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PROJECT PRE-FEASIBILITY REPORT

ON

PROPOSED INCREASED CAPACITY PLAN

(Without increase in pollution load)

FOR

MANUFACTURING OF PHARMACEUTICALS

INTERMEDIATES AND ACTIVE PHARMACEUTICAL

INGREDIENTS

OF

M/s. ZCL CHEMICALS LTD.

AT

PLOT NO. 3102/B,

GIDC INDUSTRIAL ESTATE,

ANKLESHWAR-393002 , GUJARAT

Prepared by:

Jyoti Om Chemical Research Centre Pvt. Ltd. Shed No. K- 1, 7705/2-4, GIDC Estate,

Ankleshwar- 393002, Dist: Bharuch, Gujarat.

Phone: (02646)220293, Fax: (02646) 239454

E mail: [email protected]

CONTENTS

S. No. Particulars Page No.

1 SUMMARY 1

2 INTRODUCTION 5

2.1 The Project 5

2.2 Project Proponent 5

2.3 Nature of project 8

2.4 Market Feasibility 11

2.5 Employment generation due to the project 12

3 PROJECT DESCRIPTION 12

3.1 Type of Project 12

3.2 Project Location 12

3.3 Site selection 15

3.4 Neighbouring Industries 15

3.5 Size of project 15

3.6 Process Technology 16

3.7 Raw materials 16

3.8 Resource optimization/recycling reuse 16

3.8.1 Solvent recovery 16

3.9 Resource requirement 17

3.9.1 Land 17

3.9.2 Building 17

3.9.3 Power & Fuel 17


3.9.4 Water 17

3.9.5 Man power 18

3.10 Mitigation measures & EMP 18

3.10.1 Waste water Management 19

3.10.1.1 Waste water generation 19

3.10.1.2 Waste water characteristics 19

3.10.1.3 Waste water treatment and disposal 20

3.10.2 Gaseous emission & Control 28

3.10.2.1 Flue gas emission 28

3.10.2.2 Process emission 28

3.10.3 Hazardous /non hazardous waste management 29

3.10.4 Noise control & odour 30

3.10.5 Storage ,handling and transport of Hazardous chemical 31

3.10.6 Health & Safety measures 31

4 SITE ANALYSIS 35

4.1 Connectivity 35

4.2 Land use and land ownership 37

4.3 Land use 37

4.4 Existing infrastructure 37

4.5 Soil Classification 38

4.6 Climate data 38

4.7 Social Infrastructure 39

5 PlANNING BRIEF 40

5.1 Planning concept 40

5.2 Population projection 40

5.3 Land use planning 40

5.4 Assessment of infrastructure Demand 40


5.5 Ammentities/Facilities 41

6 PROPOSED INFRASTRUCTURE 41

6.1 Processing area 41

6.2 Non processing area 42

6.3 Green belt area 42

6.4 Social Infrastructure 42

6.5 Connectivity 42

6.6 Drinking water management 43

6.7 Sewage system 43

6.8 Industrial waste management 43

6.9 Solid waste management 43

6.10 Power requirement & Supply 43

7 REHABILITATION & RESETTLEMENT (R & R)

PLAN

43

8 PROJECT SCHEDULE & COST ESTIMATES 44

8.1 Project Implementation Schedule 44

8.2 Estimated project cost 44

9 ANALYSIS OF PROPOSAL 44

LIST OF TABLES

Table

No.

Topic Page No.

1 List of Products 1

2 Contact details of the Directors 7

3 Details of Manpower 12

4 Salient features of the project site 13

5 Nearby Industries in the vicinity 15

6 Capital cost of Existing 16

7 Power and Fuel Requirement 17

8 Details of Water Consumption 18

9 Details of Wastewater Generation 19

10 Characteristics of Wastewater 19

11 Dimensional details of ETP units 25

12 Details of Flue gas emission 28

13 Details of Process emission 28

14 Details of Hazardous waste 29

15 Details of Micro Meteorological data 38

16 Project Implementation schedule 44

LIST OF FIGURES

Figure

No.

Description Page No.

1. Location of the Project site 13

2. Aerial View of the 5 Km Radial Periphery from the Project Site 14

3. Flow Diagram of ETP 26

4. Flow Diagram of MEE 27

5. Wind rose 39

M/s. ZCL CHEMICALS LTD., ANKLESHWAR

M/s. JYOTI OM CHEMICAL RESEARCH CENTRE PVT. LTD. Page 1

1.0 EXECUTIVE SUMMARY

M/s. ZCL Chemicals Ltd. is engaged in manufacturing of Pharmaceuticals Intermediates and

Active Pharmaceutical Ingredients at Plot No. 3102/B, GIDC Industrial Estate, Ankleshwar -

393002, Gujarat.

As per EIA notification 2006 and its amendment, the proposed project is falling under category

5(f). The unit is having CCA for manufacturing of Pharma Intermediates and Active

Pharmaceutical Ingredients. They have now proposed to go for increase in production capacity.

The details of products are given below table.

TABLE: 1

LIST OF PRODUCTS

Sr.

No.

Name of Products Existing as per

CCA No.

AWH-72765

(MT/Year)

Proposed

quantity

(MT/Year)

Total after

proposed

Expansion

(MT/Year)

GROUP-1

1 ThrioPypridil AmideAND/OR 204.03 -79.03 125

2 Ritalinic acidAND/OR

3 4 - benzyloxy -3- nitrophenylace

bromideAND/OR

4 Zonisamide– USPAND/OR

5 Modafinil - EP/USPAND/OR

6 4-Amino-N-[(2 R, 3S)- 3 Amino, 2

hydroxy, 4- phenyl butyl ] – n – (2 Methyl

propyl) benzene sulfonamideAND/OR

7 Darunavir AND/OR

8 Fluvoxamine Maleate- EP/BP/USP/JP

AND/OR

9 Trifluoperazine - USP/EP/BP AND/OR

10 Methylphenidate - USP/EP AND/OR

11 R & D Products AND/OR

12 Dex Methyl Phenidate AND/OR

13 Chlordiazepoxide AND/OR

14 Cillastazol AND/OR



15 7 Hydroxy 1,2,3,4 tetra hydro quenoline

AND/OR

16 Chloro Methyl cyclo propane AND/OR

17 1-(2,3 dichloro phenyl) - piperazine

hydrochloride (DCPP) AND/OR

18 BBQ (7-(4-Bromobutoxy)-3, 4-

dihydroquinolin-2(1H)-one) AND/OR

19 T2551 - Etravirin Inter AND/OR

20 Canagliflozicin Inter (n-2): 2-(4-

fluorophenyl)-5-(5-iodo-2-

methylbenzyl)thiophene AND/OR

21 Aripiprazole AND/OR

22 BET (1-(2-Bromoethyl)-4-ethyl-1,4-

dihydro-5H-tetrazol-5-one) AND/OR

23 1-Amino Indane AND/OR

GROUP – 1 (Total) 204.03 -79.03 125

GROUP – 2

24 Trimethyl pyruvic AcidAND/OR 42.03 +32.97 75

25 4,4’-Diflurobenzhydryl Piperazine

AND/OR

26 2 Tri Phenotrimethyl phenothiazine

AND/OR

27 Levomepromazine AND/OR

28 Betahistine IP / EP / USP AND/OR

29 BetahistineMesylate JP/EP AND/OR

GROUP – 2 (Total) 42.03 32.97 75

GROUP – 3

30 Phenyl 2 PiperidylAcetamide AND/OR 23.1 0 23.1

31 N- (1 Benzyl 4 Piperidinyl) N Phenyl

Propanamide HCL / NN Phenyl N 4

PiperidinylPropanamide HCl AND/OR

32 N Acetyl Hydroxy Phenyl Piperazine

AND/OR

33 Amino Ethyl Phosphoric Acid AND/OR

34 (1-Isopropyl-4-(hydroxyl Phenyl)

(piperazine) AND/OR

35 Memantine HCl AND/OR

36 Quetiapine Fumerate AND/OR

GROUP – 3 (Total) 23.1 0 23.1



GROUP – 4

37 Phenyl 2Pyridyl Acetamide AND/OR 23.266 0 23.266

38 Zaltoprofen AND/OR

39 Alprazolam AND/OR

40 Mono chloro acetonitrile AND/OR

GROUP – 4 (Total) 23.266 0 23.266

INDIVIDUAL PRODUCTS

41 BOC Nitro 0 +150 150

42 (N-[4-Methoxymethyl)-1-(phenyl methyl)-

4-Piperdinyl]-N-Phenyl Propanamaide-

Ethanedioate.

0.06 0 0.06

43 DexRitalinic Acid 0.1 0 0.1

44 Remi N Benzyl Propeonamide eater

Oxalate

0.02 0 0.02

45 Nebivolol 0.1 0 0.1

46 Flurbiprofen 0.4 0 0.4

47 Olanzapine 0.4 0 0.4

48 Levodropropizine 0.5 -0.4 0.1

49 Atomoxetine 0.5 0 0.5

50 Felbiprofen 3 0 3

51 Clozapine 1.8 0 1.8

52 Diazepam 0.4 0 0.4

53 Oxazepam 0.4 0 0.4

54 Flupirtine maleate 0.4 0 0.4

55 Bromazepam 0.4 -0.3 0.1

56 BenzhydrlPiprazine 4 0 4

Individual (Total) 12.48 +149.3 161.774

Total 304.906 +103.240 408.146

COST OF PROJECT

It is not applicable. The plot has been purchased by M/s. ZCL Chemicals Ltd. from GIDC. The

total plot area of the unit is 35595 Sq.meter. The green belt area is 6215.04 sq.m.

FUEL CONSUMPTION

The existing unit uses Natural gas as fuel for Boiler& Thermic fluid heater and diesel used for

DG Set. There will be no changes in proposed expansion for Natural gas Consumption for

Boiler& Thermic fluid heater,Diesel consumption for DG set.



ELECTRICITY CONSUMPTION

The unit have electricity from Daxin Gujarat Vij Company Ltd. The existing electricity

consumption is 1950 KVA. There will be no changes in Electricity consumption due to Proposed

Increase in production.

WATER CONSUMPTION

The source of water will be from GIDC water supply scheme.

The water consumption for industrial purpose is 143.8 KL/day. The water consumption for the

domestic& gardening purpose is 21.2 KL/day fresh water.

WASTE WATER GENERATION

The industrial waste water generation will be 45 KL/day and domestic waste water will be 10

KL/day. 55 KL/day of effluent will be treated in ETP .Treated effluent will be discharged in to

GIDC Pumping station – B through above ground fixed pipeline leading to the inlet of FETP for

further treatment and its ultimate disposal to deep sea NCTL.

GASEOUS EMISSION

There will be one stack of one boiler (capacity: 3.5 Ton/Hr), one stack of Thermic fluid heater

(capacity: 4 lac Kcal) and two stack of two Diesel generators (capacity: 250 & 750 KVA

respectively). The two D.G. sets will be used in case of emergency only. There will be no change

in Flue gas emission due to Proposed Expansion.

Process emission will be from two numbers of stacks. There will be one stack attached to

Reaction vessel in Plant-1, one stack attached to Reaction vessel in Plant-2.These stacks are

connected with scrubbers (Water +Caustic).

There will be process emission from two vents of the Water scrubber & Caustic scrubber. There

will be no additional new process stacks due to proposed expansion.

HAZARDOUS WASTE MANAGEMENT

There will be generation of ETP sludge (339 MT/Year), Carbon Waste (18.25 MT/Year),

Distillation residue (36.5 MT/Year), Discarded containers (43800 Nos/Year), Distillation residue

from contaminated organic solvents(0.73 MT/Year), Used/Waste Oil(1.83 MT/Year),



Contaminated solvents not fit for originally intended use(73 MT/Year), Spent solvent(73 MT /

Year), High COD waste from MEE stripper(540 MT/Year).

ETP sludge will be disposal at TSDF M/s. BEIL. Carbon Waste, Distillation residueand

Distillation residue from contaminated organic solvents will be send toincineration at TSDF M/s.

BEIL/RSPL & Ambuja Cements for Co -processing. Discarded containers will be sold to

authorized vendors.Used / Waste Oil will be sold to registered refiners.Contaminated solvents

not fit for originally intended use, spent solvent will be reuse within premise at site and High

COD waste from MEE stripper will be Disposal at TSDF/Incinerator.

There will be no change in Hazardous waste generation due to Proposed Expansion.

2.0 INTRODUCTION

2.1 THE PROJECT

M/s.ZCL Chemicals Limited has acquired plot no. 3102/B, GIDC Estate, Ankleshwar for

manufacturing of Pharmaceuticals Intermediates and Active Pharmaceutical Ingredients.The list of

products is provided in Table -1.

2.2 PROJECT PROPONENT

M/s.ZCL Chemicals Limited was incorporated in the year 1991. They have manufacturing unit

in Ankleshwar. They are increasing their production capacity quantity in Ankleshwar unit. The

Company delivers a broad range of advance fine Pharmaceuticals intermediates and Active

Pharmaceuticals Ingredients for pharmaceutical end use and services to customers around the

world. ZCL has been concentrating on Research and Development and has scaled up its

investments to step-up its capabilities in Generic research. The project proponents are already in

market and doing manufacturing and trading of these products.



Quality, Environment, Health and Safety Policy:

The policy of the company is as under:

Reflecting its Commitment to Global leadeaship and Excellence in Quality, Environment, Health

and Safety , ZCL Chemicals Ltd. Ankleshwar, Manufacturing Advance Intermediates, Active

Pharmaceutical Ingradient and Safety Chemical in having Guidline principles that Comminted

toward Compatancy in Quality, Lead Time , Overall Economic Feasibility through Environment

Health and Safety must satisfy our Esteem Customers.

It is Policy of ZCL Chemicals Ltd. , Ankleshwar, That

All Incident are Preventable, All identified Health Risk are Containable and identified

Environment impacts are Prevented.

Prevent Injuries and Occupational Illness at the Workplace.

Enhance quality, environment, health and safety awareness.

Comply with all Statutary and Regulatory Laws and Regulation for Quality, Environment,

Health and Safety

Continual improvement towards Quality, Technology, after Sale Service Aspect and Upgration

of Environment, Health and Safety Management system to Prevent/Minimize Pollution,

Occupation Health and Safety risks.

Enhance Visibility of Top Management towards Conservation Resource Quality, Environment,

Health And Safety.

Our Quality, Environment, Health and Safety Consciousness shall be Recognised through

acheiving excellence implementation level of ISO 9001 : 2008, ISO 14001: 2004 and Oshas

18001 : 2007 Norms.



The name and address of Directors are given in Table 2.

TABLE: 2

CONTACT DETAILS OF THE DIRECTORS

List of Directors as on 31.07.2015

Sr.

No. Name & Address of Directors

Date of

Appointment

Date of

Ceasing

Date of

Birth PAN No.

Contact

No.

1 Mr. Ajay Krishnakant Parikh 13.03.1991 Nil 24.06.1957 AACPP4774A

022--

61539900

20/301, Gurukrupa, Vithal Nagar,

CHS Ltd., 11th

Road, JVPD

Scheme,

Vile Parle (W), Mumbai – 400

049

2 Mr. Nihar Ajay Parikh 01.09.2010 Nil 13.11.1985 AKNPP4298E

022--

61539906

20/301, Gurukrupa, Vithal Nagar,

CHS Ltd., 11th Road, JVPD

Scheme,

Vile Parle (W), Mumbai – 400

049

3 Mr. Dhiren Shevantilal Shah 05.09.2011 Nil 29.04.1956 AAEPS0922M

022--

61539999

Cumbala Hill post Office

GamdeviP.Stn

Mumbai - 400026

4 Mr. PiyushMaganlal Nathwani 30.01.2015 Nil 24.04.1961 AAZPN7154P

02646-

619405

F 14,Shashwat Complex

Dahej By Pass Road

Bharuch-392001,Gujarat

5 Ms. Anuja Ajay Parikh 31.07.2015 Nil 26.07.1989 ASAPP0424F

022-

61539999

20/301,Guru Krupa,Vital Nagar

Society,

11th Road,JVPDScheme,Vile

Parle(west)

Mumbai-400049,Maharastra



2.3 NATURE OF PROJECT

The summary of the changes is as follows --

Group in CCA Existing capacity in

MTA

Proposed capacity in

MTA

Difference

in MTA

Group-1 204.03 125 -79.03

Group-2 42.03 75 +32.97

Group-3 23.1 23.1 0

Group-4 23.266 23.266 0

Individual Products

BOC Nitro (in Group 1 in existing

CCA) 150 +150

Levodropropizine 0.5 0.1 -0.4

Bromazepam 0.4 0.1 -0.3

Other products as

per CCA 11.47 11.47 0

Total 304.9 408.14 +103.24

Overall production capacity will be increased from 304.9 MT/year to 408.14 MT/year.

The reduction in BOC Nitro effluent generation is done by process improvement through R& D.

The details are as under.

NAME OF PRODUCT: - BOC NITRO

Chemical Name: - ([1S, 2R)-(1-benzyl-2-hydroxy-3-(isobutyl-(4- nitrobenzenesulfonyl) amino)

propyl))carbami acid tert-butylester

Reaction scheme:-

NH

OH

N

CH3

CH3

S

N

O

O

O

OO

OCH3

CH3

CH3

NH

OH

NH

CH3

CH3

O

OCH3

CH3

CH3

S

NO O

OO

Cl

+Base

4-nitrobenzenesulfonyl chloride

BOC NITRO -(BOC)Tert-butyl [(1S, 2R)-1-benzyl-

2-hydroxy-3-(isobutyl amino) propyl] carbamate



Improvement in the process of BOC Nitro:-

R&D has taken Design of experiments (DOE) approach for process improvement. DOE means

systematic method to determine the relationship between factors affecting a process and the

output of that process. In other words, it is used to find cause-and-effect relationships. This

information is needed to manage process inputs in order to optimize the output. It is statistical

tool. BOC Nitro process modified and develops environmentally friendly process.

Based on the DOE we have identified best suitable reaction condition with optimized ratio of

inputs without affecting quality of material as well as yield of BOC Nitro. BOC Nitro reaction is

basically nucleophile substitution reaction to generate hydrochloric acid. Reaction is carried out

in dichloromethane in presence of Triethylamine to form BOC Nitro and TEA. HCl formed as

by-product. As per work-up procedure water is added and separated organic layer and aqueous

layer. Organic layer is distilled out to get crude BOC Nitro. Crude BOC nitro is isolated from

mixture of ethyl acetate and methanol to give BOC nitro.

Aqueous layer is treated with sodium hydroxide so TEA. HCl is neutralized to get Triethylamine

layer. Organic layer (Triethylamine) separated from aqueous layer to reduce effluent load. TEA

layer to be used to get Triethylamine hydrochloride.

Following are the key factors for reducing effluent load.

Sr

No

Chemical name Input qty kg/kg of

product

(Previous process)

Input qty kg/kg

of product

(New process)

Reduction

(%)

1 Tert-butyl[(1S, 2R)-1-benzyl-2-

hydroxy-3-(isobutyl amino)

propyl]carbamate (K1601)

0.652 0.652 -

2 4-nitrobenzenesulfonyl chloride

(Nosyl Chloride)

0.710 0.463 34.78%

3 Dichloromethane 12.000 8.040 33%

4 Triethylamine 0.600 0.291 51.5%

5 Sodium carbonate 0.200 0.130 35%

6 Ethyl acetate 3.600 0.914 74.61%

7 Methanol 20.300 13.990 31.08%

8 Anhydrous Sodium sulfate 2.000 0.326 83.7%

9 Water 3.259 2.960 9.18

10 Sodium hydroxide 0.326 0.326 -

Total Input 43.63 28.09 35.61%

Effluent generation 6.11 lts/kg 4.10 lts/kg 32.89 %



• We have reduced quantity of Nosyl chloride almost stoichiometric and triethylamine as

per process requirement (1.5 mole equivalent). Reaction is completed within time frame

and there is no adverse effect on quality.

• Dichloromethane quantity reduced by 33% in main reaction.

• Methanol quantity reduced by 31.08 % and Ethyl Acetate reduced by 74.61% during

purification and product isolation.

• Improved recovery of MDC and mixture of ethyl acetate and methanol.

• As per process requirement recovered dichloromethane should be washed with water to

remove traces of methanol.

• Water quantity reduced because of 1st washing aqueous layer is kept a side and same is

used in next batch washing so overall quantity of water is reduce. 9.18%

Existing Mass balance:-

Sr.

No.

Name of Chemicals Unit Kg/Kg of

product

Output kg/kg of

product

1 K1601 Kg 0.652 Product 1.000

2 MDC Lit 12.000 Process Effluent 6.110

3 TEA Kg 0.600 Mix Solvent 33.41

4 Nosyl Chloride Kg 0.710 TEA layer 0.610

5 Na2CO3 Kg 0.200 Solid waste 2.5

6 Na2SO4 Kg 2.000

7 Methanol Kg 20.300

8 Ethyl Acetate Kg 3.600

9 Sodium Hydroxide Kg 0.326

10 Water 3.259

Total 43.63 43.63



Proposed Mass balance:-

Sr.

No.

Name of Chemicals Unit Kg/Kg of

product

Output kg/kg of

product

1 K1601 Kg 0.652 Product 1.000

2 MDC Lit 8.04 Process Effluent 4.10

3 TEA Kg 0.291 Mix Solvent 22.279

4 Nosyl Chloride Kg 0.463 Solid waste 0.4

5 Na2CO3 Kg 0.130 TEA layer 0.311

6 Na2SO4 Kg 0.326

7 Methanol Kg 13.990

8 Ethyl Acetate Kg 0.914

9 Sodium Hydroxide Kg 0.326

10 Water kg 2.96

Total 28.09 28.09

2.4 MARKET FEASIBILITY

Established in 1991, ZCL Chemicals Ltd (ZCL) is head quartered in Mumbai. The cGMP

manufacturing facility and state-of-the art R&D Center are located in the Industrial park of

Ankleshwar in Gujarat State. ZCL combines the power of Science & Technology and has been

into manufacturing of Active Pharmaceutical Ingredients (APIs) and Advance Intermediates for

Innovator and Generic companies around the world. Has earned the preferred partner status from

some of the Global Pharmaceutical companies.ZCL production site has been successfully audited

and approved by the US FDA, KFDA, WHO-GMP and Japanese customers.

It is a policy of ZCL CHEMICALS LTD, That Commitment towards competency in Quality,

lead time and overall economic feasibility must satisfy our esteemed customers.

Continual improvement towards technical and after sales service aspects of all products shall be

our motto. Renovation towards the best shall be equally participated from all our employees to

drive the organization towards achieving further success & growth in business.

Our quality system is based on ICH Q7 GMP requirements.

Our quality consciousness shall be recognized through achieving excellent implementation level

of ISO 9001:2000; ISO 14001:2004, OHSAS 18001:2007 Norms.



2.5 EMPLOYMENT GENERATION DUE TO THE PROJECT

The details are given below.

TABLE: 3

DETAILS OF MANPOWER

Sr.

No. Phase of Project Type of Labor No. of Worker

1 During construction Contractual --

2 During

commissioning Contractual --

3 During operations

Managerial 130

Skilled 40

Un-skilled 120

Total: 290

Note: There will be no change in No. of manpower due to Proposed Expansion.

3.0 PROJECT DESCRIPTION

3.1 TYPE OF PROJECT

The proposed project is not including any interlinked and interdependent projects.

3.2 PROJECT LOCATION

The proposed project site is located atPlot No. 3102/B, GIDC Industrial Estate, Ankleshwar,

Dist.Bharuch in the state of Gujarat. It is approximately 20 km distance from district head

quarter Bharuch. The approximate geographical positioning of the project site is at Latitude: 21o

37’ 36” N, Longitude: 73o01’ 58” E. The location of the project site can be identified from the

location map shown in Figure -2.

The salient features of the location of the project site are presented in below Table.4.



TABLE: 4

SALIENT FEATURES OFTHE PROJECT SITE

Particulars Details

Village Ankleshwar

Taluka/ Tehsil Ankleshwar

District Bharuch

Approx. Geographical positioning Latitude: 21o 37’ 36” N

Longitude: 73o

01’ 58” E

Nearest City Bharuchabout 20 KM

Nearest Town Ankleshwar

Nearest Highway National Highway No. 8

Nearest State highway National Highway No. 8

Nearest Railway line/ Railway

station

Ankleshwar Railway Station

Nearest Airport/ Airbase Vadodara about 94 KM

FIGURE: 1

LOCATION OF THE PROJECT SITE

Ankleshwar Industrial area

Panoli Industrial area

Jhagadia industrial area

Priaman CETP

Canal

Piraman to Katiyajal Effluent

Pipe

Jhagadiato Piraman CETP

Panoli toPiraman CETP

PROJECT SITE



FIGURE: 2

AERIAL VIEW OF THE 5 KM RADIAL PERIPHERY FROM THE PROJECT SITE



3.3 SITE SELECTION

This is capacity increase proposal, so the proponent did not consider any other alternative site for

proposed expansion. The existing plot has sufficient area for carrying out expansion.

3.4 NEIGHBOURING INDUSTRIES

The industry is located in an area, which is already industrialized. The industries in the vicinity

of the proposed project are given in the table 5:

TABLE: 5

NEARBY INDUSTRIES IN THE VICINITY

Name of Industry Direction with

respect to project

site

Address

United Phosphorus

Limited (Unit- 2)

East side of

company

Plot No. 3405/3406, GIDC Industrial

Estate,Ankleshwar-393001

Glenmark

Pharmaceutical

Ltd.

North side of

company

Plot No. 3109/C, GIDC Industrial Estate,

Ankleshwar-393001

RPG Life Sciences

Limited.

South side of

company

Plot No. 3102/A, GIDC Industrial Estate,

Ankleshwar-393001

United Phosphorus

Limited (Unit- 3)

West side of

company

Plot No. 3101/2, Ankleshwar GIDC,

Ankleshwar - 393001

3.5 SIZE OF PROJECT

The expected cost of proposed project is NIL.

Environment Protection and safety systems are existing currently. Green belt development,

provision of fire extinguishers etc. are Available. The following table shows the break-up of the

project cost.



TABLE:6

CAPITAL COST OF EXISTING

Sr.

No.

Purpose Total

(Rs. In Lacs)

1 Land 138.15

2 Building 1,141.97

3 Plant and Machinery 2,045.12

4 Q.A. Lab set up 49.32

5 Env. Protection & Safety 94.32

a) Effluent treatment Plant

b) Air pollution control & Hazardous waste management

c) Safety Equipment (PPE, fire extinguishers, Ventilation,

etc.)

d) Green belt development

Total 3,468.89

3.6 PROCESS TECHNOLOGY

Process details like process description for each grade of products are covered separately in

Annexure-VIof Form-I.

3.7 RAW-MATERIALS

The required raw materials will be purchased from the local/ Indian market& China. Details of

raw-material consumption are covered in Annexure-V of Form-I.

3.8 RESOURCE OPTIMIZATION/RECYCLING AND REUSE

3.8.1 SOLVENT RECOVERY

Methanol (81% recovery), MDC (83% recovery), Toluene (90% recovery),Chloroform (73%

recovery), Xylene (74% recovery), Acetic Acid (79% recovery) and Hexane (79% recovery) are

the solvent to be used in the process. There will be provision of recovery of solvent.



3.9 RESOURCE REQUIREMENTS

3.9.1 LAND

The plot had been purchased by M/s.ZCL Chemical Limited from GIDC. The total plot area of

the unit is 35595 sq. m.

3.9.2 BUILDING

No construction activity will be done for the proposed expansion project.

3.9.3 POWER AND FUEL

The unit’s power and fuel requirement is provided in Table 7. There will not be any increase in

fuel consumption.

TABLE:7

POWER AND FUEL REQUIREMENT

3.9.4 WATER

The category wise bifurcation of the water requirement is given in Table no 8. The source of

water will be from GIDC water supply scheme. There will be no change in Proposed Water

consumption due to Proposed Increased capacity.

Sr.

No.

Particulars Existing as per

Consent Quantity

Proposed

Quantity

Total

Quantity

Source

1. Natural Gas

for Boiler &

Thermic Fluid

Heater

290 SCM/Hrs -- 290 SCM/Hrs Gujarat

Gas

2. Diesel For DG

Sets

117 Lit/Day -- 117 Lit/Day Local

Supplier

3. Energy-

Electricity

950 KVA -- 950 KVA DGVCL



TABLE:8

DETAILS OF WATER CONSUMPTION

3.9.5 MANPOWER

The manpower required for the project as well as during the construction/commissioning

activities will be employed from the local area. The details are provided in Table 3.

Sr.

No. Phase of Project Type of Labor No. of Worker

1 During construction Contractual --

2 During

commissioning Contractual --

3 During operations

Managerial 130

Skilled 40

Un-skilled 120

Total: 290

3.10 MITIGATION MEASURES & EMP

Based on overall manufacturing & operation activities, the mitigation measures have been

proposed by the company for the control of the anticipated pollution load.

Particulars Existing water

consumption

(KL/Day)

Proposed water

consumption

(KL /Day)

i) Domestic+Others

(gardening etc) 21.2 21.2

ii) Industrial

Process 25 25

Boiler 12 12

Cooling 64.8 64.8

Washing 42 42

Total 165 165



3.10.1 WASTEWATER MANAGEMENT

3.10.1.1 WASTEWATER GENERATION

The category-wise bifurcation of the anticipated wastewater generation details is given in Table 9.

There will be no change in Proposed Wastewater generation due to Proposed Expansion.

TABLE: 9

DETAILS OF WASTEWATER GENERATION

Particulars Existing Wastewater

generation(KL/Day)

Proposed Wastewater

generation(KL /Day)

i) Domestic+

Others

(gardening etc)

10 10

ii) Industrial

Process 14 14

Boiler 4 4

Cooling 3 3

Washing 24 24

Total 55 55

3.10.1.2 WASTEWATER CHARACTERISTICS

Industrial wastewater will be generated from process, cooling tower and boiler. The expected

characteristics of industrial wastewater are provided in Table 10.

TABLE: 10

WASTE WATER CHARACTERISTICS

Sr.

No. Parameters Units

Standards

prescribed

by GPCB

Standards

prescribed by

NCTL

Before

Treatment

After

Treatment

1 pH -- 5.5 to 8.5 5.5 to 8.5 6- 9 6.5-8.5

2 Colour Pt Co 100 -- 400-1000 50-70

3 Total Suspended Solids mg/l 100 -- 4500-5500 30-60

4 Total Dissolved Solids mg/l 2100 -- 30000-35000 2000-2300

5 Oil & grease mg/l 10 -- 8-11 Not detected

6 Phenolic compounds mg/l 1 -- 1-3 Not detected

7 Cyanides mg/l 0.2 -- Not detected Not detected

8 Ammonical Nitrogen mg/l 50 100 600-800 30-50

9 Sulphate mg/l 1000 -- 5000-6000 200-300

10 B.O.D.(3 days at 27°C) mg/l 30 -- 10000-12000 55-70

11 C.O.D. mg/l 100 1000 30000-35000 170-200



3.10.1.3 WASTEWATER TREATMENT & DISPOSAL



TABLE: 11

DEMENTIONAL DETAILS OF ETP UNITS

Sr.

No. Name of Equipment Capacity

Retention time

in Hrs. MOC

1 Collection Tank 66 KL 26.4 RCC

2 Neutralization Tank 41 KL 16.4 RCC

3 Filter Press - - -

4 Filter Press Tank 05 KL 2 RCC

5 MEE Plant 40 M3/Day - MS

6 MEE O/L Collection Tank 36 KL 14.4 RCC

7 Primary Clarifier 20 KL 8 RCC

8 Aeration tank 150 KL 60 RCC

9 Secondary Clarifier 20 KL 8 RCC

10 Sludge Drying Bed 10 M2 - RCC

11 Secondary O/L Collection Tank 40 KL 16 RCC

12 Old Holding Tank 12 KL 4.8 MS

13 New Holding Tank (Final

Discharge Tank) 75 KL 30 RCC



FIGURE:3

FLOW DIAGRAM OF ETP



FIGURE :4

FLOW DIAGRAM OF MEE



3.10.2 GASEOUS EMISSIONS & CONTROL

3.10.2.1 FLUE GAS EMISSIONS

There will be flue gas emission from one Boiler, Thermic fluid heater and Two DG sets. Natural

gas is fuel and diesel will be used as fuel in DG set. The air pollution control measures are

covered in below table 12.

TABLE:12

DETAILS OF FLUE GAS EMISSIONS

Sr.

No.

Stack

Attached

To

Stack

Height

Stack

Diameter

Fuel

Consumption

Air

Pollution

Control

System

Type

of

Emission

Permissib

le Limit

As per Existing

1. Boiler

G1207A 30 m

0.45m

(Top) Natural gas --

PM

SO2

NOx

150

mg/NM3

100 PPM

50 PPM 2.

Thermic

fluid heater 22 m

0.5m

(Top) Natural gas --

As per proposed expansion

There will be no change in Flue gas emission due to Proposed expansion.

3.10.2.2 PROCESS EMISSIONS

The process emissions from the proposed manufacturing activities are given in Table 13.

TABLE:13

DETAILS OF FLUE GAS EMISSIONS

Sr.

No.

Stack

Attached

To

Stack

Height

(m)

Stack

Diameter

(m)

Air Pollution

Control System

Type of

Emission

Permissible

Limit

As per Existing

1. Reactor Vessel

Plant - 1

25 0.15 Water

Scrubber+Caustic

Scrubber

HCl

SO2

CL2

20 mg/Nm3

40 mg/Nm3

9 mg/Nm3

2. Reactor

Vessel Plant -

2

15 0.15 Water

Scrubber+Caustic

Scrubber

HCl

CL2

NH3

20 mg/Nm3

9 mg/Nm3

175 mg/Nm3

As per proposed expansion

There will be no change in Process emission due to Proposed expansion.



3.10.3 HAZARDOUSWASTE MANAGEMENT

The following type of hazardous waste will be generated from the operational activities. All the

waste will be stored separately in a designated storage area.

TABLE:14

DETAILS OF HAZARDOUS WASTE GENERATION

Sr.

No.

Name of waste Cat.

No.

Quantity Method of disposal

Existing Proposed Total

1. ETP Sludge 34.3 339 MT / year 0 339 MT / year Collection, storage within

factory premises,

transportation and final

disposal at TSDF

M/s.BEIL.

2. Carbon Waste 35.3 18.25 MT /

year

0 18.25 MT /

year

Collection, storage within

factory premises,

transportation and

incineration at TSDF

M/s. BEIL/RSPL

&Ambuja Cements for

Co -processing.

3. Distillation

residue

20.3 36.5 MT /

year

0 36.5 MT / year Collection, storage within

factory premises,

transportation and


M/s. BEIL/ RSPL

&Ambuja Cements for

Co -processing.

4. Discarded

containers

33.3 43800 Nos /

year

0 43800 Nos /

year

Collection, storage with

in factory premises,

transportation and sell to

authorized vendors.

5. Distillation

residue from

contaminated

organic solvents

36.4 0.73 MT /

year

0 0.73 MT / year Collection, storage within

factory premises,

transportation and


M/s. BEIL/RSPL

&Ambuja Cements for

Co -processing.



6. Used / Waste Oil 5.1 1.83 MT /

year

0 1.83 MT / year Collection, storage,

treatment within factory

premises, transportation

and sell to registered

refiners.

7. Contaminated

solvents not fit

for originally

intended use

20.1 73 MT / year 0 73 MT /year Collection, storage,

recovery and reuse within

premise at site.

8. Spent solvent 20.2 73 MT / year 0 73 MT / year Collection, storage,

recovery and reuse within

premise at site.

9. High COD waste

from MEE

stripper

20.2 540 MT/year 0 540 MT/year Collection, storage within

premises. Disposal at

TSDF/Incinerator.

Note: There will be no change in Hazardous waste generation due to Proposed Expansion.

3.10.4 NOISE CONTROL & ODOUR

The major noise generating installation will be the D.G. Set. It will be installed in a closed room,

acoustic enclosure will be provided around it.

Ear plugs will be provided to the operating personnel in boiler room. Low noise generating

equipments will be selected. Adequate engineering controls will be implemented to avoid noise

pollution.

The following steps will be taken for odour control.

• Raw-material feeding will be carried out by pumps and in close loop system.

• All reactions will be taken in closed reactor system.

• Roof top ventilation will be provided in the entire plant area.

• Regular monitoring will be done of piping and fittings for checking of any leakages.



3.10.5 STORAGE, HANDLING AND TRANSPORT OF HAZARDOUS

CHEMICALS

The storage and mode of transport of chemicals will be done as per detailed MSDS and chemical

hazards guidefor the hazardous chemicals.

Few chemical to be used in the proposed activities are listed as ‘Hazardous Chemicals’ as per the

Schedule-1 of the MSIHC Rules, as amended in 2000.

3.10.6 HEALTH AND SAFETY MEASURES

Few chemical to be used in the proposed activities are listed as ‘Hazardous Chemicals’ as per the

Schedule-1 of the MSIHC Rules, as amended in 2000.

Physical hazards may manifest as fires, explosions, excessive temperatures, or the release of

large volumes of gas or toxic or flammable gases or vapors. According to Schedule 2 & 3 of

MSIHC Rules.

Below mentioned is the safety measure to be taken at site for control of anticipated hazards.

Identification, analysis, assessment of hazards and risk provides vital information to risk

management. Objective of this plan is to assess the risk and to provide guidelines for facing and

controlling the emergency.

This contains the information of possible hazards and their effects on the workers, general public

and environments.

• Hazards in storage area :

Following are possible storage hazards

� Fire

� Explosion

� Spillage / leakage

� Failure of storage tanks

� Toxic gas release

Most of the chemicals are toxic in nature other than some exception. Toxic substances affect in

three ways by ingestion, absorption and inhalation. Adequate provision of safety is done to work

with toxic materials.



� All raw materials, solvents, intermediates and finished goods are stored

according to their compatibility with other chemicals. The various places

where chemicals, solvents are stored are :

- Licensed tank farm area

- Raw material store

- Cold Room

- WIP room

- Bonded store

� All the flammable liquid materials are stored in storage tanks. The tank

farm for Petroleum Class A, B & C liquids is approved by Chief

Controller of Explosives after due inspection.

� The storage tanks are mounted above grounds with bund. Bund capacity is

1.1 times higher than big tank.

� The other chances of fire hazard may be due to generation of static

electricity due to flowing of solvent in the pipeline by accumulating

electrical charge & resulting spark. For this, company has provided

adequate number of static jumpers on each flange joints with proper

earthing.

� For vehicles like tanker, which carry flammable solvents, an additional

facility is provided at gate house for dissipation of static charge generated

by the tanker while coming to company from its supplier’s location.

� Rule of no smoking is observed strictly in the company premises.

Company has implemented “No Smoking Policy” and at appropriate

places, boards are displayed.

� All the safety standards & parameters are observed strictly. The total area

is provided with adequate firefighting equipment also.

� Earthing facility is provided at the unloading point to provide earthing to

the tankers at the time of unloading.

� Flame arrestor is provided on the vents of tanks containing flammable

liquid.

� The tankers are provided with the flame arrestors (mufflers) while

entering inside the factory premises.

� The raw water tanks with capacity 250 M3.



� Water sprinkler provided on the tanks containing the flammable liquid in

tank farm area.

� The employees are trained in first aid fire fighting.

� Adequate SOPs are in place for safe handling of chemicals and concerned

employees are trained for the same.

� Spillage kit is provided to contain spillage / leakage.

• Fire and explosion

� The fire and explosion risk are associated with

- Solvents like Methanol, Toluene, Acetone, etc.

- Chemicals like phosphorous pentoxide, etc.

- certain chemical reaction like hydrogenation, grignard, distillation,

� Electrical short circuit

� The fire risk is not affecting outside factory. And hence the risk is limited

to factory area.

� The gas dispersion is Nil.

� To control the fire, fire extinguishers like DCP, CO2 and Foam are

provided. Also, factory has installed the DCP modular in the solvent tank

farm.

� Adequate water tanks having 750 M3 capacities. Facility for water at

several places in plant and factory premises.

� Sprinkler system in tank farm area to control vapour emission and thereby

reduced fire risk.

� Vapor detector system are installed in the warehouse

• Spillage control

� SOP for prevention and control of spillage

- Eliminate all sources of ignition immediately.

- Ventilate the area but isolate the material.

- Absorb the chemical into sand.

- Allow atmospheric evaporation.



- Flush the spilled area with water and detergent.

� Spillage kit for spill control.

� In tank farm area, checking of bund and bund valve is introduced and

being checked regularly.

� Training for spillage control and handling to all employees.

� Fumes and cylinder leakage kit are available.

� All employees are trained for first aid fire fighting and use of personal

protective equipments.

� The duties of responsible persons are as follows :

- To guide the people to stop the leakage and spillage.

- To ensure good housekeeping.

• Technological and civil

Our main products are bulk drug and their advanced intermediates. Considering

the use of hazardous chemicals, following steps are taken.

� All structure and other equipments are fabricated as per the engineering

specification laid down in appropriate specification of international and

national bodies in the subject.

� Vessels are equipped with temperature indicators, pressure gauges, level

indicators, safety valves, etc.

� Vessels are pressure tested as per Factories Act, 1948. Flame proof fittings

are provided.

� Regular inspection is carried out by external agency to maintain proper

health of plant, equipment and machinery.

� Thickness of tanks is carried out periodically and record maintained in

Form 11 as per Factories Act.

� Building structure is constructed as per standard practice. Material used is

tested for its quality and suitability under guidance of experts approved

under Government notification.

� The structure is being inspected by Government approved competent

person periodically and stability certificate is maintained.



� Inspection, maintenance, painting of plant / machinery etc, is carried out

regularly.

• Toxic release risk

The potential risk involved is leakage from tanks and pipelines.

To attain the toxic release of gases (DMS and Ammonia) from cylinder, cylinder

leakage control kit is available.

Fumex are available for the dilution of atmosphere inside the plant or used as an

exhaust or in case of tank cleaning it also used as a exhaust fan for fast dilute

Material Safety Data Sheet is kept as ready reference at all critical areas.

Evacuation table is displayed at gate.

Training is given related to Emergency Preparedness to both old and new

employees.

4.0 SITE ANALYSIS

4.1 CONNECTIVITY

The site is located at Plot no. 3102/B, GIDC Estate, Ankleshwar, Gujarat. The land and

Infrastructure is already available and the raw materials are easily available through the easy

transport via road connectivity.

Ankleshwar Industrial Estate was set up by Gujarat Industrial Development Corporation in early

70s. This industrial estate is spread over an area of 1600 hectares in close proximity to National

Highway No.8 and Delhi-Mumbai Railway Line. Being an ideal location for industrialization, as

on date, more than 1500 industries, consisting of chemicals, pesticides, pharmaceuticals, bulk

drugs, petroleum products, engineering, textiles, plastics, rubber and packaging etc. are located

in this industrial estate.

The town is known for its industrial township called GIDC (Gujarat Industrial Development

Corporation). Ankleshwar has an office of the ONGC (Oil and Natural Gas Corporation



Limited). GIDC is organizing Trade fare and Industrial expo occasionally to attract large number

of industries all over from India. It also helps to get customer on large basis.

Ankleshwar is connected by Indian National Highway 8 (Mumbai to New Delhi) and by the

Western Railway Division of Indian Railways. The railway division also runs the broad

gauge train services to Rajpipla. The 133 year-old Golden Bridge connects Ankleshwar to

Bharuch across the Narmada on the station front while a new bridge connects the highway, the

other bridge on the highway is now ready to use.

Ankleshwar City Bus stand is located on Station Road (i.e. located in the City, the western

section).

Development project of Ankleshwar Airport & City Bus are in pipe line in last stage.

Ankleshwar is an educated city. It has an average literacy rate of 79%, higher than the national

average of 59.5%; with 56% of the males and 44% of females literate.

Ankleshwar JN Rail Way Station, Sanjali Rail Way Station are the very nearby railway station to

Ankleshwar GIDC. However Surat Rail Way Station is major railway station 56 KM near to

Ankleshwar GIDC.

Healthcare

Hospitals include are the

• Jayaben Modi Hospital,

• Sarvajanik Hospital,

• Sanjivani Hospital

• Sardar Patel Hospital.

• And now ESIC's (Employee State Insurance Corporation)New Hospital is under Construction.

• In April 2014, the "New Life" private hospital was constructed in Jasaat Plaza (Station

Road). It is conveniently served by Ankleshwar's main bus & railway stations.

Shopping and Recreation:

• There is a lake in GIDC & City area. Situated in front of GIDC Lake, Lakeview Plaza

Mall is city's first truly integrated mall for restaurants, entertainment and hotel stay.



• NavGraha Jain Mandir (G.I.D.C), ManavMandir, Sai& Swaminarayan Temple are big

temples in Ankleshwar. Ankleshwar City is also having big Mosques HalimshaDatar

Bhandari, Garibnawaz, etc.

• Centers of Brahma Kumaris World Spiritual University is located in both GIDC and City

area which helps you to know your true self with the help of Free Rajyoga Meditation

Classes.

• There are parks such as The Millennium Park and old parks in Ankleshwar city, the GIDC

Water Reservoir, and sports center.

• There are swimming pools, Joggers park, children's park, Rotary library and other

recreation centers in the GIDC area.

• There is an Open Air Theater in GIDC Area. Chauta Bazar is the biggest shopping area in

Ankleshwar.

4.2 LAND USE AND LAND OWNERSHIP

The existing project site is located at plot no 3102/B, GIDC Estate, Ankleshwar, Gujarat. The

total plot area of the unit is 35595 Sq. M. Land ownership is with project proponents. The

geographical location is 21o 37’ 36” N latitude and longitude 73

o1’ 58” E.

They have valid consent from Gujarat Pollution Control Board, Gandhinagar. And the consent

no. is AWH:72765 and it is attached as an Annexure-XIII.

4.3LAND USE

The existing project site is located at plot no 3102/B, GIDC Estate, Ankleshwar, The plot is

notified by GIDC for industrial purpose.

4.4 EXISTING INFRASTRUCTURE

The project is currently located in a well-developed zone, which have all essential facilities such

as well-connected road network with ease of transportation, arrangement for supply of water and

power to industries, effluent disposal facilities etc.



4.5 SOIL CLASSIFICATION

The soils of the district are derived from the Deccan trap which is main rock formation of the

district. The soil of the district can be classified as light, medium and heavy according to depth,

texture and location. There is sandy loam to loamy in texture, brownish black in color.

4.6 CLIMATE DATA

As per gathered meteorological data, the maximum temperature is 42.4°C, where as the

minimum temperature is 14.8°C. The relative humidity levels varied from 13% to 86%. The

maximum and minimum as well as relative humidity for a period of March, 2014 to May, 2014

are presented in Table 15.

TABLE:15

DETAILS OF MICRO METEOROLOGICAL DATA

(Data from Indian Meteorological Department, Ahmadabad)

Based on the above metrological data, wind rose has been prepared for the summer season

period from March 2014 to May 2014. As per the metrological data, it shows that the average

wind speed in March, April, and May 2014 is 2.76 m/s with wind direction blowing to NE.

The wind rose prepared from same data is shown at Figure 5.

Month Temperature(oc) Humidity (%) Rain fall (mm)

Maximum Minimum Maximum Minimum Maximum Minimum

MARCH 2014 38.2 14.8 84 13 00 00

APRIL 2014 41.8 20.6 86 14 00 00

MAY 2014 42.4 27.2 83 17 0.8 00



FIGURE:5

WIND ROSE DIAGARMFOR PERIOD (MARCH TO MAY, 2014)

4.7 SOCIAL INFRASTRUCTURE

Population density and sex ratio of Bharuch District was reported 238 persons/sq.km. and 920

females per 1000 males respectively in 2011 census report. Total literacy of Bharuch District

was found 81.51 %.The basic amenities like primary and secondary education schools,

community health workers, primary health sub centre, private practitioners, primary health

centre, maternity and child welfare, dispensaries, T.B clinic, family welfare centre, hospital,

drinking water, transportation facilities, electricity , telephone etc. are available.



5.0 PLANNING BRIEF

5.1 PLANNING CONCEPT

Ankleshwar is largely an industrial area dominated by large scale industries, especially chemical

plants& Pharmaceutical plants.

Now the unit has proposed to increase manufacture capacity of BOC Nitro without increase in

pollution load.

Ankleshwar in Gujarat has an industrial area with common effluent treatment plant, common

incinerator and land fill site. Govt. agencies provide many basic facilities like uninterrupted

water supply, power and road network.

5.2 POPULATION PROJECTION

As per provisional reports of Census India, Population of Bharuch District in 2011 is 1,551,019.

Population of male and female are 805,707 and 713,676 respectively. The sex ratio of Bharuch

city is 920 females per 1000 males.

In education section, total literates in Vadodara District are 2,893,080 of which 1,614,087 are

males while 1,278,993 are females. Average literacy rate of Vadodara district is 78.92%.

5.3 LAND USE PLANNING

The proposed project is on a GIDC land.

5.4 ASSESSMENT OF INFRASTRUCTURE DEMAND

The M/s. ZCL Chemicals Ltd. shall get water from GIDC water supply scheme. So there will be

no additional stress on ground water resources and there will be no adverse effect on the ground

water resources available in the nearby area.

The unit has proposed 950 KVA connected load form DGVCL. The transportation facilities will

also expect to improve due to increase in the movement of workers and raw material and finished

products.



5.5 AMENITIES/FACILITIES

The available basic amenities are as under:

(A) Education Facilities:

All the villages have a minimum of one primary school.

(B) Medical Facilities:

All the surrounding villages have medical facilities.

(C) Drinking water Facilities & Power Supply:

All the villages have potable water supply and in 100% area the drinking water is

supplied through taps, wells and tube wells. All the villages have power supply facilities

in the study region.

(D) Post, Telegraph & Telephone facilities

The information collected clearly indicates that the infrastructural facilities are provided

by respective government agencies for the development of this area. For communication

purpose, post office and phones are available in most of the villages.

(E) Transport Facilities:

Bus services are available in all the villages of the study region within 5 km area and are

the most preferable mode of transport in the region. Auto-rickshaw is also used as

transport facility. Villages are connected with paved roads. All the surrounding area is

covered with 108 emergency facilities.

6.0 PROPOSED INFRASTRUCTURE

6.1 PROCESSING AREA

The process area will cover plant area likeU-1A, 1B, 2A, 2, 3, 4, ETP and utilities. The process

area covered by the unit at ground level will be 4519.59sq.m.



6.2 NON PROCESSING AREA

The non process area will cover Electrical panel room, CCOE area, Warehouse-solid & liquid,

TOC Room, 22KV Breaker Room, canteen, U/ground water tanks-all, Cold Room, Security

cabin & OHC Room, HT Yard and surrounding area-utility & main, Admin Block, Scrap yard,

open area near H2 plant, BHP Gully and all roads and passages, contractor sheds,Parking area

etc. The non process area covered by unit at ground level will be around 24860.37 sq. m.

6.3 GREEN BELT

Out of the total land area of 35595 sq. m. approximately 18% will be utilized for green belt

development. The proposed greenbelt area is 6215.04 sq. m.

6.4 SOCIAL INFRASTRUCTURE

The availability of basic amenities is covered as under:

(A) Training & Education: All the employees will be trained and educated periodically about

the hazardous nature of chemicals used in the process. Also, training for firefighting, work

permit system, first aid, safe handling of hazardous chemicals and integrating safety, in all

activities.

(B) Medical facility: Pre-employment medical checkup at the time of employment. In order to

safe guard the health of the employees, all the employees undergo periodic health checkup.

(C) Drinking water: There will be provision of Aqua Guard/R.O. at different places to provide

purified water for drinking purpose.

(D) Transportation: The unit will provide basic transportation facility for workers.

(E) Telegraph & Post: There will be provision of telephone, fax & internet facility.

(F) Power supply: There will be total connected load of 950 KVA from DGVCL.

6.5 CONNECTIVITY

Ankleshwar estate is well connected by rail and road to rest of country.



6.6 DRINKING WATER MANAGEMENT

Average daily water consumption of unit will be 9.7 KL/Day for domestic purpose. The entire

water requirement will be meeting through GIDC water supply system.

6.7 SEWAGE SYSTEM

The sewage will be diverted in soak pit. The overflow of soak pit is treated in ETP.

6.8 INDUSTRIAL WASTE MANAGEMENT

The hazardous waste like ETP sludge, Carbon Waste, Distillation residue, Discarded containers,

Distillation residue from contaminated organic solvents, Used/Waste Oil, Contaminated solvents

not fit for originally intended use ,Spent solvent, High COD waste from MEE stripperwill be

generated from the proposed activity.There will be no change in Hazardous waste generation due

to Proposed Expansion. The hazardous waste management and disposal is shown in Annexure-

XI in Form-I.

6.9 SOLID WASTE MANAGEMENT

The record of hazardous and non Hazardous waste solid waste like Personal Protective

Equipments, etc

6.10 POWER REQUIREMENT & SUPPLY

The unit will use total 950 KVAelectricity connected load from DGVCL.

7.0 REHABILITATION AND RESETTLEMENT(R &R) PLAN

The proposed project is located in Plot No: 3102/B, GIDC Estate, Ankleshwar, Dist-Bharuch,

Gujarat-391440. There will be no any human settlement affected by proposed project.



8.0 PROJECT SCHEDULE & COST ESTIMATES

8.1 PROJECT IMPLEMENTATION SCHEDULE

TABLE: 16

PROJECT IMPLEMENTATION SCHEDULE

Project implementation schedule after getting NOC from GPCB

Sr.

No.

Activity Required Period

1. Civil work not required

2. Procurement of

machinery

not required

3. Erection & installation

of machinery

not applicable

4. Trial of machinery &

equipment

not applicable

5. Commercial activity Not applicable

8.2 ESTIMATED PROJECT COST

The project cost will be Nil for proposed expansion project.

9.0 ANALYSIS OF PROPOSAL

All the manpower is utilized from local region around Ankleshwar. Company shall also try to

provide indirect employment opportunities by availing local contract services during

transportation during operational phase.

The company intends to donate 2% of the profit to agencies like NGOs or social welfare

societies for projects carried out in nearby village for their welfare and upliftment.

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