage area in bag

Used as manure within

plant premises.

2. Fly Ash

-- Boiler 3.2

MTPM

Stored at waste

storage area on

pellet


Transportation & send

to brick manufacturer.



38 | P a g e

3.8.5 Noise

Construction Phase: Noise will be generated during construction phase due to vehicular movement,

operation of construction equipment. Well maintain vehicles and construction equipment shall be engaged

to minimize the noise pollution.

Operation phase: Noise will be generated due to various industrial activities, use of utility, plant

machineries, vehicular movement etc. Proper mitigation measures will be implemented to control the

noise to keep it within the prescribed norms. The industry has proposed 55850.51 m2

area for green belt

around the periphery of the plant boundary and open space of plot. Greenbelt will help in reducing the

adverse effect of noise pollution in general.

3.9 Purpose of EIA Study

As per the provision made in EIA Notification Dated 14th September 2006 and its amendment till date, it

has been noticed that the proposed project to be developed for manufacturing speciality chemical thus

project activity falls under schedule I: 5(f) – Synthetic Organic Chemicals industry. Project is located in

PCPIR notified industrial area; hence project category is ―B‖. It is necessary to get Environmental

Clearance (EC) prior to commissioning of the proposed project by applying to SEAC, Gandhinagar, along

with the Environment Impact Assessment Study Report. Therefore the EIA study is required to be

conducted for obtaining the EC.

Public hearing is to be conducted for the project in accordance with provisions of Environmental Impact

Assessment Notification, 2006. The proposed unit falls under PCPIR Dahej region and the Public hearing

for PCPIR Dahej region was conducted on 30 July 2014 considering cumulative EIA and proceeding of

the same has been submitted to Chairman GPCB and SEIAA, followed by Final EIA submitted to 7th

Sept. 2015. The technical presentation for Environmental Clearance was held on 13th June 2016. The

current status of the PCPIR region is the Environmental clearance is not granted yet.

As per EIA notification, if public hearing conducted for the region considering cumulative EIA, the

public hearing will not be required further for individual project in the same region. Hence, for the

proposed unit PUBLIC HEARING is NOT REQUIRED.



39 | P a g e

4.0 SITE ANALYSIS

Propose project site were selected for evaluation based upon their general suitability for industrial

development. Site analysis was done to ensure that development is undertaken in such a way that reduces

negative impacts to the onsite environment and surrounding ecosystems. Propose project site is supported

by various basic infrastructure facilities i.e. water supply, transportation, electricity supply, fuel supply

etc.

4.1 Connectivity

Proposed project site is connected with road, rail and air transport. Raw materials, finished products &

personnel during the construction and operation phase shall be done by means of existing transportation

facility.

Railway station : Dahej (20 km) & Bharuch(25 km)

Highway : NH – 8 (30 kms)

Airport : Baroda (80 km)

4.2 Land form & Land Use

Proposed project site is located in PCPIR notified industrial area and surrounded by many

industries. Existing land use pattern of proposed project site is non-agricultural. Land use pattern

is non-agricultural and mainly used for the industrial activities. The environmental setting

contains an idea on the environmental conditions/locations within the vicinity of the proposed

project.

Environmental settings available surrounding of the proposed project site is mentioned in table

1.9



40 | P a g e

Table 1.9: Environmental Settings

S. No. Env. Setting Description

1. Forest & Marine

Sanctuary

There is no forest & Marine Sanctuary within 10 kms. radius of

proposed project site.

2. Stream / Rivers Narmada River (approx. 4 km)

3. Sea Arabian Sea (approx. 18 km)

4. Water body/Pond/Lack None

5. Hill / Mountain There is no Hill /Mountain within 10 kms. radius of proposed project

site.

6. Villages Atali (0.5 km) village

7. Historical, religious and

other important cultural

places.

None

4.3 Topography

Proposed project site is located at 21°42’52.93‖ N and 72°42’16.09‖E. It has an average elevation of 16

meters above sea level. Proposed project site is located in PCPIR notified industrial area, where land is

already developed for industrial purpose.The overall project site is located on plain barren land devoid of

any permanent and economically useful vegetation. The topography of the proposed site for project is

plain terrain. Forest, national park, eco sensitive area, wild life sanctuary, Historical, religious and

other important cultural place etc. is not located within 10 Km periphery of the proposed project

site. There is no change in land use/topography as the proposed project shall be established in

well-developed industrial Area of PCPIR.

4.4 Existing Infrastructure (Social/Commercial)

Key infrastructure such as hospitals, schools, bank, places of worship and social/ community

facilities such as park, market, playground etc. education, health care, community development,

income distribution, employment and social welfare are available in nearby area of proposed

project site.



41 | P a g e

4.5 Soil Classification

Proposed project site is located in PCPIR notified industrial area, where land is already

developed for industrial purpose. Quality of soil is not considerably fertile for agriculture

activities and no evidence of any influence of soil contaminant has been noticed.

4.6 Climatic data from secondary sources

Proposed project site is fall under seismic zone – III which is not highly earthquake prone area.

Semi-Arid type of climate is observed with temperature ranges 33.1°C (max.) to 21.9°C (mini.).

Wind is observed from west at 14 kmph speed. There is a chance of humidity in the weather due

to Arabian Sea. Humidity is ranges from 36 – 40%. Normally during June to September month,

rain is expected.

5.0 PLANNING BRIEF

GCL proposed to set up a new multi products plant for manufacturing different range of chemicals at Plot

No: 142, 151, 152, 153/1, 154, 155, 156, 157, 158, 159, 160, PCPIR notified industrial area, Village –

Atali, Tal-Vagra, Dist – Bharuch, Gujarat. The proposed project will be started after getting

Environmental Clearance from SEAC, consent to established from GPCB and other statutory clearances

required for. Proposed project activities will take care of all the rules and regulation of statutory authority

and provide the control measure and devices to achieve the standard norms. Proposed project for

manufacturing of Speciality Chemicals will be developed in following stages/ phases at Dahej, Gujarat.

For all above product project proponent obtained Industrial Entrepreneurs’ Memorandum (IEM)

acknowledgement from Ministry of Commerce & Industry Govt.

5.1 Population Projection

150 Nos. of skilled and semi-skilled construction workers will get direct employment during

construction phase while 800 nos. of technical personal and other contract workmen will get

direct or indirect employment after commissioning of proposed project.



42 | P a g e

5.2 Land use Planning

GCL has already occupied total 319655 m2 land for development of proposed project. All the industrial

infrastructures like STP, ETP, storm water drainage systems, sewerage network, internal RCC road, rain

water harvesting system, area lighting and electrification, water supply system, waste management system

etc. will be developed in said plot area. It is proposed to develop 55850.51 m2. Greenbelt area as per

CPCB guideline and it is 33% of area utilized for proposed project development.

5.3 Amenities / Facilities

All amenities/facilities will be required to develop green filed project is available in proposed site as well

as nearby town i.e. at Bharuch.

6.0 PROPOSED INFRASTRUCTURE

Proposed industrial plant to be supported by various basic infrastructure facilities i.e. water supply,

transportation, electricity supply, fuel supply etc. are mentioned in table 1.10

Table 1.10: Proposed Infrastructure

S.

No. Proposed Infrastructure Description

1. Industrial area 319655.00 m2

2. Green belt 55850.55 m2

3. Social Infrastructure Available within 10 km radius of project site.

4. Connectivity Project site is well connect with road, rail and air transport.

5. Drinking water management PCPIR water supply network.

6. Sewerage system Sewage treatment plant shall be installed and treated sewage shall

be reused in flushing and gardening.

7. Industrial waste management ETP followed by RO plant, Incinerator and MEE shall be

provided to achieve Zero liquid discharge.

Adequate air pollution control equipment shall install to

achieve the GPCB norms.

8. Solid waste management Collection, storage, transportation and handling of solid/hazardous



43 | P a g e

S.

No. Proposed Infrastructure Description

wastes generated from proposed project shall be done as per HW

(Management, Handling and Trans boundary Movement) Third

Amendment Rules, 2010 of Environment Protection Act, 1986.

9. Power Requirement, supply

& source

Source: Proposal to set steam back pressure turbine of

capacity 3x3 MWH.

Electricity: 33 KVA, 50 Hz

7.0 REHABILITATION & RESETTLEMENT (R&R) PLAN:

Proposed project activities will be carried out in PCPIR industrial area, which is developed for industrial

purpose and there is no population or local inhabitant at the proposed project site. Thus Rehabilitation &

Resettlement (R&R) Plan is not applicable to propose project.

8.0 PROJECT SCHEDULE & COST ESTIMATION:

8.1 Project Schedule

The proposed project will be started after getting Environmental Clearance from SEAC, consent to

established from GPCB and other statutory clearances required for.

8.2 Cost Estimation

Capital towards proposed industrial plant development including land purchase, building

construction, plant machinery – purchase and commissioning, environmental management,

greenbelt development etc. The overall project cost has been estimated Rs. 250 Crores, and is

summarized in table 1.11.



44 | P a g e

Table 1.11: Project Cost

S.No. Particulars Cost in Rs.

(Crores)

1. Land 5

2. Building and civil work 10

3. Plant and Machinery purchase 20

4. Utility /plant machineries 10

5. Environmental Management System

Incinerator 1

MEE 1

ETP & STP 5

Solid hazardous waste management including Membership for TSDF 1

OHS

Greenbelt development 2

6. Other (Water from GIDC Reservoir) 15

Total Project Cost 250

9.0 ANALYSIS OF PROPOSAL:

9.1 Financial & Social Benefits

Approximately 150 Nos. will be employed directly during construction phase.

All local people shall be employed as per their skills, qualifications and company’s

requirement during operation phase.

Proposed project will contribute to state and national economic growth to a measurable

extent.

GBL will adopt water conservation techniques and pollution abatement measures to protect

existing environment and ecology.

prefeasibility report for godavari bio-refineries...

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