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M/s Synthetic Drugs & Intermediates., Ankleshwar.

M/s. Jyoti Om Chemical Research Center Pvt. Ltd., Ankleshwar. 1

1.0 EXECUTIVE SUMMARY

M/s. Synthetic drugs & Intermediates is located at Plot No. 6503, GIDC Estate, Ankleshwar,

Dist.: Bharuch -393 002, Gujarat.

Unit is having valid CCA-AWH-99468 for the manufacturing Derivatives Benzoic Acids, Nitro

chloro benzoic acid and 4 methoxy 3 nitro benzoic acid.

Now unit wants to increase production, hence unit is going to apply for the EC on plot no. 6503,

Ankleshwar, Dist- Bharuch. Detail of existing products is mentioned in below Table No.1.

TABLE: 1 LIST OF EXISTING PRODUCTS Sr. No.

Name of Products CAS No. Quantity in MT/Month

1.0 Derivatives of Benzoic Acids -- 20 2.0 Nitro Chloro Benzoic Acids

Either/or Methyl Nitro Benzoic acid

000197 Either/or 5-50-4

21

3.0 4 Methoxy 3 Nitro Benzoic acid Either/or 5 Nitro salycilic acid

89-41-8 Either/or 9-41-8

5

TABLE: 2 LIST OF PRODUCTS AFTER PROPOSED EXPANSION

Sr. No.

Name of the

Products

CAS no. /

CI no.

Quantity MT/Month End-use of the

products Existing Proposed Total

1.0 Derivatives of Benzoic Acids

-- 20 +60 80 Pharma Industries/

Pigment Industry

2.0 Nitro Chloro Benzoic Acids Either/or methyl Nitro Benzoic acid Either/or Derivatives of Nitro Benzoic Acids

2516-96-3 Either/or 5-50-4 Either/or --

21 +59 80 Pharma Industries/

Pigment Industry

3.0 4 Methoxy 3 Nitro Benzoic acid Either/or 5

89-41-8 Either/or 9-41-8

5 0 5 Pharma Industries/

Pigment Industry



Nitro salycilic acid

4.1 Chloro Nitro Sulphonyl chloride Benzoic acid OR/and

Group 0 +10 10 Pharma Industries/

Pigment Industry

4.2 Di nitro Naphthalene OR/and

605-71-0

and

602-38-0

0 +10 10 Pharma Industries/

Pigment Industry

4.3 Derivatives of Benzo phenones OR/and


Pigment Industry

4.4 2,4 Di chloro Phenoxy acetyl chloride OR/and

774-74-3 0 +10 10 Pharma Industries/

Pigment Industry

4.5 Chloro benzoic acid sulfonyl chloride OR/and


Pigment Industry

4.6 5 Niro Iso phthalic acid OR/and

618-88-2 0 +10 10 Pharma Industries/

Pigment Industry

4.7 Nitro phthalic acid


Pigment Industry

Total 46 129 175

1.1 COST OF PROJECT The expansion will be carried out at existing plot in GIDC Estate, Ankleshwar Gujarat. The total cost of the unit after proposed expansion is Rs. 4.51 Crore. 1.2 FUEL AND ELECTRICITY CONSUMPTION

Existing natural gas permission is 25 Nm3/Hr which will be reached at 148 Nm3/Hr. Unit is

consuming LDO of 15 Lit. /hr as per existing CCA, it will be increased 60 Lit. / Hr. As per existing CCA Unit is using diesel 35 Lit/hr, it will remain same after proposed expansion.



1.3 WATER CONSUMPTION Unit is using 15 KL/Day fresh water as per existing CCA AWH-99468. Unit is using 2 KLD

water for domestic and 13 KLD water for industrial purpose as per CCA.

The source of water is GIDC water supply system. After proposed expansion unit will use total

39.86 KLD water (36.86 KLD fresh +3 KLD Recycle).

After proposed expansion, the water consumption for the domestic purpose will be 4 KLD, for

the gardening purpose will be 3.5 KLD and for the industrial purpose will be 32.87 KLD.

A detail of water consumption & water balance diagram is attached as Annexure – 7 of Form I.

1.4 WASTEWATER GENERATION

As per existing CCA, total wastewater generation is 12 KLD (2 KLD for domestic purpose & 10

KLD for industrial purpose).

Total effluent generation after proposed expansion will be 38.04 KLD (22.95 to ETP + + 8 KLD

Nitric acid (30%) generated from Derivatives of Nitro Benzoic Acids will reuse in process of

Derivatives of Benzoic Acids + 4.09 KLD sodium nitrite solution sell to actual end user under

rule 9 permission + 3 KLD of boiler blow down recycle to scrubber water)

1.5 FLUE GAS EMISSION

Existing flue gas emission machineries are Boiler-1 (600 Kg/hr), Boiler-1 (400 Kg/hr) (Stand

by), DG Set (125 KVA) & Boiler-1 (2 TPH).

Unit will install additional Thermic Fluid Heater (10 Lakh Kcal/Hr).

1.6 PROCESS GAS EMISSION

Process gas machineries are reactors.

1.7 HAZARDOUS WASTE MANAGEMENT Hazardous waste generation from the unit is ETP sludge, discarded bag/liners, Used/Spent oil,

spent carbon, spent catalyst and other process residue.

And after proposed expansion, Hazardous waste generation from the unit will be ETP sludge,

discarded bag/liners, Used/Spent oil, spent carbon, spent catalyst, Nitrate (As nitrate nitrogen),

Inorganic Acids -Nitric Acid (30 %), Off specification products, Distillation residue, Scrubber

solution, Sodium Sulphite Solution or sodium bi Sulphite, Dilute HCl (30%), and Spent

Aluminium chloride (20%).



2. INTRODUCTION

2.1 THE PROJECT



Total existing production capacity of the unit is 46 MT/Month. Unit is applying EC for

manufacturing of 175 MT/Month of different types of derivatives of benzoic acids, Chloro

benzoic acid sulfonyl chloride, Nitro phthalic acid, Derivatives of Benzo phenones, Chloro Nitro

Sulphonyl chloride Benzoic acid, & Derivatives of Nitro Benzoic Acids.

Total cost of the project is Rs 4.51 crore.

Plant layout of the unit is attached as ANNEXURE-4.

2.2 PROJECT PROPONENT





Unit falls in category 5 (f).

The promoters have well experienced in this field. Now to meet the market demand promoters

want to increase the production capacity of the unit. The plant boasts of contemporary

infrastructure facilities with advanced machinery and automated processes. They are conscious

of environment protection measures and from the conception stage itself necessary care has been

taken.

The unit believes in sustainable development and equally concern about environment

preservation and pollution control. The unit has already provided adequate Environment

Management System to meet desired norms of effluent discharge as per the statutory recruitment

and also propose to expand its continuous endeavor for the pollution prevention and betterment

of environment.

A vision, a mission and a will to succeed are the basic ingredients in the foundation of the

company. A team of well-qualified engineers and financial experts supports the company. Main

promoters as well as staff of the company have very good industrial as well as business

experience.



QUALITY POLICY

The company’s commitment is to manufacturing of synthetic drug & intermediates. The

company has in house testing facility with modern testing equipments to ascertain the quality of

raw materials as well as finished products. Continued emphasis towards process and technology

up gradation is being done effectively to enrich the product quality. R & D with initiative &

innovative ideas had resulted into excellent performance in respect of quality products.

ENVIRONMENTAL POLICY

The unit is committed to execute all operations, products and services by environmental

protection activities to the extent possible.

As a means of achieving these, the unit pledge to company with the legal & other requirements

to their core and focus on continually improving products, systems & operations

TABLE: 3

CONTACT DEAILS OF PARTNERS

Sr. No.

Name of Partner Present Residential Address

Designation Contact No.

1. Mr. Ketan Parikh 4 Impala House, 36 Viswas Colony, Alkapuri, Baroda - 390-007

Partner 9725053794 2. Mr. Varshal Parikh Partner

The partners of the company have good experience in handling the production management,

financial management.

2.3 NATURE OF PROJECT

Unit falls in category 5 (f).Unit is located in notified industrial area so it a B category project.

2.4 MARKET FEASIBILITY

Proposed expansion shall bring in additional quantity for domestic market. 3.0 PROJECT DESCRIPTION

3.1 TYPE OF PROJECT

The proposed expansion project is for manufacturing of synthetic drug & intermediates.



3.2 PROJECT LOCATION





Unit falls in category 5 (f).

The approximate geographical positioning of the project site is at Longitude: 21°37'12.00"N,

Latitude: 73° 2'26.12"E. The location of the project site can be identified from the location map

shown in Figure no.1 & 2.

The salient features of the project site are presented in below Table-No.4.

TABLE: 4

SALIENT FEATURES OF THE PROJECT SITE

Particulars Details Distance from Site

Villages Ankleshwar 3 KM

Approx. Geographical positioning

Latitude:

Longitude:

21°37'12.00"N

73° 2'26.12"E

Nearest City Ankleshwar

Bharuch

3 KM

15 KM

Nearest Railway line/ Railway station

Ankleshwar 3 KM

Domestic Airport Vadodara 94 KM



FIGURE -1

LOCATION OF THE PROJECT SITE



Ankleshwar



FIGURE: 2 AERIAL VIEW OF THE 10 KM RADIAL PERIPHERY FROM THE PROJECT SITE



3.3 SITE SELECTION

The project proponent did not consider any other alternative site for proposed project.

3.4 NEIGHBORING 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 below:

TABLE: 5

DETAILS OF NEIGHBORING INDUSTRIES

Sr. No.

Name of Industry Address Directions

1. Petroils Industries

Plot No. 6502, GIDC Estate. Ankleshwar - 393002, Gujarat, India.

East

2. Ankleshwar Ammonia Supply Co.

Plot No. 6508, GIDC Estate, Ankleshwar, Gujarat 393002

South

3. Hitesh Chemicals Plot No 6504, GIDC Estate, GIDC, Ankleshwar - 393002

West

4. Main Road -- North

3.5 SIZE OF PROJECT

The unit has proposed to modify effluent treatment plant which will be maintained as per requirements. The break-up of the proposed project cost is given in below Table No. 6.



TABLE: 6 CAPITAL COST PROJECTION Sr. No.

Purpose Existing (Rs. In Lacs)

Proposed (Rs. In Lacs)

Total (Rs. In Lacs)

1. Land 2.36 0 2.36 2. Building 19.70 100 119.70 3. Plant and Machinery 54.38 150 204.38 4. Q.A. Lab set up 10 30 40 5. Environment Protection & Safety a) Effluent treatment Plant 10.33 20 30.33 b) Fire & Safety Equipment (PPE,

fire extinguishers, Ventilation, etc.)

2 10 12

c) Green belt development 1 2 3 d) Air pollution control & Hazardous

waste Management 10 30 40

Total 109.77 342 451.77

3.6 PROCESS TECHNOLOGY

Unit is involving in the manufacturing of Bulk drug & intermediates.

These are characterized for their physicochemical properties. Process details like Process

description, chemical reactions and mass balance for each product is attached as Annexure-6 of

FORM-I. 3.7 RAW MATERIAL

Unit is involving in the manufacturing of Bulk Drug & intermediates.

Detail of Raw material consumption is attached as Annexure-5 of FORM-I.

3.8 RESOURCE REQUIREMENTS

3.8.1 LAND

The total plot area of the unit is 2000 Sq. m. Unit has allotted 463 Sq. m. for green belt

development.

3.8.2 FUEL

For production activity, fuel requirement and Power consumption is as per below table 7 and

table 8.



TABLE: 7

FUEL CONSUMPTION

Sr. No.

Name of Fuel Quantity as per CCA

As per NOC As per Expansion Total

1. Natural Gas 25 Nm3/hr 50 123 Nm3/hr 148 Nm3/hr 2. LDO 15 Lit./hr 00 45 Lit./hr 60 Lit./hr 3. Diesel 35 Lit./hr 00 00 Lit./hr 35 Lit./hr

3.8.3 POWER CONSUMPTION

TABLE: 8

POWER CONSUMPTION

3.8.4 WATER

Existing water and Proposed water consumption is incorporated in Table No:-9

TABLE: 9

WATER CONSUMPTION

Category Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

Remarks

(A) Domestic 2 2 4 (B) Gardening 2 1.5 3.5 (C) Industrial Process 5 3 8 Washing 0 2.86 2.86 Boiler 3 5.5 8.5 Cooling 3 7 10 Others (Scrubber) 00 3 (R) 3 ( R) Boiler blow down Industrial Total 11 21.36 (18.36

fresh + 3 recycle )

32.36 (29.36 fresh + 3 recycle)

Grand Total (A+B+C)

15 24.86 (21.86 fresh + 3 recycle)

39.86 (36.86 fresh + 3 recycle)

Sr. No.

Power Quantity

Quantity (As per proposed expansion)

Total Quantity

1. Electricity 99 kw 200 kw 299 kw



3.8.5 WASTEWATER MANAGEMENT

The category-wise bifurcation of the wastewater generation is given in Table 10.

TABLE: 10

WASTE WATER GENERATION

Category Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

Remarks

(A) Domestic 2 +1.5 3.5 (B) Industrial

Process 5 +15 20 8 KLD Nitric acid (30%) generated from Derivatives of Nitro Benzoic Acids will reuse in process of Derivatives of Benzoic Acids + 0.733 KLD of aluminum chloride solution to ETP + 11.27 KLD process effluent to ETP

scrubber 00 +5.18 5.18 4.09 KLD sodium nitrite solution sell to actual end user under rule 9 permission + 0.69 KLD sodium bi sulfite solution treated in ETP+ 0.40 KLD of dilute HCl to ETP

Washing 0 +2.86 2.86 To ETP Boiler 2.5 +0.50 (R ) 3 (R ) Recycle in scrubber Cooling 2.5 +1 3.5 To ETP Total Industrial waste water

10 +24.54 34.54 19.45 KLD to ETP + 8 KLD Nitric acid (30%) generated from Derivatives of Nitro Benzoic Acids will reuse in process of Derivatives of Benzoic Acids + 4.09 KLD sodium nitrite solution sell to actual end user under rule 9 permission + 3 KLD of boiler blow down recycle to scrubber water

Total (Industrial + Domestic)

12 +26.04 38.04 22.95 to ETP + + 8 KLD Nitric acid (30%) generated from Derivatives of Nitro Benzoic Acids will reuse in process of Derivatives of Benzoic Acids + 4.09 KLD sodium nitrite solution sell to actual end user under rule 9 permission + 3 KLD of boiler blow down recycle to scrubber water



3.8.5.1 WASTEWATER CHARACTERISTICS

Existing & proposed effluent characteristic before treatment and after treatment in ETP is

covered in Annexure-7 of FORM I.

3.8.5.2 WASTEWATER TREATMENT & DISPOSAL

A detail of existing & proposed effluent treatment plant (ETP) is covered in Annexure-7 of

FORM I.

3.9 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.

3.9.1 GASEOUS EMISSIONS & CONTROL

3.9.1.1 FLUE GAS EMISSION

Existing flue gas emission and proposed flue gas emission is mentioned in Table No: 11.

TABLE: 11

FLUE GAS EMISSION

As Per existing CCA AWH-89231 Sr. No

Stack attached to

Fuel Total Fuel Consumption

Stack Height in meter

APCM Pollutants Permissible Limit

1 Boiler-1 (600 Kg/hr)

Natural gas or LDO

23 Nm3/Hr/ 15 Lit/Hr

11 Adequate stack height & low NOx burner

Particulate Matter, SO2, NOx

150mg/Nm3 100ppm 50ppm

2 Boiler-1 (400 Kg/hr) (Stand By)

Natural gas or LDO

25 Nm3/Hr /15 Lit/Hr

3 DG Set (125 KVA)

Diesel 35 L/Hr 9 ---- Particulate Matter, SO2, NOx

150 mg/Nm3 100 ppm 50 ppm

NOC Amendment obtained vide CTE No 91191 1. Boiler-1

(2 TPH) Natural gas or LDO

50 Nm3/Hr/ 15 Lit/Hr

11 Adequate stack

Particulate Matter, SO2,

150mg/Nm3 100ppm



height & low NOx burner

NOx 50ppm

2. DG Set (125 KVA)

Diesel 35 L/Hr 9 ---- Particulate Matter, SO2, NOx


Unit had obtained CTE amendment for increasing boiler capacity & fuel. Boiler having capacity of 600 Kg/Hr & 400 Kg/hr will be replacing by boiler having capacity of 2TPH. And Natural gas consumption will be increasing from 25 Nm3/Hr to 50 Nm3/Hr.

DETAILS OF FLUE GAS EMISSION (AFTER PROPOSED EXPANSION) As per after proposed expansion

Sr. No

Stack attached to

Fuel Total Fuel Consumption


APCM Pollutants Permissible Limit

1. Boiler-1 (2 TPH)

Natural gas or LDO

50 Nm3/Hr OR 15 Lit/Hr


Particulate Matter, SO2, NOx


2. DG Set (125 KVA)

Diesel 35 L/Hr 9 ---- Particulate Matter, SO2, Nox


3. Boiler-1 (600 Kg/hr)

Natural gas or LDO

23 Nm3/Hr OR 15 Lit/Hr


Particulate Matter, SO2, Nox


4. Boiler-1 (400 Kg/hr) (Stand By)

Natural gas or LDO

25 Nm3/Hr /15 Lit/Hr


5. Thermic Fluid

Natural Gas or

50 Nm3/Hr Or 15 Lit/Hr

11 From G.L

Adequate stack

Particulate Matter,

150 mg/Nm3 100 ppm



Heater (10 Lakh Kcal/Hr)

LDO height & low NOx burner

SO2, NOx

50 ppm

3.9.1.2 PROCESS EMISSIONS Existing process gas emission and proposed flue gas emission is mentioned in Table No: 12. TABLE:-12 PROCESS GAS EMISSION As Per existing CCA AWH-89231 Sr. No.

Stack attached to


APCM Probable Pollutants

Permissible Limit

1 Reaction Vessels (S.S. Reactor)

15 m water scrubber followed by Alkali Scrubber

NOx 25 mg/Nm3

2 Reaction Vessels (GL reactor)

water scrubber followed by Alkali Scrubber

HBr 30 mg/Nm3

3 Reaction Vessel (SS Autoclave)

water scrubber followed by Alkali Scrubber

NOx 25 mg/Nm3

PROCESS EMISSIONS (AFTER PROPOSED EXPANSION) AFTER PROPOSED EXPANSION Sr. No.

Stack attached to



Permissible Limit

1 Reaction Vessels (S.S. Reactor)

15 m water scrubber followed by Alkali Scrubber,

NOx 25 mg/Nm3

2 Reaction Vessels (GL reactor)

water scrubber followed by Alkali Scrubber,

SO2, HCl, NOx

40 mg/Nm3

20 mg/Nm3

25 mg/Nm3



AFTER PROPOSED EXPANSION Sr. No.

Stack attached to



Permissible Limit



NOx 25 mg/Nm3



NOx 25 mg/Nm3



NOx 25 mg/Nm3

3.9.2 HAZARDOUS WASTE MANAGEMENT The following types of hazardous wastes are being generated during the operational activities.

All the wastes are being stored separately in a designated storage area. The details of hazardous

waste are below given Table 13.



TABLE 13

DETAILS OF HAZARDOUS WASTE

Sr. No.

Name of Waste Specific

Source

of

generati

on

(Name of the Activity, Product etc.)

Waste category Schedule

Generation MT per Year Mode of Disposal

Quantity As per CCA

Expansion Total after Proposed Change

1. Empty barrels/Containers/liners contaminated with hazardous chemicals waste

Raw material Storage area

33.1 6.08 +20 26.08 Collection, Storage, Decontamination, Transport and Disposal by selling to authorized vendors / recycle or reuse or send back to suppliers.

2. Chemical sludge from waste water treatment

Effluent treatment plant

35.3 70 MT +180 250 Collection, Storage, Transport and Disposal at common TSDF facility to BEIL, Ankleshwar

3. Spent/ used oil

Maintenance Area

5.1 0.01 KL/year

+0.04 0.05 Collection, Storage, Transport and Disposal by selling to registered recyclers/re-refiners/ reuse in plant & machinery as lubricant.

4. Nitrate (As nitrate nitrogen)

Derrivatives of benzoic acid & Chloro Nitro Sulphonyl chloride Benzoic acid

A12 240 MT +1235 MT 1475 MT Sodium Nitrite solution(20%): Collection, Storage, Transport and 20% Sodium Nitrite Solution disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste or treatment along with industrial effluent



5. Inorganic Acids –Spent Nitric Acid

Derivatives of Nitro Benzoic Acids

B15 120 MT +2760 MT 2880 MT Collection, Storage, Transport and 2880 KL/Year 30% Dilute Nitric acid will reuse in the manufacturing process of derivatives of benzoic acid

6. Off specification products

Di nitro naphthalene & if any product not match with customer requirement

-- 00 +82 82 Collection, Storage, Transportation, disposal at Co-Processing or Incineration Facility site.

7. Distillation residue

Derivatives of Nitro Benzoicacid & Di nitro Naphthalene

-- 00 12 12 Collection, Storage, Transportation, disposal at Co-Processing or Incineration Facility site.

8. Sodium Sulphite Solution or sodium bi Sulphite

Derivatives of Nitro Benzoic acid & Derivatives of Benzo phenones

-- 00 +250 250 Collection, Storage, treated in ETP

9. Dilute HCl (30%) 2,4 Di chloro Phenoxy acetyl choride, Derivatives of Benzo phenone




10. Spent Aluminium chloride (20%)

Derivatives of Benzo phenone


3.9.3 NOISE CONTROL & ODOUR

The major noise generating installation is the D.G. Set. Unit has installed it in a closed room and

provided acoustic enclosure around it. Unit has also provided ear plugs to the operating person of

Boiler room.

Unit is following below steps to Noise control and Odour.

Raw-material feeding is being carried out by pumps.

All reactions are being taken in closed reactor system.

Roof top ventilation is installed in the entire plant area.

Regular monitoring of piping and fittings is carried out to prevent the leakages.

3.9.4 STORAGE, HANDLING AND TRANSPORT OF HAZARDOUS CHEMICALS

The storage and mode of transport of chemicals are being done as per detailed MSDS and

chemical hazards guide (NIOSH) for 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.

3.9.5 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,

Moreover transport activity is being done through drums, so there is a manual loading and

unloading and no unloading through pipe at the site. Hence, the risk of static charge generation

during transfer of such chemicals is not significant.

3.9.6 MAN POWER

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

activities will be employed from the local area.



TABLE NO:-14

MAN POWER REQUIREMENT

Phase of project Type of labor Existing Proposed No. of workers

(Proposed Scenario)

During construction Contractual 0 Approx. 10 10

During commissioning Contractual 0 Approx. 10 10

During operations Managerial 2 2 4

Skilled 6 6 12

Un-skilled 20 15 35

Total during Operation 28 43 71

4.0 SITE ANALYSIS

4.1 CONNECTIVITY

Ankleshwar is known for Pigment and Pharmaceutical Industry. Ankleshwar is connected

by Indian National Highway 8 (Mumbai to New Delhi) and by the Western Railway Division

of Indian Railways. The railway division 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 railway station is centrally located at the intersection of NH8 & Station Road.

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

section).Development projects of Ankleshwar Airport & City Bus are in last stage.

4.2 LAND USE AND LAND OWNERSHIP







4.3 EXISTING LAND USE





4.4 EXISTING INFRASTRUCTURE

The plant is located in a well-developed industrial zone, which has all essential facilities such as

internal roads, arrangement for supply of water and power to industries, effluent disposal

facilities, gas etc.

The proposed project is relatively small in size and will be employing some skilled and unskilled

people. First preference will be given to local people, so there will be no change in population

pattern due to the proposed project.

4.5 SOIL CLASSIFICATION

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

Based on the meteorological data, wind rose have been prepared for the summer season period

between the March-2017 to May-2017. The wind rose diagram prepared from same data is

shown at Figure 3, Figure 3.1.

TABLE: 15

METEOROLOGICAL DATA

Month Temperature(oC) Humidity (%) Rain fall (mm) Maximum Minimum Maximum Minimum Maximum Minimum

March-2017 39 25 79 4 00 00 April-2017 40 26 76 3 00 00 May-2017 42 28 72 3 00 00



FIGURE: 3

WIND ROSE DIAGARM FOR PERIOD OF MARCH 2017 TO MAY 2017



FIGURE: 3.1

WIND CLASS FREQUENCY DISRTIBUTION

Observation: It observed that wind is blowing mainly towards the SW direction from NE.

Average wind speed was 2.38 m/s.

4.7 SOCIAL INFRASTRUCTURE

As of 2011 India census, Ankleshwar had a population of 140,839. Males constitute 53% of the

population and females 47%. 13% of the population is under 6 years of age.

5.0 PLANNING BRIEF

5.1 PLANNING CONCEPT:

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

Plants. Government agencies provide many basic facilities like uninterrupted water supply,

power and road network.



5.2 POPULATION PROJECTION.

As of 2011 India census, Ankleshwar had a population of 140,839. Males constitute 53% of the

population and females 47%. 13% of the population is under 6 years of age.

5.3 LAND USE PLANNING

The names of prominent industries are shown in table no: 16

TABLE: 16

NAME OF SOME PROMINENT INDUSTRIES

Sr. No.

Name of Industry Address Directions Distance (meter)

1. M/s. Crop Science Pvt. Ltd

Plot no. 5165, GIDC Ankleshwar District : Bharuch

S 50

2. M/s. Geeta Chemical

Plot no– 4906/B, GIDC Estate, Ankleshwar, Dist. Bharuch, Gujarat

N 100

3. M/s. Oza Industries Plot No:5179, Gidc Estate, GIDC, Ankleshwar - 393001

E 100

4. M/s. S K Finechem Plot No:5177, Gidc Estate, GIDC, Ankleshwar - 393001

W 50

6.0 PROPOSED INFRASTRUCTURE

6.1 PROCESSING AREA

The process area is covered plant area, raw material storage area, hazardous waste storage area,

workshop and utilities.

6.2 NON PROCESSING AREA

The non process area is covered Admin Building, toilet blocks, change room and security cabin.

6.3 GREEN BELT AREA





The total plot area of the unit is 2000 sq meter in which 463 sq. meter will be total green belt

area.



6.4 SOCIAL INFRASTRUCTURE

The availability of basic amenities is covered as under:

Training & Education: All the employees are being trained and educated periodically about

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

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

activities.

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.

Drinking water: Unit has provided Aqua Guard/R.O at different places to provide purified

water for drinking purpose.

Transportation: The unit is providing basic transportation facility to workers.

Telegraph & Post: Unit has all the facilities like telephone, fax and internet for the

employees.

6.5 CONNECTIVITY

This industrial estate is well connected to Ahmadabad/Mumbai/Vadodara through the

Ankleshwar. Rail services and Road services are available in Ankleshwar.

6.6 DRINKING WATER MANAGEMENT

Average daily water consumption of unit is 4 KL/day for domestic purpose. GIDC water is a

source of domestic water.

6.7 INDUSTRIAL WASTE MANAGEMENT

The hazardous waste management and disposal is shown in table 13.

6.8 SOLID WASTE MANAGEMENT

The Solid waste management and disposal is shown in table 13.

6.9 SOURCE OF POWER

DGVCL is a main source of Power.

7.0 REHABILITATION AND RESETTLEMENT(R &R) PLAN

The proposed project is located in GIDC Estate, Ankleshwar. There will be no any human

settlement affected by proposed project. So, there is no requirement of any R & R Plan.



8.0 PROJECT SCHEDULE & COST ESTIMATES

8.1 PROJECT IMPLEMENTATION SCHEDULE

The details of project Implementation Schedule is given in below table.

TABLE: 17

PROJECT IMPLEMENTATION SCHEDULE

Project implementation schedule after getting NOC from GPCB Sr. No. Activity Required Period 1. Civil work Immediately after getting NOC 2. Procurement of machinery 1 month after getting NOC

3. Eraction & installation of machinery

Immediately after competition of activity no.2

4. Trial of machinery & equipment

Within 1 months after competition of activity no.3

5. Commercial activity 1 months after competition of activity no.4 8.2 ESTIMATED PROJECT COST

The details of Capital cost projection are given in table no. 6.

9.0 ANALYSIS OF PROPOSAL

First preference will be given to local people for employment and Company will also try to

provide indirect employment opportunities by availing local contract services during

transportation and 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 villages for their welfare and upliftment.

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