the 497 th - gujarat state portal minutes of the 497th i.pdfpage 4 of 167 497 th meeting of...

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497thmeeting of SEAC-Gujarat, Dated 16.04.2019

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The 497th meeting of the StateLevelExpertAppraisalCommittee (SEAC) was held on 16thApril

2019 at Gujarat Pollution Control Board, Sector 10-A, Gandhinagar. Following members

attended the meeting:

1. Shri Dinesh Misra, Chairman, SEAC

2. Shri S. C. Srivastav, Vice Chairman, SEAC

3. Shri R. J. Shah, Member, SEAC

4. Shri V. N. Patel, Member, SEAC

5. Dr. V. K. Jain, Member, SEAC

The agenda of TOR/Screening & Scoping and Appraisal cases were taken up. The applicants made

presentations on the activities to be carried out along with other details furnished in the Form-1, PFR

and other reports.

3 SIA/GJ/IND2/28287/2018 M/s. Vibfast Pigments (P) Ltd

Plot No- C-1,91/6, Phase I, GIDC Estate, Vatva, Dist.: Ahmedabad

Appraisal

Category of the unit: 5(f)

Project status: New

• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/28287/2018dated

26/03/19 for obtaining Environmental Clearance.

• SEIAA issued TOR to PP vide their letter dated 30/11/2018.

• Project proponent has submitted EIA Report prepared by Satva Environ Consultancy, Ahmedabad

based on the TOR issued by SEIAA.

• This is a new unit proposes manufacturing of Pigments as tabulated below:

Sr.

No. Name of the Products

CAS

NO

Quantity

MT/Month

End-use of

products

1.

Fluorescent Pigments- HTPA Series

26659-15-4

75

MT/Month

Raw

material of

plastic

industries,

textile,

fabrics etc

Fluorescent Pigments- HTPA Series (Lemon Yellow)

Fluorescent Pigments – HTPA Series Green

Fluorescent Pigments-HTPA Series Pink

Fluorescent Pigments-HTPA Series Orange-R

Fluorescent Pigments-HTPA Series Orange-Y

Fluorescent Pigments – HTPA Series Blue

Fluorescent Pigments-HTPA Series Chrome

Fluorescent Pigments – HTPA Series Magenta

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Fluorescent Pigments – HTPA Series Violet

Fluorescent Pigments – HTPA Series Near Red

2

Fluorescent Pigments – I Series

26659-15-4

Fluorescent Pigments – I Series Lemon Yellow

Fluorescent Pigments – I Series Yellow 7000

Fluorescent Pigments – I Series Green

Fluorescent Pigments – I Series Orange

Fluorescent Pigments – I Series Pink (B)

Fluorescent Pigments – I Series Pink R

Fluorescent Pigments – I Series Chrome(Y)

Fluorescent Pigments – I Series Red Orange

Fluorescent Pigments – I Series Magenta (BF)

Fluorescent Pigments – I Series Magenta (B)

Fluorescent Pigments – I Series Magenta (R)

3.

Fluorescent Pigments – IT Series

26659-15-4

Fluorescent Pigments – IT Series Lemon Yellow

Fluorescent Pigments – IT Series Yellow

Fluorescent Pigments – IT Series Yellow 7000T

Fluorescent Pigments –IT Series Lemon Yellow 501 (S)

Fluorescent Pigments – IT Series Saturn Yellow

Fluorescent Pigments – IT Series Green

Fluorescent Pigments – It Series Green (Y)

Fluorescent Pigments – IT Series Orange

Fluorescent Pigments – IT Series Red Orange IT

Fluorescent Pigments – IT Series Pink (B)

Fluorescent Pigments – IT Series Pink (R)

Fluorescent Pigments – IT Series Chrome

Fluorescent Pigments – IT Series Yellow Chrome(Y)

Fluorescent Pigments – IT Series Magenta (B)

4.

Fluorescent Pigments – IX Series

26659-15-4

Fluorescent Pigments – IX Series Lemon Yellow

Fluorescent Pigments – IX Series Saturn Yellow

Fluorescent Pigments – IX Series Yellow FBG

Fluorescent Pigments – IX Series Green FBG

Fluorescent Pigments – IX Series Green

Fluorescent Pigments – IX Series Orange

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Fluorescent Pigments – IX Series Orange R

Fluorescent Pigments – IX Series Red

Fluorescent Pigments – IX Series Pink (B)

Fluorescent Pigments – IX Series Pink (R)

Fluorescent Pigments – IX Series Chrome

Fluorescent Pigments – IX Series Chrome Y

Fluorescent Pigments – IX Series Magenta

Fluorescent Pigments – IX Series Magenta (R)

Fluorescent Pigments – IX Series Magenta (B)

Fluorescent Pigments – IX Series Royal Blue

Fluorescent Pigments – IX Series Peacock Blue

Fluorescent Pigments – IX Series Violet

Fluorescent Pigments – IX Series Red Violet

Fluorescent Pigments – IX Series Green (Y)

Fluorescent Pigments – IX Series Green 8000

5.

Fluorescent Pigments – IX – T

26659-15-4

Fluorescent Pigments – IX – T series Lemon Yellow

Fluorescent Pigments – IX – T Series Yellow

Fluorescent Pigments – IX – T Series Green

Fluorescent Pigments – IX – T Series Green (Y)

Fluorescent Pigments – IX- T Series Orange – R

Fluorescent Pigments – IX – T Series Orange Y

Fluorescent Pigments –IX-T Series Orange

Fluorescent Pigments – IX – T Series Red

Fluorescent Pigments – IX - T Series Pink

Fluorescent Pigments – IX – T Series Pink (B)

Fluorescent Pigments – IX T Series Pink (R)

Fluorescent Pigments – IX – T Series Chrome

Fluorescent Pigments – IX – T Series Chrome (Y)

Fluorescent Pigments – IX – T Series Red Orange

Fluorescent Pigments – IX – T Series Magenta R

Fluorescent Pigments – IX – T Series Magenta

Fluorescent Pigments – IX – T Series Royal Blue

Fluorescent Pigments – IX – T Series Peacock Blue

Fluorescent Pigments – IX – T Series Violet

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Fluorescent Pigments – IX – T Series Red Violet

Total Production Quantity 75

MT/Month

• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006.

• PP was called for presentation in the SEAC meeting dated 16/04/2019.

• Salient Features of the project including Water, Air and Hazardous waste management:

Sr. No.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 2.0 Crores

B Total Plot area ( sq. meter) 697 Sq. m.

Green belt area( sq. meter) 50 Sq. m.

C Employment generation 15

D Water

i

Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)

GIDC Water Supply

Status of permission from the concern authority.

ii Water consumption (KLD)

Sr No

Category Water Consumption in KL/Day

1. Domestic Purpose 1.0

2. INDUSTRIAL

Process 0.0

Total water Consumption ( Domestic) 1.0

Total water Consumption (Industrial ) 0.0

Note: There is no water use in Process hence total industrial water consumption will be Nil.

1) Total water requirement for the project: 1.0 KLD

2) Quantity to be recycle: Nil.

3) Total fresh water requirement : 1.0 KLD

iii Waste water generation (KLD)

Sr No Category Wastewater Generation in

KL/Day

1. Domestic Purpose 0.8

2.

INDUSTRIAL

Process 0.0

Total Wastewater generation (Domestic) 0.8

Total Wastewater generation (Industrial) 0.0

Note: There is no wastewater generation from the Industrial Activity.

iv

Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.

Existing & Proposed Effluent Treatment Plant

• Not applicable as there is no generation of wastewater from manufacturing process hence there is no need of any Effluent Treatment Plant

497

Total Water Consumption

Domestic and Gardening

1.0 KLD

Sewage

0.8 KLD

Treatment scheme including segregation at source.

� • Not applicable as there is no generation of wastewater from manufacturing

process hence there is no need of any Effluent Treatment Plant

Note: (In case of CETP discharge) :

Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and

Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP

� Not applicable

Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):

� there is no generation of wastewater from manufacturing process hence there is no

need of any Effluent Treatment Plant

v

Mode of Disposal & Final meeting point

Domestic:

The generated sewage

tank

Industrial:

Not applicable, as there is no generation of wastewater from manufacturing

process.

vi

In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility

- Not Applicable

Membership of Common facility (CF)

- Not Applicable

vii Simplified water balance diagram with reuse / recycle of waste water:

vii Reuse/Recycle details (KLD) [Source of reuse & application area]

- Nil.

E Air

i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.


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1.0 KLD

Domestic and Process

NIL KLD

Wastewater

Nil KLD


Not applicable as there is no generation of wastewater from manufacturing

process hence there is no need of any Effluent Treatment Plant


water keeping in view direction under section 18 (1) (b) of the Water (Prevention and

Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.


no generation of wastewater from manufacturing process hence there is no

need of any Effluent Treatment Plant


The generated sewage @0.8 KLD will be disposed through soak pit/septic


process.

In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.


Simplified water balance diagram with reuse / recycle of waste water:

Reuse/Recycle details (KLD) [Source of reuse & application area]

No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

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Not applicable as there is no generation of wastewater from manufacturing

water keeping in view direction under section 18 (1) (b) of the Water (Prevention and

no generation of wastewater from manufacturing process hence there is no

will be disposed through soak pit/septic



Simplified water balance diagram with reuse / recycle of waste water:


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Existing & Proposed

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter

)

Type of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

Remarks

1 D. G. Set

(65 KVA) 5.00 HSD 10 L/hr

PM

SO2

NOx

Acoustic

Enclosure

Proposed

2

Hot Air

Generator

(0.5 Lac

Kcal/hr)

5.0 Natural

Gas

100

SCM/Day PM

Adequate

Stack

height

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) Existing & Proposed

Sr.

no.

Source of

emission

With Capacity

Stack

Height

(meter)

Type of

emissions i.e.

Air Pollutants

Air Pollution

Control

Measures

(APCM)

Remarks

1 Spray Dryer

20 LPH (Lab

Scale)

5.00 PM Adequate Stack

height Proposed

2 Pulveriser (6

Nos) 11.0 PM Dust Collector Proposed

iii Fugitive emission details with its mitigation measures.

� The entire manufacturing activities will be carried out in the closed reactors and regular

checking and maintenance of reactors will be carried out to avoid any leakages.

� The tank vents will be equipped with either a carbon filter or an oil trap to prevent water

vapor from entering the tank as it breathes.

� All the motors of pumps for the handling of hazardous chemicals will be flame proof and

provided with suitable mechanical seal with stand-by arrangement

� Control of all parameters on a continuous basis will be done by adequate control valves,

pressure release valves and safety valves etc.

� All the flange joints of the pipe lines will be covered with flange guards.

� All the raw materials will be stored in isolated storage area and containers tightly closed.

� There will also be provision of adequate ventilation system in process plant and

hazardous chemical storage area.

� A regular preventive maintenance will be planned to replace or rectify all gaskets, joints

etc.

� The unit will also develop green belt within the factory premises to control the fugitive emission from spreading into surrounding environment

F Hazardous waste

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(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Existing & Proposed

I

Sr.

no.

Type/Name of

Hazardous

waste

Source of

generation

Category and

Schedule as

per HW Rules.

Quantity

(MT/Annum

)

Disposal Method

1 Used Oil Plant

Machinery 5.1

0.06

MT/year

Collection, storage,

Reuse within

premises.

2. Discarded Container

Material Storage

33.1 60 MT/ year

Collection storage and disposal by

sending to actual users/recyclers

ii Membership details of TSDF, CHWIF etc. (For HW management) Not Applicable

iii Details of Non-Hazardous waste & its disposal(MSW and others) Not Applicable

G Solvent management, VOC emissions etc.

i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents

- Ortho Toluene - Para Toluene

ii VOC emission sources and its mitigation measures

� Sources of fugitive emissions include storage of chemicals, solvents storage, loading

and unloading section, raw material handling and, hazardous waste storage area

Measures :

� The fugitive emissions in terms of handling losses will get reduced by proper storage

and handling.

� Hazardous chemicals will be stored as per standard criteria.

� Periodically monitoring will be carried out as per the post project monitoring plan.

� Proper ventilation in storage & production rea shall be ensured

� All materials must be stored in suitable packing to prevent contamination of air.

� Enclosed system & efficient procedures for materials charging shall be ensured.

� Procedures for start-up shut down, operation & maintenance procedures shall be

established & maintained.

� The coverage of greenbelt around the plant also acts as natural barrier to stop carrying of dust along with the wind current..

H � Details regarding storage of Hazardous chemicals

Storage details Name of major Hazardous chemicals Remarks

Storage tanks NIL

Drum/Barrel storage Acetic Acid

Acrylic acid

Fluorescent red 112

Melamine

Plasticizer

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� Applicability of PESO : Not Applicable

• During the meeting dated 16/04/2019, technical presentation made by the Project proponent.

• During the meeting, the project was appraised based on the information furnished in the EIA Report

and details presented during the meeting.

• The baseline environmental quality has been assessed for various components of the environment

viz. air, noise, water, biological and socioeconomic aspect for the study area of 10 km radial

distance from project site for the period March’ 18 to May’ 18. Ambient Air Quality monitoring was

carried out for PM2.5, PM10, SO2, NOx and VOCat Nine locations, including the project site. Values

conform to the prescribed standards for Ambient Air Quality. The incremental Ground Level

Concentration (GLC) has been computed usingAERMOD View (Lakes Environment Software)

• The resultant concentrations are within the NAAQS. The modeling study proved that the air

emissions from the proposed plant would not affect the ambient air quality of the region in any

significant manner. The ambient air quality around the proposed project site will remain within the

National Ambient Air Quality Standards (NAAQS).

• Risk assessment including prediction of the worst-case scenario and maximum credible accident

scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-

Site Emergency Plan has been covered in the RA report.

• Committee noted that this proposal is for new Pigment manufacturing unit at GIDC,Vatva.

• There will be no water consumption for industrial purpose. There will be no industrial effluent

generation as well as discharge from the unit.

• Natural and diesel will be used as fuel. Dust collector will be provided with pulveriser as APCM.

• PP has addressed hazardous waste management.

• Committee deliberated CER, EMP and baseline data. Compliance of ToR is found satisfactory.

After detailed discussion, committee decided to recommend the project to SEIAA Gujarat for

grant of Environmental Clearance with following specific conditions.

1. There shall be no water consumption for industrial purpose. Unit shall not carry out washing

activity. There shall be no industrial effluent generation as well discharge from the unit.Hence,

unit shall strictly adhere to Zero Liquid Discharge (ZLD) condition.

2. Unit shall strictly adhere to notarized undertaking dated 08.04.2019 regarding no industrial

effluent generation as well as discharge.

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3. There shall be no drainage connection within premises.

4. All adequate measures shall be taken to prevent soil and ground water contamination.

4 SIA/GJ/IND2/32786/2018 M/s. Mundra Solar Limited

180/P, Within Notified APSEZ, Mundra, Tal.: Mundra, Dist.: Kutch.

Appraisal

Category of the unit: 3(a)

Project status: New




• Project proponent has submitted EIA Report prepared by Wolchem India Limited based on the TOR

issued by SEIAA.

• This is a new unit proposes for manufacturing of Poly Silicon as tabulated below:

Sr.

No.

Name of the

Products

CAS no. /CI no. Quantity

MT/Month

End-use of products

1 Poly Silicon

- 2583.33 For use in manufacturing of

Solar cell and Modules

• The project falls underCategory B of project activity3(a)asper the schedule of EIA Notification 2006.



Sr.

no.

Particulars Details

A

A Total cost of Proposed Project (Rs. in Crores): 7,381 Crores

B Total Plot area ( sq. meter) 5,70,900 Sq. m.

Green belt area ( sq. meter) 1,89,000 Sq. m.

C Employment generation 1,146 nos.

D Water

i

Source of Water Supply

(GIDC Bore well, Surface water, Tanker supply etc...)

From APSEZ (Group Company)

letter no.

APSEZL/EMC/14072015 dated

14 Jul 2015

Status of permission from the concern authority. APSEZ


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Category Quantity

KLD

Remarks

(A) Domestic 60

(B) Gardening 48 Recycled Water

(C) Industrial

Process 11,000

Washing

Boiler

Cooling 8000

Others 940

Industrial Total 19,940

Total (A + B + C) 20,048

1) Total water requirement for the project: 20,000 KLD

2) Quantity to be recycled: 48 KLD

3) Total fresh water requirement: 20,000 KLD


Category Waste water

KLD

Remarks

(A) Domestic 48 STP treated water will

be used for Gardening

(B) Industrial

Process 9,750

Washing

Boiler

Cooling 2,500

Others

Total Industrial

waste water

12,250

Total [A + B] 12,298

iv Treatment facility within premises with capacity

[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.

� Refer EIA Report Details are given in section 2.10 on page no. 48 & 53


� Refer EIA Report Details are given in section 2.10 on page no.48 & 53


Management of waste water keeping in view direction under section 18 (1) (b) of the

Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding

compliance of CETP.

� Not Applicable

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� Not Applicable

� Treated water will be discharge through outfall channel of APSEZ.

v Mode of Disposal & Final meeting point: Into Sea

Domestic:

Recycled Water will be used in gardening, plantation, Greenbelt

development & miscellaneous use

Industrial: Water will be discharge through outfall channel of APSEZ

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc.

Name of CF

� Not Applicable

Membership of Common facility (CF) - Not Applicable (For waste water treatment)

vii Simplified water balance diagram with reuse / recycle of waste water

Refer to EIA Report

viii Reuse/Recycle details (KLD)

Total reuse 48 KLD

Source of waste

water for reuse

with quantity in

KLD (From where it

is coming)

Application area

with quantity in KLD

(Where it is used)

Characteristics

of waste water

to be reused

(COD, BOD, TDS

etc.)

Remarks

regarding

feasibility

to reuse i.e.

From STP.

60 KLD STP is

proposed, 48 KLD

treated water will be

generated.

48 KLD will be used in

gardening, plantation,

Greenbelt

development &

miscellaneous use.

As per GPCB /

CPCB Norms.

E Air

i Flue gas emission details


Sr.

no.

Source of

emission

With Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity of

Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1 Process Stack 30 Natural

Gas

1,64,00,000

Cubic

meter per

year

PM2.5,

PM10,

SO2, NOx

Details in EIA

report Section

2.12.1 & 4.3.2

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2 DG Set 30 HSD 25 Lt/hr

PM2.5,

PM10,

SO2, NOx

Details in EIA

report Section

2.12.1 & 4.3.2

ii Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)

----

iii Fugitive emission details with its mitigation measures: As below:

• All material storage tanks will be provided with vent condensers having chilled water and brine circulation.

• Mechanical seals will be provided for all the reactors for improving emission control measures.

• To prevent Fugitive emission, various steps will be taken like regular sprinkling of water and paved road. The fugitive emissions from solvents and chemicals will be minimum as all the chemicals and solvents will be handled with closed operations and transfer

F Hazardous wastes

(as per the Hazardous and Other Wastes (Management and Transboundary Movement)

Rules 2016.

i Sr.

no.

Type/Name of

Hazardous

waste

Specific Source

of generation

(Name of the

Activity, Product

etc.)

Category and Schedule as per HW Rules.

Quantity

(MT/Annum)

Management of HW

1 Chemical Sludge Waste/Effluent water Treatment

35.3 1800 TSDF

2 Used Oil Oiling in Compressors and DG Set

5.1 20 KL/Year ThroughRegistered Recycler

3 Oil Soaked cotton waste and residue

Used for shop floor/maintenance

33.2

1.5 TSDF

4 Empty Barrel/ Containers

Consumables Supply

33.1 12 ThroughRegistered Recycler

5 Graphite Parts CVD Reactors B2010 3.0 ThroughRegistered Recycler/TSDF

6 Waste Silicon Reactors B1010 90 ThroughRegistered Recycler/TSDF

7 Spent Activated Carbon

H2 Plant A4160 0.25 TSDF

8 Filters Chlorosilane Purification

36.2 0.25 TSDF

9 Jumbo Gunny Bag

MG-Si Supply 33.1 100 ThroughRegistered Recycler/TSDF

10 E waste - A1180 2.0 ThroughRegistered Recycler

ii Membership details of TSDF, CHWIF etc. TSDF Membership will be

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(For HW management- obtained after CTE.

iii Details of Non-Hazardous waste & its disposal (MSW and others)

Refer Section 4.5 on page no. 134

G Solvent management- VOC emissions etc.

Refer EIA Report. Details provided in section 4.3 on page no. 125

i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. -

Details in Table Format

� Refer EIA Report. Details provided in section 4.3 on page no. 125


� Refer EIA Report. Details provided in section 4.3 on page no. 125



Tonner Chlorine (Cl2) Gas

IBC Hydrochloric Acid (HCL)

Pipeline Hydrogen Gas (H2) In-House Manufacturing

SS Tank Tri Chlorosilane

(SiHCL3)

Produced as part of the Poly

Si process cycle by

reaction of HCl with MG‐Si

SS Tank Silicon Tetrachloride (SiCl4) Produced as part of the Poly

Si process

Jumbo Bags Metallurgical

Grade Silicon

(MG-Si)

Pipeline Nitrogen (N2) Gas In-House Manufacturing -

Two tanks of 200 m3

capacity each

• This proposal was considered in the SEAC meeting dated 16.04.2019. During meeting, Committee

deliberated on source of raw material, product profile, generation of spent HCl & its management,

waste water generation & its management, HW management matrix, source & quantification of HW

generation, safety precautions for storage & handling of H2 gas, baseline details, EMP, CER etc.

• During discussion, Committee observed the following points:

� Manufacturing process including mass/material balance with sources and are not properly

addressed.

� Wastes generated in the form of liquid, gaseous & solid state are not addressed separately.

� Spent HCl generation and its sound management is not submitted.

� Justification for use of salt water for neutralization of effluent is not addressed.

� Flue gas emission details & its management is not adequate.

� Process gaseous emission details with its mitigation measures & final disposal of bleed liquor

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not addressed.

� Hazardous waste matrix is not properly addressed in accordance with the HWM Rules, 2016.

� Details of EMP-CER with break-up is not submitted.

� Project specific safety details are not addressed.

� Chemical reaction and relevant details not covered in EIA report.

� Composition of waste generated from the different sources and its management as per

prevailing laws/rules &regulations is not addressed properly.

During SEAC meeting, Committee noted that most of the ToR pertaining to the above mentioned points

are not addressed properly in EIA report as well as in presentation. Committee concluded that PP is not

well prepared and compliance of TOR is not satisfactory.

In view of the above, Committee unanimously decided to consider the proposal after submission

of the following details:

1. Redress ToR no. 8, 10, 16,17,19,23,26,27, 28,37, 40,41,44,46,50 and incorporate it in EIA.

2. Compliance of MoEF&CC’s OM dated 01/05/2018 regarding “Corporate Environment

Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be

made as per MoEF&CC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities

therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP

report.

3. Justification of quantity of ETP sludge against treatment of industrial effluent.

4. Sources of process gas emission, process stack and its APCM.

5. Sound management of bleed liquor (exhausted scrubbing media) as per the HWM Rules, 2016.

5 SIA/GJ/IND2/30448/2018 M/s. Sanghi Industries Limited

Survey No. 125/1, 125/2 and 126/1+2+3,

Vill.: Shivrampur, Tal.: Choryasi, Dist.: Surat.

Appraisal

Category of the unit: 3(b)

Project status: New




• Project proponent has submitted EIA Report prepared by Eco Chem Sales & Services based on the

TOR issued by SEIAA.

• Public Hearing for the project was held on 22/03/2019.

• This is new unit proposes for stand alone cement grinding as tabulated below:

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Sr. No.

Name of the Products

Quantity MMT/Annum

End-use of products

1 Cement (OPC / PPC / PSC)

2.0 Customer

• The project falls underCategory B of project activity 3(b) asper the schedule of EIA Notification 2006.



Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 282.28

Brief details of EMP

S. No.

Particulars Capital Cost

(Lakhs) Recusing Cost (Lakhs/annum)

1. Air Pollution Control Devices 752.15 85.00

2. Water Pollution & Reclamation 35.00 5.60

3. Occupational Health and Safety 49.85 18.30

4. Environmental Monitoring 54.00 27.81

5. Green Belt Development 20.00 12.00

Total 911.00 148.71

Brief details of CER Approximately Rs. 424.00 Lakhs (~1.5%) is been allocated for following CER activities for next five years.

S.No. CER Activities Cost (Lakhs)

1. Drinking water facility in nearby village 75.00

2. Up-gradation and hygiene facilities in nearby village 149.00

3. Plantation in community areas 55.00

4. Training and Awareness Program 75.00

5. Education & Farming related activities 70.00

Total 424.00

B Total Plot area ( sq. meter) 48,560 m2

Green belt area,/Tree Plantation area ( sq. meter) 1650 m2

C Employment generation 780 Nos. (Construction + Operation)

D Water

i

Source of Water Supply(GIDC Bore well, Surface water, Tanker supply etc...)

The water requirement shall be met from irrigation department/Private Tanker.


Application has been made to Irrigation Department which is under process


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S. No. Particulars Water Consumption, (KLD)

A. Domestic 15.0

B. Industrial

1. Processing/Cooling 150

2. Dust suppression & Fire Fighting 10 KLD Fresh Water + 58 KLD from Blow down = 68 KLD

Total Industrial 160.0

C. Gardening 25 KLD Fresh water + 20 KLD recycled= Total 45

Total Fresh water Requirement 200.0

Total water Requirement 278.0

1) Total water requirement for the project: 278 KLD 2) Quantity to be recycle: 78 KLD 3) Total fresh water requirement: 200 KLD

iii

Waste water generation (KLD)

Type / Source

Quantity of Waste Water

Generated (Kilo Litre per Day)

Treatment

Capacity (Kilo

Litre per Day)

Treatment

Method

Mode of

Disposal

Quantity of Treated

Water Used in Recycling / Reuse (Kilo

Litre per Day)

Quantity of Discharged

Water (Kilo Litre per

Day)

Domestic 10.0 15 STP - 8 None

Industrial 70.0 150 Cooling Tower

- 70 None

iv Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..

STP – 15 KLD

v Mode of Disposal & Final meeting point

Domestic: Recycle through STP and use for green belt

Industrial: Recycle through close circuit Cooling Tower

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility

Not Applicable


Not Applicable

vii Reuse/Recycle details (KLD)

78 KL

E Air

i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Proposed

S.No. Location Types of Emission

Qty. Nos.

Air Pollution Control Measures(APCM)

Stack Details

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Page 17 of 167

1 Cement Mill (VRM)

PM SOx NOx

01 Bag House Capacity - 11,00,000 m3/hr

Height – 55 m Dia – 3.2 m APC: Bag filters Air emission: PM 30 mg/Nm3 SOx 100 ppm NOx 100 ppm

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) Proposed

-

Sr. no.

Source of emission

Type of emission

Stack/Vent Height (meter)

Air Pollution Control Measures (APCM)

1 Not Applicable

-


Fugitive emission during raw material handling and feeding process and vehicle movements. Mitigation measures – High efficiency pulse air jet type bag filters will be considered to arrest the air borne dust at all the locations where transfer of material are takes place; The automatic bagging machine with bag filters will be installed for packing plant; Unloading of coal trucks will be carried out with proper care avoiding dropping of the materials from height. Sprinklers will be installed in Raw Material / Fuel storage/ Loading / unloading areas. The sprinkling of water will be done along the internal roads in the plant in order to control the dust arising due to the movement of vehicular traffic; Proper maintenance of vehicles shall be carried out; All the workers inside the plant will be provided with disposable dust masks; Thick greenbelt will be developed around the plant to arrest the fugitive emissions; and Periodic air quality monitoring shall be carried out as per CPCB / SPCB norms etc.

F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Proposed

i Solid/ Hazardous waste will be collected, stored, transported and disposed as per the Hazardous Waste (Management, Handling and Trans-boundary Movement) Rules, 2016. Dust collected from air pollution control equipment will be 100% recycled in system. Generated used oil from plant machinery will be utilized as alternative fuel to burn in existing cement plant at Sanghipuram.

ii Membership details of TSDF, CHWIF etc. Not Applicable


-

G Solvent management, VOC emissions etc. Not Applicable


• Not Applicable


• Not Applicable

• During the meeting dated 16/04/2019, technical presentation made by the Project proponent.

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Page 18 of 167

• During the meeting, the project was appraised based on the information furnished in the EIA Report,

various issues raised during the public hearing and details presented during the meeting.

• The baseline environmental quality has been assessed for various components of the environment

viz. air, noise, water, biological and socioeconomic aspect for the study area of 10 km radial

distance from project site for the period 01/10/2018 to 31/12/2018. Ambient Air Quality monitoring

was carried out for PM2.5, PM10, SO2, NOx, CO and VOC at Nine locations, including the project

site. Values conform to the prescribed standards for Ambient Air Quality. The incremental Ground

Level Concentration (GLC) has been computed using ISCST 3.

• The resultant concentrations are within the NAAQS. The modeling study proved that the air

emissions from the proposed plant would not affect the ambient air quality of the region in any

significant manner. The ambient air quality around the proposed project site will remain within the

National Ambient Air Quality Standards (NAAQS).

• Risk assessment including prediction of the worst-case scenario and maximum credible accident

scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-

Site Emergency Plan has been covered in the RA report.

• Committee noted that this proposal is for new project of 2.0 MMTPA Standalone Cement Grinding at

Survey No. 125/1, 125/2 and 126/1+2+3, Village: Shivrampur, Taluka: Choryasi, District: Surat .

• Cooling bleed off will be utilized for dust suppression within premises. There will no process effluent

generation. Sewage will be treated in STP and treated sewage will be utilize on land for

gardening/plantation within premises.

• PP has proposed to use Lignite or Coal or Petcoke 12 TPH as fuel in HAG. Committee noted that

use of Petcoke in HAG is not allowed in Gujarat as per approved fuel notification. PP has not

proposed APCM for SOx control incase of use of lignite. Committee found that details of stacks

attached to APCS are not addressed. While deliberation on fuel, PP informed that they will not use

lignite &Petcoke as a fuel.

• This office has received representation from M/s. L&T Limited, Hazira against this project regarding

anticipated air pollution due to proposed Cement grinding unit through email dated 12.04.2019. M/s.

L&T Ltd. represented that they are manufacturing super critical turbine generator, nuclear

equipments, war weapons (gun, tanks etc.) and fugitive dust emission of proposed project will

adversely affect quality and performance of the product which being used in national security. The

same issue was also raised by M/s. L&T Limited during public hearing on dated 22/03/2019.The

copy of representation of M/s. L&T Limited, Hazira was given to PP for compliance of the issues

raised by them.


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Page 19 of 167

• Committee deliberated CER, EMP and baseline data. PP has not furnished status of all the

applicable Rules, Acts, Regulation, Clearances in a tabular form as per given ToR no. 5.

After deliberation, SEAC unanimously decided to consider the proposal after submission of

the following details:

1. Readdress ToR no. 5, 40

2. Point wise action plan regarding representation of L&T Ltd. Hazira.

3. Submit raw material & product transportation route, its impact on surrounding area and

mitigation measures.

4. Undertaking regarding no use of Lignite &Petcoke as fuel.

5. Sound APCM to control fugitive dust emission during raw material transportation, storage,

handling, loading, unloading, transfer; fuel grinding etc.

6. Details of vents/stacks with specific source &Air Pollution Control System.

7. Compliance of Coal & Ash handling guidelines & its commitment.

6 SIA/GJ/IND2/31394/2018

M/s. Gujarat Dyestuff Industries

Plot No. Z/25,26,27,28, Dahej SEZ,

Vill.: Dahej, Tal. : Vagra,Dist.: Bharuch

EC

Amendment


Project status: EC Amendment

• This unit has been granted EC vide letter no. SEIAA/GUJ/EC/5(f)/43/2018 dated January 31, 2018.

• Now this unit has applied for EC amendment vide proposal no. SIA/GJ/IND2/31394/2018 dated

28.03.2019.

• During the meeting dated 16/04/2019, technical presentation made by the Project Proponent (PP).

• Unit has applied for EC amendment to total water consumption from 34.5 KLD to 166 KLD. The

additional water consumption will be utilized in cooling purpose only.

• Industrial effluent will be treated in ETP and reused in cooling make up. Complete ZLD will be

maintained.

• PP explained that the acetic anhydride plant requires huge amount of cooling and the conventional

cooling system is through cooling water (upto 40 degree) followed by chill water (upto 10 degree)

and finally through brine (upto -10 degree). When the EC application was done they had envisage

that the chill water and brine requirement would be met through using VAM (Vapour absorption

Machine) waste heat from gas based power plant (Proposed) and flue gas from furnace. Based on

above the water consumption in the cooling tower which was envisaged in the plant was 28.5 KLPD.

Thereafter, when the detailed engineering was conducted after the approval of the EC it was

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Page 20 of 167

revealed that firstly there was not enough flue gas generated out of the furnace and gas based

power plant of 500 KVA. Also coupled with the idea that small gas based power plant (Proposed)

was highly uneconomical against cheaper power (Rs. 4.50/ KW) available at SEZ Dahej. During the

detailed engineering it was finalized that it is economical to utilize flue gas generated out of the

furnace for pre heating the thermic fluid required for the heating purpose. Which would entail

reduced coal consumption and less carbon footprint. The idea of gas based power plant was

shelved and grid power was taken. Finally the scheme was developed for electrical run compressors

for generating chill water and brine which would require cooling tower systems. Hence instead of

250CMH a cooling tower of 1100 CMH was installed.Based on 1100 CMH cooling tower and

considering evaporation loss of 0.57 % of circulating water and drift loss of 0.05% the total make up

water requirement in the cooling tower works out to be 160KLPD.

• PP added that the other factor has affected the high consumption of water is the fact that the drift

and evaporation losses at Dahej being a coastal area is on higher side as compared to other

locations.

• After detailed discussion, committee decided to recommend for grant of amendment in

condition no. 4 of EC granted to this unit vide letter no.SEIAA/GUJ/EC/5(f)/43/2018 dated

January 31, 2018to SEIAA with following specific condition and other condition shall remain

same.

1. Unit shall maintain record/logbook of fresh water consumption in cooling system on day to day

basis.

7 SIA/GJ/IND2/33097/2019 M/s Sujal DyeChem Pvt. Ltd.

Plot No C1-132,125,133, Phase I, GIDC Estate Vatva, Dist.: Ahmedabad.

Screening & Scoping

Category of the unit : 5(f)

Project status: Expansion

• This office has received an application vide their online proposal no. SIA/GJ/IND2/33097/2019 dated

20/03/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for

preparation of EIA/EMP report.

• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.

• This is an existing unit engaged in manufacturing of synthetic organic chemicals and now proposes

for expansion as tabulated below:

SR. NO

PRODUCT NAME Cas No. Existing Mt/Month

Additional MT/Month

Total MT/Month

1 Vinyl Sulphone Ester of Ortho Anisidine (OAVS)

26672-22-0 2.0 -2.0 NIL

2 Formulation of Dye (Wood Stains)

8.0 NIL 8.0

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Page 21 of 167

3 Pyrazolone

15.0 15.0 30.0

1. 1 phenyl 3 Methyl 5 Pyrazolone 61278-21-5

2.Para Toyl 3 Methyl 5 Pyrazolone 86-92-0

3. 1,3 Sulpho Phenyl 3 Methyl 5 Pyrazolone

119-17-5

4. 1, 4 Sulpho phenyl 3 Methyl 5 Pyrazolone

89-36-1

5. 1,3 Metachloro 3 Methyl 5 Pyrazolone

20629-90-7

4 Solvent Dyes Such as

1. Solvent Yellow 33 8003-22-3

NIL

65

50




5. Solvent Blue 35 17354-14-2

6. Solvent Blue 36 14233-37-5

7. Solvent Blue 104 116-75-6

8. Solvent Blue 122 67905-17-3

9. Solvent Orange 60 6925-69-5

10. Solvent Red 111 82-38-2

11. Solvent Red 207 15958-69-6

12. Solvent Violet 13 81-48-1

13. Pigment Orange 3468-63-1

14. Solvent Violet 14 8005-40-1

15.0 15. Solvent Red 135 20749-68-2

16. Solvent Yellow 163 106768-99-4

30

17. Solvent Red 52 81-39-0

18. Solvent Red 195 89106-94-5

NIL

19. Solvent Yellow 157 27908-75-4

20. Solvent Orange 105 31482-56-1

21. Solvent Orange 63 16294-75-0

22. Solvent Green 3 128-80-3

Total

40.0 78.0 118




Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores):

Existing: 1.0 Cr. Proposed: 1.0 Cr. Total: 2.0 Cr.

B Total Plot area ( sq. meter)

Existing: 1574 sq. m Proposed: 706.53 Sq. m

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Page 22 of 167

Total: 2280.53 sq. m

Green belt area ( sq. meter)

Existing: 200 sq. m Proposed: NIL Total: 200 Sq. m

C Employment generation Existing: 15 Proposed: 10 Total: 25

D Water

i


GIDC Water



Sr No

Category Existing Additional Total

1. Domestic Purpose 1.5 NIL 1.5

2.

INDUSTRIAL

Process 3.3 13.7 17.0

Washing 1.5 0.1 1.6

Boiler 1.0 2.0 3.0

Total water Consumption (Domestic) 1.5 Nil 1.5

Total water Consumption (Industrial ) 5.8 15.8 21.6

1) Total water requirement for the project: 23.1 KLD 2) Quantity to be recycled: NIL 3) Total fresh water requirement: 23.1KLD


Sr No

Category Existing Additional Total

1. Domestic Purpose 1.0 NIL 1.0

2.

INDUSTRIAL

Process water 10.7 9.4 20.1

Washing 1.5 0.1 1.6

Boiler 0.1 0.2 0.3

Total Waste water Generation (Domestic) 1.0 NIL 1.0

Total Waste water Generation (Industrial) 12.3 9.7 22.0

iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..

• Existing Effluent Treatment Plant

Sr. No.

Name of Unit No. of Unit Capacity

1 Collection Tank-II 1 8.0 KL

2 Neutralization Tank –II 1 5.0 KL

3 Primary Settling Tank 1 10.0 KL

4 Aeration Tank 1 6.0 KL

497

5 Secondary Settling Tank

6 Holding Tank

7 Dual Media Filter

8 Final Collection Tank

9 Sludge Drying Bed

• Additional Effluent Treatment

Sr. No.

Name of Unit

1 Collection Tank

2 Neutralization Tank

3 Settling Tank

4 Holding Tank

5 Sludge Drying Bed


• Existing Effluent Treatment Plant

• Additional Effluent Treatment Plant


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Secondary Settling Tank 1

Holding Tank 1

Dual Media Filter 1

Final Collection Tank 1

Sludge Drying Bed 4 0.9mX0.9mX1.0 m

Additional Effluent Treatment Plant

Name of Unit No. of Unit

Collection Tank-I 2

Neutralization Tank -I 1

Settling Tank 1

Holding Tank 2

Sludge Drying Bed 4


Existing Effluent Treatment Plant

Additional Effluent Treatment Plant

Page 23 of 167

5.0 KL

5.0 KL

--

10 KL

0.9mX0.9mX1.0 m

Capacity

15 KL

15 KL

10 KL

15 KL

8 ft X 8 ft

497

Note: (In case of CETP discharge) :Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 compliance of CETP.

� The total industrial wastewater generation from Manufacturing process and other ancillary process will be 22.00 KLD out of which 1.6 KLD Washing Effluent will be sent to CETP Vatva For their treatment and then Discharge Through common facility for the spray dryer and MEE.

Existing Quality of Effluent Going to CETP (1.6 KLD)

Parameter Result mg/l

PH 7.5

TSS 50

COD 900

TDS 2200

Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):� Not applicable


Domestic: The generated 1.5 KLD sewage

Industrial: The total industrial wastewater generation from Manufacturing process and other ancillary process will be 22.00 KLD out of which 1.6 KLD Washing Effluent will be sent to CETP Vatva For their treKLD Waste Water Discharge Through common facility for the spray dryer and MEE.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water

� We have not required Common facility for waste water Treatment


(For waste water treatment)We have not required for membership certificate for Waste water treatment

vii Simplified water balance diagram

Existing Water balance diagram


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Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding

The total industrial wastewater generation from Manufacturing process and other ancillary process will be 22.00 KLD out of which 1.6 KLD Washing Effluent will be sent to CETP Vatva For their treatment and then remaining 20.4 KLD Waste Water Discharge Through common facility for the spray dryer and MEE.

Existing Quality of Effluent Going to Proposed Quality of Effluent Going to CETP (1.6 KLD)

Result mg/l Parameter Result mg/l

7.5- 8 PH 7.5-

50-60 TSS 50-60

900-1000 COD 700-800

2200-2700 TDS 2200-2700



The generated 1.5 KLD sewage will be disposed through soak pit/septic tank.

The total industrial wastewater generation from Manufacturing process and other ancillary process will be 22.00 KLD out of which 1.6 KLD Washing Effluent will be sent to CETP Vatva For their treatment and then remaining 20.4 KLD Waste Water Discharge Through common facility for the spray dryer and

In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)

We have not required Common facility for waste water Treatment


(For waste water treatment) We have not required for membership certificate for Waste water treatment

Simplified water balance diagram with reuse / recycle of waste water

Existing Water balance diagram

Page 24 of 167

Management of waste water keeping in view direction under section 18 (1) (b) of the issued by CPCB regarding

The total industrial wastewater generation from Manufacturing process and other ancillary process will be 22.00 KLD out of which 1.6 KLD Washing Effluent will be sent

remaining 20.4 KLD Waste Water

Proposed Quality of Effluent Going to

8

60

800

2700

will be disposed through soak pit/septic tank.

The total industrial wastewater generation from Manufacturing process and other ancillary process will be 22.00 KLD out of which 1.6 KLD Washing

atment and then remaining 20.4 KLD Waste Water Discharge Through common facility for the spray dryer and


We have not required for membership certificate for Waste water treatment

497

After Expansion Water Balance Diagram

vii Reuse/Recycle details (NIL) [Source of reuse & application area]

Total reuse NIL KLD

E Air


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After Expansion Water Balance Diagram

Reuse/Recycle details (NIL) [Source of reuse & application area]

Page 25 of 167

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Page 26 of 167

i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Existing & Proposed

-

Sr. no

Stack attached to

Stack height in meter

Type of Fuel

Consumption APCM Type of Emission

Remarks

1 Steam Boiler (2 TPH)

14

PNG (E) Agro waste (A)

650 SCM/Day(E) 2 MT/Day (A)

Multi Cyclone Separator

PM SOx NOx

Existing

2

Thermic Fluid Heater (4 Lac KCal/hr)

14

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) Existing & Proposed

-

Sr

no

Stack attached

to

Stack height

in meter APCM

Type of

Emission Remarks

1. Reaction Vessel

(2 Nos.) 15

Two Stage Water

Scrubber followed

by Alkali Scrubber

PM

SOx

NOx

HCl

Existing


� The entire manufacturing activities will be carried out in the closed reactors and regular checking and maintenance of reactors will be carried out to avoid any leakages.

� The tank vents will be equipped with either a carbon filter or an oil trap to prevent water vapor from entering the tank as it breathes.

� All the motors of pumps for the handling of hazardous chemicals will be flame proof and provided with suitable mechanical seal with stand-by arrangement

� Control of all parameters on a continuous basis will be done by adequate control valves, pressure release valves and safety valves etc.

� All the flange joints of the pipe lines will be covered with flange guards. � All the raw materials will be stored in isolated storage area and containers tightly closed. � There will also be provision of adequate ventilation system in process plant and

hazardous chemical storage area

F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Existing & Proposed

i

Sr. No

Types of Hazardous Waste

Sources Categor

y

Existing

MT/Year

Additional

MT/Year

Total MT/Year

Disposal

1 ETP

Sludge ETP Area 35.3 96 14.00 110.0


Transportation and Dispose to

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Page 27 of 167

TSDF

2 Used Oil Plant

Machinery 5.1 0.010 0.45 0.5

Collection, storage, Reuse within premises.

3 Discarded Container and Bag

Material Storage

and Handling

33.1 0.200 200.00 200.00


Transportation and

Reuse/Dispose to Authorized Reprocessors

4 Spent

Sulphuric Acid

1-3 Sulpho Phenyl 3 Methyl 5

Pyrazolone&

1-4 Sulpho Phenyl 3 Methyl 5

Pyrazolone

26.3 480 2760 3240


Transportation and Dispose to

Novel

5 Solvent

Dyes

Solvent

Dyes 26.1 324 1404 1728

Collection,

storage, and

reuse in

Process after In

house

distillation

6 Solvent

Residue

Distillation

Unit 26.2 6.0 30.0 36.0


Transportation and Dispose to Co-processor or

through common

incineration facility

-

ii Membership details of TSDF, CHWIF etc. (For HW management)

We have obtain membership after permission

iii Details of Non-Hazardous waste & its disposal(MSW and others)

No Applicable


i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.

� Types of Solvent : Methanol, ODCB, Xylene, IPA, Butanol � Spent solvents will be recovered through in-house distillation column with double

condenser System � 98% - 99% recovery will be carried out. � Recovered solvents will be collected in receiver and transferred to reaction vessel

through vaccum and completely reused within process.


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Page 28 of 167

� Sources of fugitive emissions include storage of chemicals, loading and unloading section, raw material handling and, hazardous waste storage area

Measures : � The fugitive emissions in terms of handling losses will get reduced by proper storage

and handling. � Hazardous chemicals will be stored as per standard criteria. • Periodically monitoring

will be carried out as per the post project monitoring plan. � All materials must be stored in suitable packing to prevent contamination of air. � Enclosed system & efficient procedures for materials charging shall be ensured.



Storage tanks NIL

Drum/Barrel storage

HCl Sulphuric Acid 98% Copper Cyanide Ethyl Acetate TertButanol Sodium Hypochlorite Methanol Toluene Hexane


• Technical presentation was made by the project proponent along with their consultant/expert

Satva Environ Consultancy, Ahmadabad during SEAC meeting dated 16/04/2019.

• Committee noted that this unit has proposed expansion in Dye manufacturing at GIDC, Vatva.

• Process effluent and boiler blow down will be sent to common spray dryer and common MEE of

GESCL, Vatva after giving primary treatment within premises.

• Washing effluent will be sent to CETP, Vatva after giving primary treatment within premises.

• Two Stage Water Scrubber followed by Alkali Scrubber will be provided as APCM with reactors.

• Spent sulphuric acid will be sent to NOVEL. Solvent residue will be sent for co-processing or

CHWIF for incineration.

• Considering the above project details, after detailed discussion, the terms of reference (ToR)

were prescribed as below and as per the standard TOR for the Synthetic Organic Chemical

projects recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and

approved by SEIAA in its 12th meeting dated 16/09/2017 for the EIA study to be done covering

10 Km radial distance from the project boundary.

1. Undertaking of not manufacturing Vinyl Sulphone Ester of Ortho Anisidine (OAVS) after

proposed expansion.

2. Justification of ETP sludge quantity against treatment of industrial effluent.

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3. Details with respect to justification for proposed expansion: (1) To address proportionate

availability of space for production plant. (2) To address proportionate availability of storage

area for raw materials finished goods, utilities and goods carrier movement within premises.

(3) To address proportionate captive/common infrastructure available to accommodate

additional load due to proposed expansion. (4) Environment impact and its mitigation

measures for common/ captive infrastructure due to proposed production.

4. Membership certificate of NOVEL, Vatva for acceptance of 3240 MT/Year Spent Sulphuric

Acid.

5. Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment

Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall

be made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities


report.

6. Explore the use of renewable energy to the maximum extent possible. Details of provisions to

make the project energy-efficient through of energy efficient devices and adoption of modes

of alternative eco-friendly sources of energy like solar water heater, solar lighting etc.

Measures proposed for energy conservation.

7. PP shall furnish status of all the applicable Rules, Acts, Regulation, Clearances in a tabular

form.

8. PP shall address spent solvent with details of storage, handling and re-use under the

Hazardous and other Waste (Management and Transboundary Movement) Rules 2016.

9. Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent

proposed for use in-house with detailed chemical properties including vapor pressure. LDAR

shall endeavour prevention of losses of solvents to the best minimum extent.

10. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard

during unloading, storage, transportation, handling and processing of Solvents.

11. Segregation of waste water streams based on characteristics and its proper management

keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of

Pollution) act, 1974 issued by CPCB regarding compliance of CETP.

• The TOR prescribed as above and as per the standard TOR approved by SEIAAand the model

ToRs available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical

Industry’ shall be considered as generic TORs for preparation of the EIA report in addition to all the

relevant information as per the generic structure of EIA given in Appendix III in the EIA Notification,

2006.

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• The project proponent shall have to apply for Environmental clearance through online portal

http://environmentclearance.nic.in/ along with final EIA report.

8 SIA/GJ/IND2/33347/2019 M/s. Dhenu Industries

Plot No. 48 GIDC Estate Kadi,

Kadi, Dist.: Mehsana

Screening &

Scoping


Project status: New





• This is new unit proposes for manufacturing of synthetic organic chemicals as tabulated below:

SR.

NO PRODUCT NAME

Proposed

MT/Month

Group 1 250

1. Disizing enzymes

2. Mercerizing wetting agent

3. Wetting agent

4. Peroxide stabilizer

5. Silicone defoamer

6. Scouring agent

7. Dye fixing agent

8. Anti-creasing agent

9. Nonionic soaping agent

10. Anionic soaping cum washing agent

11. Dye levelling agent

12. Silicone softener

13. Cationic and nonionic softener

14. Hydrophilic softener

15. Poly ethylene wax emulsion

16. Loop acceletar

17. Khadi paste

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18. PVA Emulsion

19. PE Emulsion

20. Cotton Khadi

21. Fevicol-5H

22. Sticker Gum

23. Lamination Gum

24. Carboxymethyl Starch

25. Carboxymethyl Tamarind

26. Carboxymethyl Guar Gum

27. Carboxymethyl Cassia Tora

28. Cationic Guar Gum Powder

29. Depolymerized Guar Gum

30. Hydrolyzed Tamarind

31. Cross Linked Guar Gum Powder

32. Hydroxy Ethyl Guar Gum

33. Hydroxy Ethyl Tamarind

34. Hydroxy Propyl Guar Gum

35. Sodium Meta Chloro Acetic Acid (SMCA)

Group -2 100

1. Tridecyl Alcohol 12 Ethoxylate

2. Stearic Acid 6 Ethoxylate

3. Polyethylene Glycol 200 (PEG 200)

4. Cocoamine 2 Ethoxylate

5. Castor oil 40 Ethoxylate

6. Lauryl Alcohol 5 Ethoxylate

7. Nonyl Phenol 9 Ethoxylate

8. Tallow Diamine 10 Ethoxylate

9. Tallow Amine 10 Ethoxylate

10. Surcose 10 mole Ethoxylate

11. Stearyl Amine 10 Ethoxylate

12. Oleyl Amine 10 Ethoxylate

13. OleylCetyl alcohol 6 Ethoxylate

14. Octyl Alcohol 2 Ethoxylate

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Page 32 of 167




Sr. Particulars Details

15. Octyl Alcohol 6 Ethoxylate

16. Octyl Alcohol 10 mole Ethoxylate

17. Octyl Alcohol 20 mole Ethoxylate

18. Oleic Acid 7 mole Ethoxylate

19. Oleic Acid 14 mole Ethoxylate

20. Cetyl Alcohol 20 Ethoxylate

21. Lauryl Amine 10 Ethoxylate





26. Lauric Acid 10 Ethoxylate

27. Glycerine 25 Ethoxylate

28. 2 Ethyl Hexanol 12 Ethoxylate

29. Nonyl Phenol 2 mole Ethoxylate




33. Glycerine EO PO Polymer

34. Pluronic L 68

35. Di Ethylene Tri Amine 80 PO 90 EO

36. Poly Propylene Glycol 400

37. Poly Propylene Glycol 900

38. oly Propylene Glycol 2020

39. Pluronic L 61

40. Pluronic L 62

41. Pluronic L 64

42. Tri Decyl Alcohol 6 EO 4 PO

Total Production Quantity 350

of 167


Page 33 of 167

no.



Green belt area ( sq. meter) 200 Sq. m.


D Water

i

Source of Water Supply (GIDC Bore well, Surface

water, Tanker supply etc...)

GIDC water Supply



Sr.

No.

Category Quantity

(KL/Day)

1. Domestic 2.0

2. Industrial 6.5

Mfg. Process 4.0

Boiler 1.0

Washing 0.5

Cooling 1.0

Total Water Requirement(1 +2) 8.5


2) Quantity to be recycle: 0.7NIL

3) Total fresh water requirement: 7.8 KLD


Sr.

No.

Category Quantity

(KL/Day)

1. Domestic 1.5

2. Industrial 0.7

Process NIL

Boiler (Blow-down) 0.1

Washing, 0.5

Cooling 0.1

3. Total Industrial Waste Water 0.7


[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP

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Page 34 of 167

etc..

Sr.

No. Name of Unit Capacity

1 Collection Tank 5 KL





compliance of CETP.

� Total Waste Water Generation 0.7 KLD From Washing and Blow Down, It Will

Be Reuse Totally Reuse in Emulsion making Process and Thickner. Hence, unit

is Going to Zero Liquid Discharge


� Total Waste Water Generation 0.7 KLD From Washing and Blow Down, It Will

Be Reuse Totally Reuse in Emulsion making Process and thickner. Hence, unit

is Going to Zero Liquid Discharge


Domestic: Domestic 1.5 KLD sewage generated will be disposed through soak

pit/septic tank.

Industrial: • Total Waste Water Generation 0.7 KLD From Washing and Blow

Down, It Will Be Reuse Totally Reuse in Emulsion making Process and

Thickner. Hence, unit is Going to Zero Liquid Discharge

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE

etc. , Name of CF

No required Common Facility


(For waste water treatment)

Collection TankReuse in Emulsion

Making Process and Thickner

497

vii Simplified water balance diagram with reuse / recycle of

viii Reuse/Recycle details (0.7KLD)

Total reuse 0.7 KLD

Source of waste

water for reuse


(From where it is

coming)

Blow Down

E Air


No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA

etc.

-

Sr.

no

Stack attached

to


of 167


Reuse/Recycle details (0.7KLD)


Application

area with

quantity in KLD

(Where it is

used)

Characteristics of

waste water to be

reused (COD, BOD,

TDS etc.)

Emulsion

making

process and

Thickner

pH = 6.5 to 8.00

COD <150

TDS<2500

Flue gas emission details

Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA

Stack

height

Type of

Fuel

Consumptio

n APCM

Page 35 of 167

waste water

Remarks

regarding

feasibility to

reuse i.e.

---

Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA

APCM Type Of

Emission

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Page 36 of 167

in

meter

1 Non IBR Boiler

(0.5 TPH) 15

Agro

waste and

briquettes

500 Kg/Day

Adequate

Stack

Height

PM

SOx

NOx

-

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)

There is no any Type of Process gas Emission


As below:

� The entire manufacturing activities will be carried out in the closed reactors and

regular checking and maintenance of reactors will be carried out to avoid any

leakages.

� The tank vents will be equipped with either a carbon filter or an oil trap to prevent

water vapor from entering the tank as it breathes.

� All the motors of pumps for the handling of hazardous chemicals will be flame proof

and provided with suitable mechanical seal with stand-by arrangement

� Control of all parameters on a continuous basis will be done by adequate control

valves, pressure release valves and safety valves etc.

� All the flange joints of the pipe lines will be covered with flange guards.

� All the raw materials will be stored in isolated storage area and containers tightly

closed.

� There will also be provision of adequate ventilation system in process plant and

hazardous chemical storage area.

� A regular preventive maintenance will be planned to replace or rectify all gaskets,

joints etc.

� The unit will also develop green belt within the factory premises to control the

fugitive emission from spreading into surrounding environment

F Hazardous wastes

(as per the Hazardous and Other Wastes (Management and Transboundary

Movement) Rules 2016.

i Sr.

No

Types of

Hazardous Sources Category

Propose

MT/Year Disposal

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Page 37 of 167

Waste

1 Used Oil Plant

Machinery 5.1 0.020


Reuse within premises.

2

Discarded

Container

Empty Bags

with liner

Material

Storage

and

Handling

33.1 200


Transportation and

Dispose by selling to

Registered Recycler

-

ii Membership details of TSDF, CHWIF etc.

(For HW management)

We will obtained after getting

NOC from GPCB

iii Details of Non-Hazardous waste & its disposal

(MSW and others)

Not applicable


i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered

Solvents

There is no any type of Solvent use in Process


• Sources of fugitive emissions include storage of chemicals, solvents storage,

loading and unloading section, raw material handling and, hazardous waste

storage area Measures:

• The fugitive emissions in terms of handling losses will get reduced by proper

storage and handling.

• Hazardous chemicals will be stored as per standard criteria. • Periodically

monitoring will be carried out as per the post project monitoring plan.

• Proper ventilation in storage & production area shall be ensured

• All materials must be stored in suitable packing to prevent contamination of air

• Enclosed system & efficient procedures for materials charging shall be

ensured.

• Procedures for start-up shut down, operation & maintenance procedures shall

be established & maintained.

• The coverage of greenbelt around the plant also acts as natural barrier to stop

carrying of dust along with the wind current.


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Page 38 of 167

Storage details Name of major Hazardous

chemicals

Remarks

Storage tanks NIL

Drum/Barrel storage L.A. 10 mole emulsifier

OP – 10 Emulsifier

Acetic Acid

Vegetable fatty acids

Acrylic acid

Sulfuric Acid

Oleyl Alcohol

Cylinder Ethylene Oxide 350 kg 3 Cylinder



Satva Environ Consultancy, Ahmedabad during SEAC meeting dated 16/04/2019.

• Committee noted that this is a new unit proposes synthetic organic chemical manufacturing at

GIDC,Kadi.

• Industrial effluent generated from washing, cooling and boiler will be collected and used in mfg

process within premises. There will be no process effluent generation.

• Agro waste will be used as fuel in Steam Boiler (Non IBR) of capacity 0.5 TPH. There will be no

process gas emission.

• Hazardous waste management is addressed.

• Committee asked PP to take adequate safety precautions in Ethylene Oxide (EO) Storage,

Transportation and Handling to which PP agreed.

• Considering the above project details, after detailed discussion, the terms of reference

(ToR) were prescribed as below and as per the standard TOR for the Synthetic Organic

Chemical projects recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated

14/09/2017 and approved by SEIAA in its 12th meeting dated 16/09/2017 for the EIA study

to be done covering 10 Km radial distance from the project boundary.

1. Safety precautions for Ethylene Oxide (EO) storage, handling and transportation as per the

prevailing law/rules & regulations.





of 167


Page 39 of 167

report.






form.

• The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model




2006.



9 SIA/GJ/IND2/33489/2019 M/s.Sweta Petro Chem

Plot No. D-2/CH/356, GIDC Industrial Estate,

Dahej, Dist.: Bharuch

Screening & Scoping


Project status: New

• This office has received an application vide their online proposal no. SIA/GJ/IND2/33489/2019dated




• This is new unit proposes for manufacturing of synthetic organic chemicals as tabulated below.

Sr.

No.

Name of the

Products

CAS no. /CI no. Quantity

MT/Month

End-use of products

1. PIPERAZINE DERIVATIVE

N-Acetyl-4-(4-Hydroxyphenyl)Piperazine(AHPP) Either/Or

67915-02-0 100 API Intermediate

1-(2-Chloroethyl)-4-(3-


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Page 40 of 167

Chlorophenyl) Piperazine Either/Or

1,1-Dimethyl 1-Piperazine Carboxylate (BOC Piperazine) Either/Or


1-Hydroxyethylethoxypiperazine (HEEP) Either/Or


1-(4-Methoxyphenyl) PiperazineEither/Or


1-(4flurophenyl) PiperazineEither/Or


1-Benzylpiperazine Either/Or


Bis Chloro Ethyl Amine Hcl


2. ALDEHYDE

2,4,6 TrimethoxyBenzaldehydeEither/Or


3,4 DihydroxyBenzaldehyde


3. HYDROGENATION PRODUCT

(N:N di-sec-butyl) peraphenylenediamine

101-96-2 400 Tert-butyl 6-[(1E)-2-[4-(4-fluorophenyl)-6-(1-methylethyl)-2-[methyl(methylsulfonyl)amino]-5-pyrimidinyl]ethenyl]-2,2-dimethyl-1,3-dioxane-4-acetate

N:N-BIS(1:4 Dimethyl pentyl) PeraphenyleneDiamine

3081-14-9 400 Tert-dimethyl 6-[(1E)-2-[4-(4-fluorophenyl)-6-(1-methylethyl)-2-[methyl(methylsulfonyl)amino]-5-pyrimidinyl]ethenyl]-2,2-dimethyl-1,3-dioxane-4-acetate

4. R & D Product 0.16

Total 920.84

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Page 41 of 167




Sr.

no.

Particulars Details

A


B Total Plot area ( sq. meter) 5001.50 Sq. m.

Green belt area ( sq. meter) 1509.35 Sq. m.


D Water

i

Source of Water Supply(GIDC Bore well, Surface


GIDC Bharuch.

Status of permission from the concern authority. Unit Obtained Assurance letter of 55

KLD water consumption from GIDC.


Category Quantity

KLD

Remarks

(A) Domestic 3 Fresh water from GIDC

(B) Gardening 4 Fresh water from GIDC

(C) Industrial

Process 19 Fresh water from GIDC

Washing 5 Fresh water from GIDC

Boiler 7 Fresh water from GIDC

Cooling 12 Fresh water from GIDC

Others 3 1 KLD used in Process Scrubber

2 KLD used in Boiler Scrubber (From Boiler

Blow down 2 KLD.)

Industrial Total 46 Fresh 44 KLD + 2 KLD Boiler Blow Down.

Total (A + B + C) 53 Total Fresh water consumption 51 KLD & 2 KLD Internal Reused.

1) Total water requirement for the project: 53 KLD


of 167


Page 42 of 167

3) Total fresh water requirement: 51 KLD


Category Waste water

KLD

Remarks

(A) Domestic 2 Disposed through Soak pit

(B) Industrial

Process 39.2 Low COD stream 31 KLD + High COD/High TDS

stream 8.2 KLD (Out of 8.2 KLD, 0.1 KLD Stripper

loss and 0.2 KLD MEE salt generated. Therefor

Total 8 KLD MEE Condensate + 31 KLD Low

COD stream = 39 KLD will be send to ETP.

Washing 5 Send to ETP

Boiler 2 Boiler blow down will be used in Boiler Scrubber.

Cooling 2 Send to ETP

Others 2 • 1 KLD (Process scrubber)--Scrub Solution

Na2SO3 will be generated and treated in to in

house ETP.

• 1 KLD (Boiler scrubber)--Total 2 KLD Boiler

blow down will be generated. This boiler blow

down will be used in the water scrubber of

boiler 1 KLD Water will be evaporated.

Remaining 1 KLD Solution Will be generated,

which will be used for Ash quenching & Coal

handling.

Total Industrial

waste water

50.2 From total industrial waste water 1 KLD boiler

scrub solution will used for Ash quenching & Coal

handling. 2 KLD boiler blow down reused in boiler

scrubber. Therefore total 47 KLD generated

waste water will be sent to ETP for treatment.

Total [A + B] 52.2 50 KLD Effluent to ETP, 0.2 KLD loss& 2 KLD

Domestic disposed through soak pit.



of 167


Page 43 of 167

� ETP Capacity 60 KLD followed by Sand filter and Activated Carbon filter & MEE used

for High COD/High TDS stream having 10 KLD capacity.


� ETP Flow diagram is given below.


Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention

and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.

� It is new project, then 18 (1) (b) is not applicable.


� Not Applicable.


Domestic: Disposed in soak pit.

Industrial: The Process effluent stream from the plant will be segregated into two

parts—High COD/High TDS and Low COD stream. The High COD /High

TDS stream will be treated with Multi effect evaporator, and the low COD

effluent generated from Multi effect evaporator will be sent to ETP

collection tank, with the other Low COD effluent streams. Low COD

effluent stream from various production plants and utility block is first

HIGH COD

STREAM

LOW COD

STREAM

To CETP Dahej

Final

Collection

Tank

SLUDGE TO TSDF

EQUALIZATION &

Neutralization TANKFILTER PRESS AERATION TANK-1 SETTLING TANK-1

SLUDGE DRYING

BED

AERATION TANK-2SETTLING TANK-2COLLECTION TANKSAND FILTERCARBON FILTER

Mix Solvent to end

user.

MEE CONDENSATE

MEE SALT TO TSDF

STRIPPER MEE

of 167


Page 44 of 167

collected in Stripper & Equalization tanks and treated in in house ETP

followed by sand filter and Activated carbon filter after that 45 KLD waste

water send to CETP Dahej.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name

of CF

� CETP, Dahej.





Total reuse 2 KLD

Source of waste Application Characteristics of Remarks

1 KLD Eva . Loss

8 KLD

Effleunt to CETP Dahej 45 KLDSludge TO TSDF Site 2 MT/Day

Effluent

due to

Reaction

& Raw

material

20.7 KLD


51 KLD Fresh

To Soak Pit

Process Scrubber

Fresh 1 KLD

Coal Handling &

Ash quenching

Scrub Solution

1 KLD

Effluent Treatment Plant (47 KLD)

Gardening

Fresh 4KLD

Boiler Blow

Down

2 KLD

Cooling Tower

Blow Down

2 KLD

Process

Fresh 19 KLD

Washing

Fresh 5 KLD

Cooling Tower

Fresh 12 KLD

Boiler

Fresh 7 KLD

Boiler Scrubber

Recycle 2 KLD

Domestic

Fresh 3 KLD

Waste Water

From Process

39.2 KLD

Sewage

2 KLDWashing

water 5 KLD

0.5 KLD Loss

31 KLD

MEE (8.1 KLD)

SALT to TSDF (0.1

KLD)

MEE Condensate (8 KLD)

LOW COD 31 KLD (10.8 KLD

From Process + 20.2 From

Reaction & R.M

HIGH COD STREAM

8.2 KLD

Stripper

Loss Strip Solvent

0.1 KLD

of 167


Page 45 of 167

water for reuse

with quantity in

KLD (From where it

is coming)

area with

quantity in

KLD (Where it

is used)

waste water to be

reused (COD, BOD,

TDS etc.)

regarding

feasibility

to reuse i.e.

Boiler Blow down

2 KLD

2 KLD Boiler

blow down will

be reused in

boiler scrubber.

Waste water

characteristics

COD:-50-70 mg/l,

BOD:-15-25 mg/l and

TDS:- 1500-2000 mg/l.

Reusable in

Boiler

Scrubber

E Air



-

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

01 Steam Boiler

2 TPH

22

Agro

waste

briquette

/ Coal

5 MT /day PM SO2 NOX

Cyclone

Separator + Bag

filter + water

scrubber 02 Thermic Fluid

Heater 1 Nos.

(5 Lack Kcal)

03 DG Set

250 KVA 09 Diesel

15 Lit/ Hr.

Or 360

Lit/Day

PM SO2 NOX

Adequate Stack

Height


-

Sr.

no.

Specific Source of

emission

(Name of the Product

& Process)

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution

Control

Measures

(APCM)

of 167


Page 46 of 167

1 Reactor Vent

(From Manufacturing

Process ofBis Chloro

Ethyl Amine Hcl )

SO2

17 Alkali Scrubber

-

iii Fugitive emission details with its mitigation measures:

As below:

Sr.

No.

Source Probable

Pollutant

Emission

Control Measures/ APCM

1. Solvent storage tank

Air pollutant (VOC)

i) Carry out work place area monitoring to find out concentration level in ambient air.

ii) Provision of breather valve cum flame arrester.

2. Solvent recovery system

Air pollutant (VOC)

i) Solvent recovery system with steam condensation system.

ii) Pumps & motors are mechanical seal type.

3 Handling of raw material bags in storage area

Air pollutant (PM)

i) Provision of exhaust ventilation

ii) Provision of PPE.

iii) Provision of Job rotation to reduce exposure.

4 Flange joints of pipeline, pump & motors

Air pollutant (VOC)

i) Routine &periodic inspection to check leakage.

ii) Preventive maintenance, Follow SOP for maintenance.

iii) Pumps & motors will be mechanical seal type.

iv) LDAR program will be followed.

Provision of Flange guard.

5 Solid raw material transferring to reactor

Air pollutant (PM)

Hopper will be provided with powder transfer system.

6 Liquid raw material transferring to reactor

Air pollutant (VOC)

Feeding of liquid raw material will be carried out by closed pipeline and mechanical seal pump.

7 Loading /unloading at storage area

Air pollutant (VOC)

Unloading through pipeline to tank in a close system.

F Hazardous wastes


Rules 2016.

i -

Sr Type/Nam Specific Source of Category Quantit Management of HW

of 167


Page 47 of 167

.

n

o.

e of

Hazardou

s waste

generation

(Name of the Activity,

Product etc.)

and

Schedule

as per

HW

Rules.

y

(MT/An

num)

1. Effluent Treatment Plant Sludge

From ETP 35.3 730 Collection, Storage, Transportation, Disposal at TSDF site authorized by the GPCB.

2. MEE Salt From MEE 35.3 36.5 Collection, Storage, Transportation, Disposal at TSDF site authorized by the GPCB.

3. Used Oil From Lubrication 5.1 2 Collection, Storage, Transportation, Reused, Disposal at by Selling registered refiners.

4. Empty Barrels/ Containers/ Liners Contaminated with hazardous chemicals/ wastes

From Packing Material

33.1 350 Collection, Storage, Decontamination, Transportation and Reuse or sell to registered recyclers

5. Distillation Residue

Production process ofworst case scenario:-1-(2-Chloroethyl)-4-(3-Chlorophenyl) Piperazine, and 1,1-Dimethyl 1-Piperazine Carboxylate

28.1 128 Collection, Storage, Send for co- processing /Incineration.

6. Recoverable spent solvent

Production process ofworst case scenario:-N-Acetyl-4-(4-Hydroxyphenyl)Piperazine,2,4,6 TrimethoxyBenzaldehyde, N:N-BIS(1:4 Dimethyl pentyl) PeraphenyleneDiamine

28.6 25,028 Collection, Storage, Transportation & recover and reuse internally.

of 167


Page 48 of 167

7. Non-Recoverable spent solvent

Production process ofworst case scenario:-N-Acetyl-4-(4-Hydroxyphenyl)Piperazine,2,4,6 TrimethoxyBenzaldehyde, N:N-BIS(1:4 Dimethyl pentyl) PeraphenyleneDiamine

28.6 500 Collection, Storage, Transportation & sell to end user having Rule-9 Permission.

8. Acetic Acid Production process of N-Acetyl-4-(4-Hydroxyphenyl)Piperazine.

--- 522 Collection, Storage, Transportation & sell to end user having Rule-9 Permission.

9. Sodium Bromide Solution

Production process of 1-(2-Chloroethyl)-4-(3-Chlorophenyl) Piperazine

C4 502 Collection, Storage, Transportation & sell to end user having Rule-9 Permission.

10.

Spent Charcoal / Carbon

Production process of 1-(4-Methoxyphenyl) Piperazine

28.3 28 Disposal by Co-processing / incineration in common incineration of BEIL

11.


From Effluent Treatment plant

26.1 4 Collection, storage, transportation & co processing/incineration in common incineration of BEIL.

12.


From Solvent Recovery System

26.1 2 Collection, storage, transportation & co processing/incineration in common incineration of BEIL.

13.

Potassium Chloride Powder

Production process of 1-(4flurophenyl) Piperazine

--- 1,440 Collection, Storage, Transportation & sell to end user having Rule-9 Permission.

14.

Spent residue containing spent catalyst

Production process of (N:N di-sec-butyl) peraphenylenediamine and N:N-BIS(1:4 Dimethyl pentyl) PeraphenyleneDiamine

28.2 164 Collection, Storage, Transportation & sell to end user having Rule-9 Permission.

15.

Scrubber Solution

Production process ofBischloroethly amine

C4 365 To Effluent Treatment Plant.

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Page 49 of 167

Hcl

16.

Mix solvent From stripper 28.6 36.5 Collection, Storage, Transportation & send to co-processors / incineration.

17.

Date Expired Product

From Premises 28.4 12 Collection, storage, transportation , co-processing in cement plants /incineration in common incinerator, landfill in common TSDF (if calorific value is less than 2500 kcal/kg).

18.

Off-specification Product

Production Process 28.5 12 Collection, storage, transportation , Co-processing in cement plants /incineration in common incinerator, landfill in common TSDF (if calorific value is less than 2500 kcal/kg).


(For HW management)

Unit will apply for membership for

membership of TSDF and incineration.


(MSW and others)

MSW waste will be collected by notified

authority of GIDC.

Sr. No.

Waste Quantity Mode Of Disposal

1. Glass Waste ( Z13) 0.01 MT/month

To TSDF.

2. Paper waste (Z44) 0.1 MT/month At notified area facility.

3. Fly Ash 1.5 MT/ Month

Send to authorize Brick manufactures



(Details in Table Format)

Sr

.

N

o.

Name of

Representative

Product

Name of

Solvent

used

Produ

ct

Quanti

ty in

MT/Mo

nth

Solve

nt

Quan

tity

used

in ton

Solve

nt

recov

er

Quan

tity in

Solvent

Recove

red

Quantit

y in

MT/Mo

Percent

age

Recove

ry

of 167


Page 50 of 167

1.

N-Acetyl-4-(4-

Hydroxyphenyl)Piperazi

ne

Xylene

100

1 0.95 95 95 %

Methanol 2.50 2.38 237.50 95 %

2.

1-(2-Chloroethyl)-4-(3-

Chlorophenyl)

Piperazine

Xylene

100 1.5 1.43 142.5 95 %

Methanol 2.5 2.38 237.5 95 %

3.

1,1-Dimethyl 1-

Piperazine Carboxylate

(BOC Piperazine)

Xylene

100

2.23 2.13 212.6 96 %

Methanol 2.50 2.38 238.10 95 %

4.

1-

Hydroxyethylethoxypip

erazine (HEEP)

Toluene

100

1 0.95 95 95 %

Methanol 1.20 1.15 115 96 %

5. 1-(4flurophenyl)

Piperazine

Iso

Propyl

alcohol

100 4 3.80 380 95 %

6. 1-Benzylpiperazine Toluene 100 1 0.90 90 90 %

7. Bis Chloro Ethyl Amine

Hcl

Ethylene

Dichlorid

e

100 4.39 4.21 420.96 96 %

8.

2,4,6

TrimethoxyBenzaldehy

de

Methanol 20 0.67 0.64 12.80 96 %

9.

3,4

DihydroxyBenzaldehyd

e

Acitic

Acid 20 1.25 1.19 23.80 95 %

10

.

(N:N di-sec-butyl)

peraphenylenediamine

Methyl

Ethyl

Keton

400 1.55 0.86 344.40 55 %

11

.

N:N-BIS(1:4 Dimethyl

pentyl)

PeraphenyleneDiamine

Methyl

iso amyl

Ketone

400 1.65 0.90 358.00 55%


� Provision of mechanical seal in pump.

� Regular inspection of tank roof seals.

� Adequate measures for the minimization/prevention of the fugitive emission.

� Regular maintenance of valves, pumps and other equipment to prevent leakage.

� Entire process to be carried out in the closed reactor with proper maintenance of

temperature.

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Page 51 of 167

� Regular periodic monitoring of work area to check the fugitive emission.

� Adequate stack heights as per the GPCB estimation will be provides at all locations to

reduce GLCs of pollutants.

� Air Pollution Control System will be installed in the plant.


Storage details Name of major

Hazardous chemicals

Remarks

Storage tanks Ethylene Dichloride --

Bags Sodium hydroxide ---

Storage Tanks

Acetic anhydride --

Storage Tanks Acetic acid --

Storage Tanks Toluene --

Drums Thionyl chloride --

Cylinder Hydrogen --

Drums Benzoyl chloride --

Storage Tanks Hydrochloric Acid --

Storage Tanks Isopropyl alcohol --

Storage Tanks Hydrogen bromide --

Drums Phosphoric Acid --

� Applicability of PESO: Unit will obtain PESO Certificate after getting CTE.


Jyoti Om Chemical Research Centre Pvt. Ltd. during SEAC meeting dated 16/04/2019.

• Committee noted that this is a new unit proposes synthetic organic chemical manufacturing at

GIDC, Dahej-II.

• The Process effluent stream from the plant will be segregated into two parts—High COD/High

TDS and Low COD stream. The High COD /High TDS stream will be treated with Multi effect

evaporator and the low COD effluent generated from Multi effect evaporator will be sent to ETP

collection tank with the other Low COD effluent streams. Low COD effluent stream from various

production plants and utility block is first collected in Stripper & Equalization tanks and treated in

in-house ETP followed by sand filter and Activated carbon filter after that 45 KLD wastewater

send to CETP, Dahej.

• Cyclone Separator + Bag filter + water scrubber will be provided as APCM with boiler and TFH.

of 167


Page 52 of 167

Alkali scrubber will be provided as APCM with reactor vent.

• Hazardous waste management is addressed.






1. Justification of quantity of ETP sludge and MEE salt against treatment of industrial effluent.

2. Adequacy assessment report of ETP, RO & MEE and feasibility of report of reuse of treated

industrial effluent for industrial purpose within premises.





report.






form.





shall endeavor prevention of losses of solvents to the best minimum extent.







2006.


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10 SIA/GJ/IND2/33580/2019 M/s. Filatex India Limited

Plot No. D-2/6-A, Dahej GIDC-2, Village Jolva,

Tal.: Vagra, Dist.: Bharuch.

Screening &

Scoping

Category of the unit: 1(d)

Project status: Modernization/Modification





• This is existing unit engaged in mfg Synthetic Fibres with Gas based CPP and now applied forCoal

based CPP as tabulated below.

Sr.

no.

Name of the

Products

CAS

no. /

CI no.

Quantity (MT/Month) End-use

of the

products

Existing Prop

osed Total

Permissible Installed

1 POY/FDY/DTY

(Partially Oriented

Yarn/ Fully Drawn

Yarn/ Draw

Texturising Yarn)

-

45604.17

25854.17 0 45604.17 Textile

Industry

2 Intermediate

Products

(Polyester chips)

- 10645.83 10645.83 0 10645.83

Textile Industry/c

aptive consumpti

on

3 Gas Engine

based captive

Power plant

- 38.02 MW 8.01 MW

(2.67 MW x 3)

-30.01 8.01 MW

(2.67 MW x 3)

Captive Use

4 Coal based captive Power plant

- 0 0 30

MW 30 MW

Captive Use

• The project falls underCategory B of project activity1(d) asper the schedule of EIA Notification 2006.


• Salient features of the project including Water, Air and Hazardous waste management:

Sr.

no

Particulars Details

A Total cost of Proposed Project Existing:1500

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Page 54 of 167

(Rs. in Crores): Proposed:160

Total: 1660

B Total Plot area

( sq. meter)

Existing: 2,60,292.84 Sq. m.

Proposed: 0 Sq. m.

Total: 2,60,292.84 Sq. m.

Green belt area

( sq. meter)

Existing: 32,109 Sq. m.

Proposed: 8842 Sq. m.

Total: 40,951 Sq. m.*

*32,225 sq. m. inside pant premises +

8726 sq. m. outside plant premises

C Employment generation Existing:1200

Proposed: 800

Total: 2000

D Water

i

Source of Water Supply(GIDC Bore well,

Surface water, Tanker supply etc...)

Dahej GIDC

Status of permission from the concern authority. Provisional permission is obtained for

additional water requirement


Existin

KLD

Proposed (Additional) KLD

Total after Modernization KLD

Remarks

(A) Domestic 40 473 513

Proposed quantity includes requirement for emergency housing and additional manpower requirement.

(B) Gardening

52 36 88

(C) Industrial

Process 150 0 150

DM Plant In 235 210 445

Boiler 106 170 276

Other- Cutter 14 0 14

Other- Spin oil 92 0 92

Softener Plant In 3982 210 4192 2789 fresh + 1403 recycled

Cooling 3908 198 4106

Scrubber/Coal/ash suppression

378 22 400 400 RO reject will be reused

Industrial Total 4745 442 5187

Grand Total

(A+B+C) 4837* 951 5788**

*Fresh 3664.6 + Recycled 1172.4 **Fresh 3985 + Recycled 1803

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Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Modernization

KLD

Remarks

(A) Domestic 24 410 434

(B) Industrial

Process 450 0 450

Washing 0 0 0

Boiler 8 120 128

Cooling 586 48 634

Others (DM Plant reject)

23 40 63

Others (Softener Plant reject)

74 12 86

Others (Spin oil)

8 0 8

Total Industrial waste

water

1149 220 1369


[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..

� Two ETPs with capacity of 400 KLD and 800 KLD having primary, secondary and

tertiary treatment followed by RO.


� Cooling blow down stream will be segregated and treated in RO.


Management of waste water keeping in view direction under section 18 (1) (b) of the Water

(Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of

CETP.

� Not Applicable


� Total domestic and industrial waste water except cooling blow down will be treated

in ETP having Primary, Secondary and tertiary treatment followed by RO. While

cooling blow down will be treated in RO. Total RO permeate will be recycled and

RO reject will be reused.

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Page 56 of 167


Domestic: Domestic effluent will be treated in ETP followed by RO and treated water will

be reused.

Industrial: Industrial effluent will be treated in ETP followed by RO and treated water will be reused.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF

etc.

Name of Common facility (CF)(For waste water treatment)

� Not Applicable



-



[Source of reuse & application area]

Total reusePP.KLD

-

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Page 57 of 167

Source of

waste water

for reuse

with quantity

in KLD (From

where it is

coming)

Application

area with

quantity in

KLD (Where

it is used)

Characteristics

of waste water

to be reused

(COD, BOD,

TDS etc.)

Remarks regarding feasibility

to reuse i.e.

RO Reject Scrubber-123 KLD and Coal/Ash suppression-277 KLD

COD – <100 mg/l BOD – <30 mg/l TDS – <6000 mg/l

High TDS water will improve efficiency of scrubber attached with TFH in which coal is being used as fuel and it is completely feasible to use for coal and ash suppression.

RO Permeate Softener plant – 1403 KLD

COD – <100 mg/l BOD – <30 mg/l TDS – <400 mg/l

It is completely feasible to use RO permeate in softener plant.

E Air



etc.

Existing & Proposed

-

Sr.

no.

Source of

emission

With Capacity

Stack

Height

(meter)

Type of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

Existing

1 Gas engine* (2.67 MW)

30.5 Natural

Gas 6666.7

SCM/day

SPM SO2 NOX

Natural Gas is used as fuel, adequate stack height is provided.

2 Gas engine (2.67 MW)

30.5 Natural

Gas

6666.7

SCM/day

SPM SO2 NOX


3 Gas engine (2.67 MW)

30.5 Natural

Gas

6666.7

SCM/day

SPM SO2 NOX


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4

TFH (11 Million Kcal/hr)

50 Coal

52.5 TPD

SPM SO2 NOX

Multi cyclone dust collector followed by wet film separator


52.5 TPD

TFH Stand by (11 Million Kcal/hr)

52.5 TPD

5


50 Coal

52.5 TPD

SPM SO2 NOX

Electrostatic Precipitator (ESP)


52.5 TPD

TFH Stand by (11 Million Kcal/hr)

52.5 TPD

6 D. G. Set (1250 KVA)

11 Diesel 68 Lit/day SPM SO2 NOX

Adequate stack height is provided

7 D. G. Set (1000 KVA x 6 Nos.)

11 each

Diesel 332

Lit/day

SPM SO2 NOX

Adequate stack height is provided

Proposed

1

Boiler of 30 MW Coal based power plant (125 TPH)

78

Imported Coal / Mixture of 70% importe

d & 30%

Lignite

518 TPD /

570 TPD

SPM SO2

NOX

Electrostatic Precipitator (ESP)

* EC was obtained for 38.02 MW gas engine based CPP with 12 nos. of engines having 208000 SCM/day natural gas consumption. 9 nos. of gas engine with total sanctioned capacity of 30.01 MW will replaced by proposed coal based CPP.

-


Existing & Proposed

- No process gas emission from existing and proposed activities. -


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Page 59 of 167

� Coal and Ash handling system will be provided. Coal will be stored in closed yard

while ash will be stored in silos. Adequate water will be sprinkled for Coal/ash

suppression.

� Hazardous waste will be stored at designated storage area which will reduce the

fugitive emission.

F Hazardous waste

(As per the Hazardous and Other Wastes (Management and Transboundary Movement)

Rules 2016.

Existing & Proposed

i

Sr.

no.

Type/Name

of

Hazardous

waste

Specific

Source of

generation

(Name of

the Activity,

Product

etc.)

Categor

y and

Schedul

e as per

HW

Rules.

Quantity

(MT/Annum)

Management

of HW

Existing Proposed Total

1 Discarded Containers

Raw material storage area

33.1 50 0 50

Collection, storage and

send to authorized recycler.

2 Used oil

Plant Machineries,

DG Set, Coal based CPP

5.1 10 10 20


reuse as lubricants in

the machineries

within the premises or

send to authorized re-

processors

3 ETP sludge ETP 35.3 100 220 320


sent to TSDF site.

4 D. M.

Resins

DM plant for water

treatment 35.2 0.5 0.4 0.9


sent to TSDF site.

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5 Fly Ash

TFH and boiler of

Coal based CPP

- 7665 22630 30295

Collection, storage and Sent to brick manufacturer

or cement manufacturer

6 Bio-Medical

Waste Dispensary - 0 0.002 0.002


Sent to Authorized

Common Bio-Medical Waste

Facility

-


(For HW management)

Saurashtra Enviro Projects Private Limited,

Kutch.

Membership Certificate No: 1200000328

iii Details of Non-Hazardous waste & its

disposal(MSW and others)

30295 TPA Fly Ash will be collected, stored

and sent to brick manufacturer.


i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents

etc. (Details in Table Format)

� None




Hazardous chemicals

Remarks

Storage tanks - -

Drum/Barrel storage - -

Coal Yard Coal

� Applicability of PESO : No

• PP was called for pres Technical presentation was made by the project proponent along with

their consultant/expert Envision Enviro Technologies Pvt. Ltd., Surat during SEAC meeting

dated 16/04/2019.

• Committee noted that this proposal is for modernization through Fuel/Technology change of

CPP. There will be no increase in production quantity of POY/FDY/DTY (Partially Oriented Yarn/

Fully Drawn Yarn/ Draw Texturizing Yarn) and POY/FDY/DTY Chips.

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• Total domestic and industrial waste water except cooling blow down will be treated in ETP

having Primary, Secondary and tertiary treatment followed by RO. While cooling blow down will

be treated in RO. Total RO permeate will be recycled and RO reject will be reused in APCM.

• ESP will be provided with proposed Steam Boiler of 30 MW Coal based power plant. Imported

Coal / Mixture of 70% imported & 30% Lignite will be used as fuel in it.

• EC was obtained for 38.02 MW gas engine based CPP with 12 nos. of engines having 208000

SCM/day natural gas consumption. 9 nos. of gas engine with total sanctioned capacity of 30.01

MW will replaced by proposed coal based CPP.


• After detailed discussion regarding the project, the following Terms of Reference were

prescribed for EIA study to be done covering 10 Km radius from the project boundary

including public hearing.

1. Executive summary of the project – giving a prima facie idea of the objectives of the proposal,

use of resources, justification, etc. In addition, it should provide a compilation of EIA report

including EMP and the post-project monitoring plan in brief.


Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be

made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities


report.


make the project energy-efficient through of energy efficient devices and adoption of modes of

alternative eco-friendly sources of energy like solar water heater, solar lighting etc. Measures

proposed for energy conservation.


form.

5. Present land use pattern of the study area shall be given based on satellite imagery.

6. Geological features and geo-hydrological status of the study area.

7. Demarcation of proposed activities in lay out of the existing premises. Provision of continuous

unobstructed peripheral open path within the project area for unobstructed easy movement of

the emergency vehicle / fire tenders without reversing back. Mark the same in the plant layout.

8. Proposal for air cooled condensers instead of water cooled condensers in order to reduce the

raw water requirement.

9. Technical details of the proposed power plant along with details of strategy for

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implementationreuse / recycle and other cleaner production options for reduction of wastes.

Generation of waste gases and utilization of waste heat have to be set out.

10. Assessment of source of the water supply with adequacy of the same to meet with the

requirements for the project. Copy of letter of permission obtained from the concerned authority

for supply of additional raw water for the proposed activities.

11. Action plan for complete ZLD for proposed CPP.

12. Application wise break-up of treated effluent quantity to be recycled / reused in various

applications like sprinkling on roads, coal storage yard etc.

13. Detailed water balance (including reuse-recycle, if any) along with qualitative and quantitative

analysis of each waste stream to be generated from all sources including Boilers, Cooling

Towers, D.M. Plant etc. Details of methods to be adopted for the water conservation.

14. Details of the treatment facilities proposed for the effluent to be generated from the power plant

including existing project. Details of the ETP units including its capacity (KL/day), size of each

unit, retention time and other technical parameters and details about up-gradation in the existing

ETP (if any proposed) to take care of the wastewater to be generated from the proposed

activities.

15. Characteristics of untreated and treated wastewater. A detailed effluent treatability study vis-à-

vis the adequacy and efficacy of the treatment facilities proposed for the wastewater to be

generated along with adequacy and efficacy report. The characteristic on which treatability is

based shall also be stated.

16. Site-specific meteorological data including temperature, relative humidity, hourly wind speed and

direction and rainfall shall be provided.

17. Anticipated environmental impacts due to the proposed project/production may be evaluated for

significance and based on corresponding likely impacts VECs (Valued Environmental

Components) may be identified. Baseline studies may be conducted within the study area of 10

km for all the concerned/identified VECs and likely impacts will have to be assessed for their

magnitude in order to identify mitigation measures.

18. One complete season base line ambient air quality data (except monsoon) to be given along

with the dates of monitoring. The parameters to be covered shall be in accordance with the

revised National Ambient Air Quality Standards as well as project specific parameters. Locations

of the monitoring stations should be so decided so as to take into consideration the pre-

dominant downwind direction, population zone and sensitive receptors. There should be at least

one monitoring station in the upwind direction. There should be at least one monitoring station

in the pre dominant downwind direction at a location where maximum ground level concentration

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Page 63 of 167

is likely to occur.

19. Impact of the project on the AAQ of the area. Details of the model used and the input

parameters used for modeling should be provided. The air quality contours may be plotted on a

location map showing the location of project site, habitation, sensitive receptors, if any. The

wind roses should also be shown on this map. Air quality modeling to be carried out considering

the partial and complete failure of the ESP.

20. Quantity of the fuel requirement, its source and transportation, storage, handling and

management along with the environmental management to be adopted for this. Fuel analysis to

be provided (sulphur, ash content and heavy metals including Pb, Cr, As and Hg).

21. A confirmed fuel linkage along with the supportive documents of long term supply of coal for the

project requirements should be provided.

22. Specific details of (i) Details of the utilities required (ii) Quantity and characteristics of each fuel

along with analysis report and its source (iii) Flue gas emission rate from each utility (iv) Air

Pollution Control Measures proposed to each of the utility along with its adequacy.

23. Technical details of ESP proposed to be installed as air pollution control system along with its

adequacy, details of its operational controls with DCS, system for online monitoring of the

pollutants from the stack etc. Details of provisions to be kept in ESP to ensure that in any case

the air emission does not cross the GPCB norms including provision of standby field in the ESP,

preventive maintenance, failure / tripping control system, guarantee from the ESP supplier,

alternative arrangements in case of the failure / tripping of the ESP etc. ESP should be

designed to achieve GPCB norms at the outlet.

24. List of all the sources of fugitive emission. Detailed plan for prevention and control of fugitive

emission / dusting at each and every stage of fuel handling including unloading / loading at port,

transportation from port to plant, unloading / loading / stacking / conveyance / transfer at plant

etc. Detailed specifications and schematic diagram of water sprinkling system including number

of sprinklers to be installed, pipe diameter and nozzle diameter of the sprinklers, quantity of

water to be consumed by sprinklers etc.

25. Impact on local transportation infrastructure due to the project such as transportation of fuel, ash

etc. Base line status of the existing traffic, projected increase in truck traffic as a result of the

project in the present road network, impact on it due to the project activities, carrying capacity of

the existing roads and whether it is capable of handling the increased load. Arrangement for

improving the infrastructure like road etc. if any should be covered. Whether any additional

infrastructure would need to be constructed and the agency responsible for the same with time

frame.

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26. Details and time bound program for installation of online monitoring system in the existing as

well as proposed plants for monitoring of the pollutants from the stacks and process vents with a

software and an arrangement to reflect the online monitored data on the company's server,

which can be accessed by the GPCB on real time basis.

27. Provision of Continuous Ambient Air Quality Monitoring Station [CAAQMS] within premises, with

an arrangement to reflect monitored data on the company’s server, which can be accessed by

the GPCB on real time basis.

28. Details of measures proposed for the noise pollution abatement and its monitoring.

29. Details of management of the hazardous wastes to be generated from the project stating detail

of storage area for each type of waste, its handling, its utilization and disposal etc. How the

manual handling of the hazardous wastes will be minimized.

30. Detailed plan of ash evacuation, handling, storage and utilization should be provided.

Undertaking stating that ash pond shall not be constructed and it shall be stored in closed silos

only should be incorporated.

31. Details of seismic design aspects to be adhered to in the project.

32. Technical details of conveyor belts and mitigation measures to ensure that there will be no dust

emission from conveyor belts.

33. Details of proposed disposal of solid wastes that may generate due to spillage of materials.

34. Specific safety measures proposed at storage yard / warehouse and conveyor belts.

35. Details of firefighting system including provision for flame detectors, temperature actuated heat

detectors with alarms, automatic sprinkler system, location of fire water tanks & capacity,

separate power system for firefighting, details of qualified and trained fire personnel& their job

specifications, nearest fire station &time required to reach the proposed site. Submit line

diagram of the fire hydrant network.

36. Copy of membership certificate of Common Environmental Infrastructure like TSDF, if any taken,

should be incorporated.

37. Details of 100% fly ash utilization plan as per latest fly ash Utilization. Notification of GOI along

with firm agreements / MoU with contracting parties including other usages etc. shall be

submitted. The plan shall also include disposal method / mechanism of bottom ash.

38. A detailed EMP including the protection and mitigation measures for impact on human health

and environment as well as detailed monitoring plan and environmental management shall

proposed for implementation and monitoring of EMP. The EMP should also include the concept

of waste-minimization, recycle/reuse/recover techniques, energy conservation, and natural

resource conservation. Total capital cost and recurring cost/annum earmarked for environment

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pollution control measures.

39. Occupational health impacts on the workers and mitigation measures proposed to avoid the

human health hazards along with the personal protective equipment to be provided to the

workers. Provision of industrial hygienist and monitoring of the occupational injury to workers as

well as impact on the workers. Plan for periodic medical checkup of the workers exposed.

Details of work zone ambient air quality monitoring plan as per Gujarat Factories Rules.

40. Risk assessment including prediction of the worst-case scenario and maximum credible accident

scenario related to fire and explosion issues due to storage and use of fuel should be carried

out. The worst-case scenario should take into account the maximum inventory of storage at site

at any point in time. The risk contours should be plotted on the plant layout map clearly showing

which of the activities would be affected in case of an accident taking place. Based on the

same, proposed safeguard measures including On-Site / Off-Site emergency plan should be

provided. Measures to guard against fire hazards including details of automatic fire detection

and control system &detailed fire control plan showing hydrant pipeline network, provision of DG

Sets, fire pumps, jockey pump, toxic gas detectors etc. should also be provided.

41. Provisions for water supply, fuel (kerosene or cooking gas), lighting, sanitation etc. to the

construction work force so as to avoid felling of trees/mangroves and pollution of water and the

surroundings. Details of personal protective equipments to be provided to construction workers

at the site.

42. Submit checklist in the form of Do’s & Don’ts of preventive maintenance, strengthening of HSE,

manufacturing utility staff for safety related measures.

43. Public hearing shall be carried out as per the MoEFCC’s OM dated 27/04/2018. A tabular chart

for the issues raised and addressed during public hearing/consultation and commitment of the

project proponent on the same should be provided. An action plan to address the issues raised

during public hearing and the necessary allocation of funds for the same should be provided.

44. Detailed five year greenbelt development program including annual budget, types &number of

trees to be planted, area under green belt development [with map], budgetary outlay; along with

commitment of the management to carry out the tree plantation activities outside the premises at

appropriate places in the nearby areas and elsewhere.

45. Proposal for socio-economic development activities including community welfare program most

useful in the project area for the overall improvement of the environment. Submit a detailed plan

for social corporate responsibilities, with appropriate budgetary provisions for the next five years

and activities proposed to be carried out; specific to the current demographic status of the area.

46. Plan for compliance of the EP Rules and CREP guidelines for the proposed power plant.

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47. Compliance status of the existing unit with respect to various conditions given in the

Environmental Clearance and CC&A orders obtained for the existing plants.

48. Records of any legal breach of Environmental laws i.e. details of show- cause notices, closure

notices etc. served by the GPCB to the existing unit in last three years and actions taken then

after for prevention of pollution.

49. Copy of Environmental Clearance obtained for the existing project and a certified report of the

status of compliance of the conditions stipulated in the environmental clearance for the existing

operation of the project by the Regional Office of the MoEF&CC.

50. Details of fatal / non-fatal accidents, loss of life or man hours, if any, occurred in the existing unit

in last three years and measures proposed to be taken for avoiding reoccurrence of such

accidents in future.

51. Any litigation pending against the project and / or any direction / order passed by any Court of

Law against the project, if so, details thereof.

52. Does the company have a well laid down Environment Policy approved by its Board of

Directors? If so, it may be detailed in the EIA report. Does the Environment Policy prescribe for

standard operating process / procedures to bring into focus any infringement / deviation /

violation of the environmental or forest norms / conditions ? If so, it may be detailed in the EIA.

53. What is the hierarchical system or administrative order of the company to deal with the

environmental issues and for ensuring compliance with the EC conditions. Details of this system

may be given.

54. Does the company have a system of reporting of non-compliances / violations of environmental

norms to the Board of Directors of the company and / or shareholders or stakeholders at large?

This reporting mechanism should be detailed in the EIA Report.

55. Certificate of accreditation issued by the NABET, QCI to the environmental consultant should be

incorporated in the EIA Report.

56. An undertaking by the Project Proponent on the ownership of the EIA report as per the

MoEF&CC OM dated 05/10/2011 and an undertaking by the Consultant regarding the prescribed

TORs have been complied with and the data submitted is factually correct as per the MoEF&CC

OM dated 04/08/2009.

57. All documents to be properly referenced with index and continuous page numbering.

58. PP shall ensure participation of people during Public Hearing with equality in gender so as to

encourage woman participation in Public hearing & at the same time their issues shall also be

given weightage.

59. A tabular chart with index for point-wise compliance of above.

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60. Adequacy assessment report of ETP. Feasibility report of reuse of treated industrial effluent for

industrial purpose within premises.

61. Adequate APCM for SOx control incase of lignite used.

62. Compliance of MoEF & CC Notification on dated 28th June, 2018.

63. To justify quantity of ETP sludge generation against treatment of industrial effluent.

64. Provide ESP with stack no. 4 connected to 3 TFH (Each TFH capacity (11 Million Kcal/hr) and

coal consumption in each TFH 52.5 TPD).

• The above mentioned project specific TORs/additional TORs and the model TORs available in

the MoEFCC’s sector specific EIA Manual for ‘Thermal Power Plants’ shall be considered as

generic TORs for preparation of the EIA report in addition to all the relevant information as per

the generic structure of EIA given in Appendix III in the EIA Notification, 2006.

• The draft EIA report shall be submitted to the Gujarat Pollution Control Board for conducting the

public consultation process as per the provisions of the EIA Notification, 2006.


http://environmentclearance.nic.in/along with final EIA report.

Validity of ToR:

• The ToRs prescribed for the project will be valid for a period of three years for

submission of EIA & EMP report. ToR will lapse after three years from the date of issue.

• The period of validity could be extended for a maximum period of one year provided an

application is made by the applicant to the Regulatory Authority, at least three months

before the expiry of valid period together with an updated Form-I, based on proper

justification and also recommendation of the SEAC.

11 SIA/GJ/IND2/33751/2019 M/s. Pro-Life Bio-Chemical Industries Pvt. Ltd

Plot No. 2921 & 2922, GIDC Estate-Panoli, Panoli, Dist.: Bharuch.

Screening & Scoping







• This is existing API manufacturing unit and now proposes for manufacturing of Dyes & Dyes

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Intermediates as tabulated below:

Sr.

no.

Name of the

Products

CAS no. /

CI no.

Quantity, MT/Month End-use of the

products Existing Proposed Total

1 Diclofenac Sodium

15307-79-6 3 --- 3 Pharmaceutical

Intermediate

2 Piroxicam 36322-90-4 0.2 --- 0.2 Anti- inflammatory

drug

3 Methoxy Tetralone


Intermediate

4 Palmitoyl Chloride


Intermediate

5 DehydroThio-P-Toluidine

92-36-4 2 --- 2 Dye and Dyes Intermediates

6 3,4 Di Chloro Benzyl Chloride

102-47-6 3 --- 3 Dye and Dyes Intermediates

7 Acid Orange 7 633-96-5 ---

30 30

Dye and Dyes Intermediates

8 Acid Red 88 1658-56-6 --- Dye and Dyes Intermediates

9 Acid Metanilic Yellow

587-98-4 --- Dye and Dyes Intermediates

10 Acid Scarlet 3R 2611-82-7 --- Dye and Dyes Intermediates

11 Acid Yellow 1 46-70-8 --- Dye and Dyes Intermediates

12 Disperse Orange 25

31482-56-1 ---

30 30


13 Disperse Orange 44


14 Disperse Red 54 6021-61-0 --- Dye and Dyes Intermediates

15 Disperse Red 73 16889-10-4 --- Dye and Dyes Intermediates

16 Disperse Violet 93


17 Disperse Violet 99


18 Disperse Yellow 241


19 Reactive Black 5 17095-24-8 ---

20 20


20 Reactive Orange 16


21 Reactive Red 194


22 Reactive Red 195


23 Direct Yellow 27 10190-68-8 --- 10 10 Dye and Dyes Intermediates

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24 Direct Violet 35 6227-20-9 --- Dye and Dyes Intermediates

25 Direct Violet 51 5489-77-0 --- Dye and Dyes Intermediates

26 Direct Yellow 132


27 HC Blue 2 33229-34-4 --- Dye and Dyes Intermediates

28 HC Blue 16 502453-61-4 --- Dye and Dyes Intermediates

29 HC Yellow 4 59820-43-8 --- Dye and Dyes Intermediates

30 Basic Green 1 633-03-4 ---

30 30


31 Basic Green 4 569-64-2 --- Dye and Dyes Intermediates

32 Basic Violet 1 8004-87-3 --- Dye and Dyes Intermediates


34 Basic Orange 1 4438-16-8 --- Dye and Dyes Intermediates


36 Basic Blue 99 68123-13-7 --- Dye and Dyes Intermediates

37 Basic Brown 16 26381-41-9 --- Dye and Dyes Intermediates

38 Basic Brown 17 68391-32-2 --- Dye and Dyes Intermediates

39 Basic Red 76 68391-30-0 --- Dye and Dyes Intermediates

40 Basic Yellow 57 68391-31-1 --- Dye and Dyes Intermediates

41 Basic Blue 124 67846-56-4 --- Dye and Dyes Intermediates


43 Basic Red 51 77061-58-6 --- Dye and Dyes Intermediates


45 Basic Yellow 87 68259-00-7 --- Dye and Dyes Intermediates

46 Fast Scarlet G Base

99-55-8 ---

30 30


47 Fast Orange GC Base


48 Fast Yellow GC Base


of 167


Page 70 of 167

49 Fast Scarlet RC Base


50 Fast Red B Salt 56315-29-8 --- Dye and Dyes Intermediates

51 Fast Orange GC Salt


52 Fast Yellow GC Salt


53 Fast Red RC Salt


54 Fast Red GL Salt


55 Fast Red 3GL Salt


56 Fast Scarlet R Salt


57 Fast Orange RD Salt


58 Solvent Black 27 12237-22-8 ---

20 20


59 Solvent Orange 162


60 Solvent Red 127 61969-48-0 --- Dye and Dyes Intermediates

61 Solvent Blue 63 6408-50-0 --- Dye and Dyes Intermediates

62 Naphthalene 1,5 Di Sulfonic Acid

81-04-9 --- 30 30 Dye and Dyes Intermediates

Total 12.2 200 212.2




Sr.

no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing:0.96 Crores

Proposed:2.5 Crores

Total: 3.46 Crores

B Total Plot area

( sq. meter)


Proposed: 5,000 Sq. m.

Total: 10,000 Sq. m.

Green belt area

( sq. meter)

Existing: 3300 Sq. m.

Proposed: 0 Sq. m.

Total: 3300 Sq. m.

of 167


Page 71 of 167

C Employment generation Existing:20 Nos.

Proposed:20 Nos.

Total:40 Nos.

D Water

i



GIDC water Supply

Status of permission from the concern authority. GIDC Water supply letter will be

provided at the time of EIA.


Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1.5 4.0 5.5

(B) Gardening 2.0 3.0 5.0

(C) Industrial

Process 1.8 59.0 60.8

Washing 2.5 2.0 4.5

Boiler 1.0 6.0 7.0

Cooling 1.0 9.0 10.0

Others 0.2 1.0 1.2 Scrubber

Industrial Total 6.5 77.0 83.5

Grand Total (A+B+C) 10.0 84.0 94.0





Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 1.0 2.0 3.0

(B) Industrial

Process 1.8 70.0 71.8

Washing 2.5 2.0 4.5

497

Boiler

Cooling

Others

Total Industrial waste water

iv Treatment facility within premises with


� For Existing:-In-house ETP (Primary, Secondary, Tertiary)+Send to PETL� For Proposed :-Primary ETP + In� After Proposed Expansion :


� Effluent is generated from process, which are subjected to Intreatment additional waste water will be treated into the primary ETP and then send to (in-house) MEE for further treatment. Aftebe recycled within the plant premises.

� Effluent Treatment plant Details.

� Existing ETP


of 167

0.2 1.0 1.2

0.3 3.0 3.3

0.2 0.0 0.2

Total Industrial waste water 5.0 76.0 81.0

Treatment facility within premises with capacity

house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..

house ETP (Primary, Secondary, Tertiary)+Send to PETLPrimary ETP + In-house MEE

After Proposed Expansion :- Capacity of ETP:- 90 KLD


Effluent is generated from process, washing, and boiler blow down, Cooling bleed off which are subjected to In-house ETP (Primary, Secondary, and Tertiary). After treatment additional waste water will be treated into the primary ETP and then send to

house) MEE for further treatment. After adequate treatment, Condensed water will be recycled within the plant premises. Effluent Treatment plant Details.

Page 72 of 167

house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..

house ETP (Primary, Secondary, Tertiary)+Send to PETL

washing, and boiler blow down, Cooling bleed off house ETP (Primary, Secondary, and Tertiary). After

treatment additional waste water will be treated into the primary ETP and then send to r adequate treatment, Condensed water will

497

� Proposed ETP


Management of waste water keeping in view

and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP

1. Existing: i. For the existing production capacity, the generated effluent is collected, treated into

ETP and then discharge to PETLexisting discharge permission of the unit will be continue.

2. Proposed: i. For proposed expansion, Industrial waste water will be treated into the primary ETP

and then send to (inCondensed water will be recycled within the plant premises.


� For Existing:-Not Applicable

� For Proposed:- For proposed expansion,

the primary ETP and then send to (in

adequate treatment, Condensed water will be recycled within the plant premises.

Hence unit will maintain ZLD for proposed Expansion.


Domestic: Domestic waste water will be disposed in to Septic tank/Soak pit.

Industrial: Existing:

� For the existing production capacity, the generated effluent is collected, treated into ETP further treatment. After expansion existing discharge permission of the unit will be continue.

Proposed:

� For proposed expansion, Industrial waste water will be treated into the primary ETP and then send to (inAfter adequate treatment, Condensed water will be recycled within the plant premises.


of 167




For the existing production capacity, the generated effluent is collected, treated into and then discharge to PETL-CETP for further treatment. After expansion

existing discharge permission of the unit will be continue.

For proposed expansion, Industrial waste water will be treated into the primary ETP and then send to (in-house) MEE for further treatment. After adequate treatment, Condensed water will be recycled within the plant premises.


Not Applicable

For proposed expansion, Industrial waste water will be treated into

the primary ETP and then send to (in-house) MEE for further treatment. After


Hence unit will maintain ZLD for proposed Expansion.


Domestic waste water will be disposed in to Septic tank/Soak pit.

For the existing production capacity, the generated effluent is collected, treated into ETP and then discharge to PETLfurther treatment. After expansion existing discharge permission of the unit will be continue.

Proposed:

For proposed expansion, Industrial waste water will be treated into the primary ETP and then send to (in-house) MEE for further treatment. After adequate treatment, Condensed water will be recycled within the plant premises.

Page 73 of 167

direction under section 18 (1) (b) of the Water (Prevention

.

For the existing production capacity, the generated effluent is collected, treated into CETP for further treatment. After expansion

For proposed expansion, Industrial waste water will be treated into the primary ETP MEE for further treatment. After adequate treatment,

Industrial waste water will be treated into

house) MEE for further treatment. After



For the existing production capacity, the generated effluent is and then discharge to PETL-CETP for

further treatment. After expansion existing discharge permission of the

For proposed expansion, Industrial waste water will be treated into the MEE for further treatment.

After adequate treatment, Condensed water will be recycled within the

497


etc.

Name of Common facility (CF) (For waste water

� For Existing: - PETL: Panoli Enviro Technology Limited

� For Proposed:-Generated additional waste water send to

treatment. After adequate treatment, Condensed water will be recycled within the plant

premises.



Membership Certificate of waste water [PETL] is attached as


[1]EXISTING WATER FLOW DIAGRAM:

[2]AFTER EXPANSION WATER FLOW DIAGRAM:


of 167

In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF

Name of Common facility (CF) (For waste water treatment)

PETL: Panoli Enviro Technology Limited-CETP

Generated additional waste water send to (in-house) MEE for further


mbership of Common facility (CF)


Membership Certificate of waste water [PETL] is attached as Annexure-II


[1]EXISTING WATER FLOW DIAGRAM:-

[2]AFTER EXPANSION WATER FLOW DIAGRAM:-

Page 74 of 167


house) MEE for further


II


497



Total reuse:65 KLD

-

Source of waste

water for reuse with

quantity in KLD

(From where it is

coming)

MEE(Condensed

Water)

[65 KL/Day]

• Condensed water (65 KLD) will be recycle in process.

E Air



Existing & Proposed

-

Sr. no.

Source of emission

With Capacity


of 167

Reuse/Recycle details (KLD)



Application

area with

quantity in

KLD (Where it

is used)

Characteristics of

waste water to be

reused (COD, BOD,

TDS etc.)

In Process,

Washing

[65 KL/Day]

pH

TDS (mg/lit)

TSS (mg/lit)

COD (mg/lit)

Condensed water (65 KLD) will be recycle in process.


Stack Height (meter)

Type of Fuel

Quantity of Fuel MT/Day

Type of emissions

i.e. Air Pollutants

Page 75 of 167

Remarks

regarding

feasibility

to reuse i.e.

6-8

300-500

100-150

100-400


emissions

Air Pollution Control

Measures (APCM)

of 167


Page 76 of 167

Existing

1. Boiler

[Cap. 1 TPH] 12

Natural Gas

3000 Nm3/Day

PM SO2 NOx

Adequate Stack Height

2. Thermic Fluid

Heater[Cap. 2 Lac K Cal./hr]

12

Proposed

1. Boiler

[Cap. 1 TPH] 11

Natural Gas

1200 Nm3/Day

PM SO2 NOx


2.

Thermic Fluid Heater[Cap. 2 Lac

K Cal./hr] [2 Nos.]

11

3. DG

[150 KVA] 11 Diesel

60 Lit/Day

-


Existing & Proposed

-

Sr. no.

Specific Source of emission(Name of the

Product & Process)

Type of emission


Air Pollution Control Measures (APCM)

Existing

1. Reaction Vessels HCl 13 Two Stage Water Scrubber

Proposed

1. Reaction Vessels-1 HCl 11 Two Stage Water Scrubber

2. Reaction Vessels-2 HBr 11 Two Stage Alkali Scrubber

-


� Minimum Joints & flanges

� Pumps with mechanical seals

� Proper ventilation

� Adequate PPEs

F Hazardous waste


Rules 2016.

Existing & Proposed

i

Sr

.

no

Type/Name

of

Hazardous

Specific

Source of

generation

Catego

ry and

Schedu

Quantity

(MT/Annum)

Management of

HW

of 167


Page 77 of 167

. waste (Name of

the Activity,

Product

etc.)

le as

per HW

Rules.

Existi

ng

Propo

sed

Total

1. Empty barrels/ containers/liners contaminated with hazardous chemicals /wastes

Raw Material

and Packaging

33.1 123 2097 2220 Collection, Storage, Transportation, reuse or send back to supplier or sold to Authorized Vendors.

2. Used Oil From Machinery

5.1 0.012

0.188 0.200 Collection, Storage, Transportation and sold to authorized Recyclers.

3. ETP Sludge ETP 35.3 3 1437 1440 Collection, Storage, Transportation and sent to TSDF site-BEIL-Ankleshwar.

4. MEE Salt MEE 35.3 --- 2520 2520 Collection, Storage, Transportation and sent to TSDF site-BEIL-Ankleshwar.


Process Existing: [1]Disclofenac Sodium [2]Piroxicam [3]Methoxy Tetralone

36.1 0.24 --- 0.24 Collection, Storage, Transportation, Co-Processing or disposal at CHWIF-BEIL-Ankleshwar.

6. Spent Carbon

Process Existing: [1]Disclofenac Sodium

36.2 0.6 --- 0.6 Collection, Storage, Transportation and sent to CHWIF Facility-BEIL-Ankleshwar.

7. Spent Catalyst

Process [1]Acid Yellow1 [2]All

26.5 --- 50 50 Collection, Storage, Transportation and sent to TSDF

of 167


Page 78 of 167

Disperse Dyes [3]All Direct Dyes [4]All Basic Dyes [5]Solvent Blue 63

site-BEIL-Ankleshwar.

8. Hydrochloric Acid [28-33%]

Scrubber [1]Disperse Orange 25 [2]Disperse Orange 44 [3]Reactive Black 5 [4]Reactive Orange16 [5]Reactive Red 194 [6]Reactive Red 195 [7]Direct Yellow 27 [8]Direct Violet 35 [9]Direct Violet 51

--- --- 365 365 Collection, Storage, Captive consumption for the manufacturing of product Sr. No. 7 to 16,17 to 29,31,33 to 35,37 to 45,47 to 59,61.

9. Sulfuric Acid [30-40%]

Process [1]Disperse Red 73 [2]Disperse Violet 93 [3]Disperse Violet 99

26.3 --- 256 256 Collection, Storage, Captive consumption as neutralizing agent in ETP [In-House].

10.

Acetic Acid [30-40%]

Process [1]Reactive Orange 16 [2]Basic Brown 17

--- --- 193 193 Collection, Storage, Transportation and sell to authorized end users registered under rule-9. LOI For the same is attached as Annexure IV.

11.

Sodium Bromide [30-40%]

Process [1]Basic Blue 99

--- --- 275 275 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.

of 167


Page 79 of 167

LOI For the same is attached as Annexure IV.

-


(For HW management)

Membership Certificate is attached as

Annexure-III



Not Applicable




Sr.

No. Name of Product Name of Solvent

Solvent

Quantity

(MT/Month)

Solvent

Recovered

Quantity

(MT/Month)

Percentage

Recovery

(%)

1 DiChlorofenac Sodium Ethyl Chloro Acetate 5.0 4.9 98

Toluene 5.0 4.9 98

2. Pyroxicam Methanol 0.13 0.12 96

Propanol 0.13 0.12 96

3. Di Methoxy Tetralone Ethanol 5.0 4.8 96


• Minimum joints/flanges

• Adequate Condenser

• Brine will be utilised as chilling agent

• Pumps with double mechanical seals

• Proper Ventilation

• PPEs



Storage tanks Toluene, Methanol, Ethyl Chloro Acetate, Acetic Acid

Drum/Barrel storage

1,2,4 Diazo Acid, 2 Methoxy 4 Nitro Aniline, 2,6 Di Chloro Phenol, 2-Amino-4-Nitro Phenol, 2-Amino-5-Nitro Phenol,2-Amino-Pyridine,2-Chloro Aniline, 2-Chloro-5-[Trifluoromethyl] Aniline,2-Ethyl Hexyl Amine, 2-Methoxy- 5-Nitro Aniline,3,4 Di Chloro benzoic Acid,3,4 Dichloro Aniline,3,7 Di Bromo-8-Amino-8-hydroxy(1,4)Napthaquinone-immie(1),3-Amino Phenyl Trimethyl Ammonium Chloride, 3-Amino-N,N,N-Tri Methyl Benzenenaminium Chloride,3-Chloro Aniline,3-Methyl-1-Phenyl-1H-Pyrazol-5(4H)-One,3-Pyridine Carbonitrile,4 Methyl Benzene 1, 3 Diamine, 4-[Dimethylamino] Benzaldehyde, 4-Chloro-2-Nitro

of 167


Page 80 of 167

Aniline, 4-Methyl-2-Nitro Aniline, 5-Chloro-2- Methoxy Aniline, 6 Chloro 2,4 Di Nitro Aniline, 7-Tri Methyl Amino-2-Napthol, Acetic Anhydride,Acetoactaniside, Aniline, Anti-Dusting Oil,Benzaldehyde, Beta Napthol, C-Acid, Catalyst, Chloro Acetyl Chloride,Chrominating Agent,Cyano PNA,Cynuric Chloride, Di Methoxy Naphthalene, Di Methyl Aniline, Di Methyl Sulphate, DPA,DTPTDiSA, Dye/Dyes Intermediates,Dyto DF,Emulsifier,Ethanol,Ethylcellosolve,GSalt,Gamma Acid,H2SO4,H-Acid, HCl,HNO3,KD-12,KD-22,KD-7,KD-8,Kiri Mol,Liq Ammonia,Meta Xylidine O-Sulfonic Acid,Metanilic Acid, Mono Methyl Aniline, M-PhenyleneDiamine, N-(4-Amino Phenyl Acetamide), N-(4-Amino-3-Nitro Phenyl Acetamide), NaNO2,NaOH,Naphthalene,Nitro Sulfuric Acid,N-Phenyl-J-Acid, O-Anisidine, OCPNA, Oleum,Palmitic Acid, P-Anisidine, Para Nitro Aniline, P-Formaldehyde,Phenyl Methyl Pyrozolone,Primene, Propanol, Rhodamine, Saccharin Sodium, Salicyclic Acid,Salt,SodaAsh,SodiumAcetate,SodiumBicarbonate,SodiumCarbonate,SodiumMetal,SodiumNapthionic Acid, Sodium Napthonate,Sulfanilic Acid,Sulpho Tobias Acid,Sulphur,ThionylChloride,Vinyl Sulphone Ester,ZnCl2

� Applicability of PESO : Yes


Ecopreneur Incorporateduring SEAC meeting dated 16/04/2019.

• Committee noted that this proposal is for expansion in manufacturing of Synthetic Organic

Chemicals at GIDC, Ankleshwar. PP has proposed to manufacture Dyes & Dyes Intermediates.

• For proposed expansion, Industrial waste water will be treated into the primary ETP and then

send to (in-house) MEE for further treatment. After adequate treatment, Condensed water will be

recycled within the plant premises.

• Natural gas will be used as fuel. Two stage alkali scrubber will be provided as APCM with

proposed reactors.

• Distillation residue will be sent for co-processing or CHWIF. Sodium Bromide and Acetic Acid

will be sent to actual end user having rule-9 permission. ETP sludge and MEE salt will be sent

to TSDF for landfilling.






of 167


Page 81 of 167

1. Justification of quantity of ETP sludge and MEE Salt against treatment of industrial effluent.

2. Adequacy assessment report of ETP. Feasibility report of reuse treated industrial effluent for

industrial purpose within premises.

3. To address management of Off Specification Product, Spent Aluminum Chloride and Spent

Acid Generation from API manufacturing as per the HWM Rules, 2016.











report.






form.







during unloading, storage, transportation, handling and processing of Solvents




of 167


Page 82 of 167


2006.



12 SIA/GJ/IND2/32958/2019 M/s. Reliance Chemicals

Plot No. 4794, GIDC, Industrial Estate, Ankleshwar, Dist.: Bharuch.

Screening & Scoping







• This is an existing Synthetic Organic Chemical manufacturing unit and now proposes for expansion

as tabulated below:

Sr.

no.

Name of the

Products

CAS no. /

CI no.



1 Pigment Red 23

6471-49-4 1 0.0 1 Printing , Ink Industry, Pigment Industry

2 Pigment Red 24


3 Pigment Yellow 2


4 2-Nitro P Phenylene Di Amine

5307-14-2 0.0 11.0 11.0 Dyes Intermediate

5 Diphenyl acetonitrile

86-29-3 0.0 11.0 11.0 Pharmaceutical Ind.

Total 11.0 22.0 33.0




Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: 0.45 crores

Proposed: 0.45 crores

Total: 0.90 crores

of 167


Page 83 of 167

B Total Plot area

( sq. meter)

Existing: 1000.0 Sq. m.

Proposed: 0.0 Sq. m.

Total: 1000.0Sq. m.

Green belt area

( sq. meter)


Proposed: 0.0 Sq. m.

Total: 300.0Sq. m.

C Employment generation Existing: 10

Proposed:10

Total:20

D Water

i



GIDC water supply

Status of permission from the concern authority. GIDC water supply letter will be

submit at the time of EIA.


Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1 2 3

(B) Gardening 1 1.2 2.2

(C) Industrial

Process 2.2 3.8 6.0

Washing 0.3 0.3 0.6

Boiler 0.5

1.2 1.7

Cooling 0.0 0.5 0.5

Others 0.0 1.0 1.0 Scrubber

Industrial Total

3

6.8 9.8

Grand Total (A+B+C) 5 10 15


2) Quantity to be recycled: 0.0 KLD


of 167


Page 84 of 167


Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1 2 3

(B) Industrial

Process 2.1 4.0 6.1

Washing 0.3 0.3 0.6

Boiler 0.0 0.3 0.3

Cooling 0.0 0.1 0.1

Others 0.0

0.0 0.0 Scrubbing water goes along

with By-product-NaBr.

Total Industrial

waste water

2.4 4.7 7.1



� After Expansion :-Adequate Primary ETP + ETL-CETP


� Flow Diagram of ETP is attached below.




compliance of CETP.

� For Existing, Industrial effluent is being treated in to the ETP unit and after

adequate treatment of waste water is being sent to ETL-CETP for further treatment

of 167


Page 85 of 167

and disposal.

� For Proposed, additional generated waste water will be treated into the ETP and

then send to ETL. [Enviro Technology Limited] for further treatment.

Note:

In view of the meeting held on 11/06/2018 at GPCB, Gandhinagar and based on the MOM

of that Meeting, for issuing permission for additional hydraulic load to CETP/FETP and

subsequently to its member units in Ankleshwar and Panoli area, it is proposed to discharge

the wastewater after resorting to the primary treatment and meeting with the inlet norms

prescribed to ETL-CETP if additional membership is issued to our unit based on above

mentioned GPCB policy and we are existing member of ETL since long and membership

certificate for the same is attached as Annexure.

Now, As per the recent letter issued by the Board on dated Letter No. GPCB/ANK/C-

1144/479160, dated. 19.12.2018, we are eligible to Send Industrial effluent into the ETL and

membership certificate for the same is attached in Annexure. Hence, considering the same,

we are going to apply for the discharge at ETL.


� Not Applicable



Industrial: For Existing, Industrial effluent is being treated in to the ETP unit and after

adequate treatment of waste water is being sent to ETL-CETP for further

treatment and disposal.

For Proposed, additional generated waste water will be treated into the ETP

and then send to ETL. [Enviro Technology Limited] for further treatment.

Note:

In view of the meeting held on 11/06/2018 at GPCB, Gandhinagar and based

on the MOM of that Meeting, for issuing permission for additional hydraulic

load to CETP/FETP and subsequently to its member units in Ankleshwar and

Panoli area, it is proposed to discharge the wastewater after resorting to the

primary treatment and meeting with the inlet norms prescribed to ETL-CETP if

additional membership is issued to our unit based on above mentioned GPCB

policy and we are existing member of ETL since long and membership

certificate for the same is attached as Annexure.

Now, As per the recent letter issued by the Board on dated Letter No.

of 167


Page 86 of 167

GPCB/ANK/C-1144/479160, dated. 19.12.2018, we are eligible to Send

Industrial effluent into the ETL and membership certificate for the same is

attached in Annexure. Hence, considering the same, we are going to apply for

the discharge at ETL.


etc.


� For Existing + Propose:-ETL-CETP



We are member of ETL-CETP since long and Membership certificate for the same is

attached as Annexure II.




Total reuse.- 0.0 KLD

-

E Air

of 167


Page 87 of 167



Existing & Proposed

-

Sr

.

n

o.

Source

of

emission

With

Capacity

Stack

Heig

ht

(mete

r)

Type

of

Fuel

Quantity of Fuel

MT/Day

Type of

emissio

ns i.e.

Air

Pollutan

ts

Air

Pollution

Control

Measure

s

(APCM)

Existin

g

Propos

ed Total

1.

Steam

Boiler

[0.8TPH]

10

Natur

al

Gas

88

Nm3/Da

y

190

Nm3/Da

y

278

Nm3/Da

y

PM

SO2

NOx

Adequate

Stack

height

2.

Hot Air

Generator

[2 lakh

kcal/hr.]

10

Note: - There will not requirement of additional utility only quantity of fuel will increase.


Existing & Proposed

-

Sr. no.

Specific Source of emission(Name of the

Product & Process)

Type of emission


Air Pollution Control Measures

(APCM)

Existing

There shall be no process gas emission from existing Products

Proposed

2 Reaction vessel HBr 10 Two stage Alkali

scrubber

-





� Adequate PPEs

F Hazardous waste

of 167


Page 88 of 167


Rules 2016.

Existing & Proposed

i

Sr

.

no

.

Type/Name

of

Hazardous

waste

Specific

Source of

generatio

n

(Name of

the

Activity,

Product

etc.)

Catego

ry and

Schedu

le as

per HW

Rules.

Quantity

(MT/Annum)

Management of

HW

Existi

ng

Propos

ed

Tot

al

1. Empty barrels/ containers/liners contaminated with hazardous chemicals /wastes

Raw Material

and Packaging

33.1 5.0 5.0 10 Collection,

Storage,

Transportation,

Decontamination,

reuse or send

back to supplier,

and sold to

Authorized

Vendors.

2. Filter & Filter Bags from Centrifuge

Filtration 35.1 -- 0.15 0.15 Collection, Storage, Transportation, disposal at CHWIF-BEIL-Ankleshwar.

3. Used Oil From

Machinery

5.1 0.015 0.015

0.003

Collection, Storage, Transportation and sold to authorized Recyclers.

4. ETP Waste From ETP 35.3 --- 126 126 Collection, Storage, Transportation and sent to TSDF site.


Process [1] 2-Nitro-P-Phenylene

20.3 --- 14.5 14.5 Collection, Storage, Transportation, Co-Processing or

of 167


Page 89 of 167

Di Amine [2] Diphenyl acetonitrile

sent to CHWIF-BEIL- Ankleshwar.

6. Spent Solvent

Process [1] 2-Nitro-P-Phenylene Di Amine [2] Diphenyl acetonitrile

26.4 --- 1183 1183

Collection, Storage, Recovery and recycle for manufacturing of product.

7. Sodium Bromide [20-25 %]

Process [1]Diphenyl acetonitrile

--- -- 650 650 Collection, Storage, Transportation and sell to authorized end users registered under rule-9. LOI For the same is attached as Annexure III.

8. Aluminum Chloride [30-40 %]

Process [1]Diphenyl acetonitrile

--- -- 425 425 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.LOI For the same is attached as Annexure III.

-


(For HW management)

Membership Certificate will provide at the time

of EIA



Not Applicable




Sr. No.

Name of Product Name of Solvent

Solvent Quantity

(MT/Month

Solvent Recovered Quantity

Percentage

Recovery

of 167


Page 90 of 167

) (MT/Month) (%)

1 2-Nitro-P-Phenylene Di Amine

Acetic Acid

43.4 42 97

2 Diphenyl acetonitrile Benzene 38.7 37.3 96

IPA 16.5 16 97


� Minimum joints/flanges � Adequate Condenser � Brine will be utilised as chilling agent � Pumps with double mechanical seals � Proper Ventilation � PPEs



Hazardous chemicals

Remarks

Storage tanks Hydrochloric Acid Tank

Sulfuric Acid Tank

Drum/Barrel storage O-Amino Azo Toluene Drum

Sodium Nitrite Srum

Caustic Flakes Bag/Drum

2 - Naphthol Bag/Drum

P-Amino Azo Benzene Bag/Drum

Aniline Drum

P-Phenylene Di Amine Bag/Drum

Acetic Acid Drum

Nitric Acid Drum

Benzyl Cyanide Drum

Bromine Bottle

Benzene Drum

Aluminum chloride Cylinder

Sodium carbonate Drum

IPA Drum

Caustic Soda Drum





Chemicals at GIDC, Ankleshwar.

• Industrial effluent will be treated in ETP consists of primary treatment units and then sent to M/s.

ETL, CETP for further treatment and disposal.

• Natural gas will be used as fuel. Two stage alkali scrubber will be provided as APCM with

reactor vent.

of 167


Page 91 of 167

• Distillation residue will be sent for co-processing or CHWIF. Bleed liquor (Sodium Bromide) will

be sent to actual end user having rule-9 permission.






1. Provide detoxification treatment for Cyanide bearing stream generated from process and

washing.


3. Quantity and quality of process effluent generation product wise and adequacy assessment

report of ETP to achieve inlet norms of M/s. ETL, CETP.

4. Safety precautions for Bromine, Benzyl Cyanidestorage, handling and transportation as per

the prevailing law/rules & regulations.











report.






form.




of 167


Page 92 of 167









2006.



13 SIA/GJ/IND2/31285/2019 M/s. ReeAtharva Life Science Pvt. Ltd.

Plot No: 5178, GIDC Ankleshwar,

Ankleshwar, Dist.: Bharuch

Screening & Scoping







• This is existing Synthetic Organic Chemical manufacturing unit and now proposes for expansion as

tabulated below:

:Sr.

No.

Name of

the

Products

CAS no.

/CI no.

Quantity MT/Month End Use of the

product

Existing Prop Total

of 167


Page 93 of 167

API (SYNTHETIC APIs) : 20 MT/Month

1 Venlafaxine Either / or 93413-69-5

-- 20 20 Depression &

Anxiety disorder

2 Amlodipine Either / or 88150-42-9

Antihypertensive

3 Atorvastatin Either / or 134523-00-

5

Cardiovas

cular

Disease

4 Citalopram

hydrobromide Either

/ or

59729-32-7

Depression,

Anxiety

disorder,

Phobia

5 QuetiapinFumarat

e Either / or

111974-72-

2

Atypical anti-psychotic

6 Escitalopram

Oxalate Either / or

219861-08-

2

Treatme

nt of

Depress

ion

7 Dothiepine Hydrochloride Either / or

897-15-4 Major Depressive Disorder

8 Rosiglitazone Maleate Either / or

155141-29- 0

Diabetes

9 Clomipramine Hydrochloride Either / or

17321-77-6

Depression and obsessive-compulsive disorder

10 Carbamazepine Either / or

298-46-4 Antiepilepsy

11 MetoprololTartarate Either / or

37350-58-6

Chest Pain, Heart failure & High Blood Pressure

12 Mebendazole Either / or

31431-39-7

Antifungal

13 Phenylephrine HCL Either / or

61-76-7 Allergic

14 Sucralfate USP Either / or

54182-58-0

Intestinal Ulcers & Stomach ulcers

of 167


Page 94 of 167

15 Theobromine Either / or

83-67-0 lung diseases

16 Metoprolol Succinate Either / or

98418-47-4

Antihypertensive

17 Fluconazole Either / or 86386-73-4

Antifungal

INTERMEDIATES :- 40 MT/Month

18 2, 5 Dichloro Para

PhenyleneDiamine

Either / or

20103-09-7

-- 40 40 Pharma Intermediates

19 2,5 Dimethyl Para

PhenyleneDiamine

Either / or

86386-73-4

20 2-{2[2-[ 2,6

Dichlorophenyl)Amino]

Phenyl]Acetyl]Oxyacet

ic Acid] Either / or

1216495- 92-9

21 2-Mercapto 5-Methoxy

Benzimidazole Either /

or

37052-78-1

22 2 Nitro 4

Methoxy Aniline

Either / or

96-96-8

23 3-[4-Chloro-5-

(Cyclopentyloxy)-2-

Fluorophenyl]-5-

(Propan-2-Ylidene)-

1,3-Oxazolidin-4-

One. (PIK) Either / or

2886-65-9

24 Sodium/Potassium {2-

[ (2,6 Dichloro

Phenyl)Amino]

Phenyl}

AcetateEither

/ or

15307-77-4

25 2 Chloro Para

PhenyleneDiamin

e Either / or

615-66-7

26 2-Chloro 1-

Phenoxy Benzene

Either / or

10304-81-1

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Page 95 of 167

27 2,3

XylylAnthranilic

Acid Either / or

28022-11-9

28 2 Chloro 5

Methyl PPD

Either / or

5307-03-9

29 5 Amino Ortho

Toluedene Either /

or

99-55-8

30 4-Bromo

Anisole Either /

or

104-92-7

31 3 Amino 4 Methoxy

Acetanilide Either /

or

6375-47-9

32 Para Anisidine Either

/ or

104-94-9

33 2 Chlor 4 Fluoro

5NBC Either / or

86393-34-2

34 Para Amino

Salicylic Acid v

Either / or

65-49-6

DERIVATIVES TO CHLORINATION USING THIONYL CHLORIDE-30 MT/M

35 Bis-(2 Chloro Ethyl)

Amine Hcl Either /

or

821-48-7 -- 30 30 Aripripra

zole,

Trazodo

ne

36 4(2-Chlore Ethyl)

Morpholine HCL

(CEM HCL) Either /

or

3647-69-6 Floredil, Morclofone

37 2 Chloro Ethyl

Amine Hcl Either /

or

821-48-7 Ifosfamide

38 Di Methyl Amino

Isopropyl Chloride

(DMIPC)-HCL Either

/ or

4584-49-0 Methadone

,Isothipendyl

39 4CBC (4 Chloro

– Butyryl

Chloride ) Either

4635-59-0 Mitomycin

of 167


Page 96 of 167

/ or

40 M4CB(4-

Methoxy Butyryl

Chloride) Either

/ or

824-94-2 Pharma Intermediates

41 Cyclo Propyl

Carbonyl Chloride

Either / or

4023-34-1 Prazepam

42 Cyclohexane

Carbonyl Chloride

Either / or

2719-27-9 Praziquantel

43 2-Furoyl

Chloride Either /

or

527-69-5 Diloxanide

44 Acetyl Salicyl

Chloride Either / or


45 O P Dichloro

Benzoic Acid Either

/ or

50-84-0 Lamotrigine

46 Para Nitro

Benzoic Acid

Either / or


NITRO TO AMINO CONVERSION BY CATALYTIC HYDROGENATION :- 40

MT/Month

47. Nitro to

Amino

Conversion

by catalytic

Hydrogenatio

n

-- 40 40 Pharma Industries

P-

(Nitromethyl)Benzoate Either / or

619-50-1

5-Amino Salicylic

Acid Either / or

89-57-6

4-Amino 2-

Chloro Aniline

Either / or

3964-52-1

2,5 Di Amino

Toluene Either / or

95-70-5

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ALDEHYDE TO ALCOHOL CONVERSION BY CATALYTIC HYDROGENATION

:- 40 MT/Month

48. Aldehyde to

Alcohol

Conversion by

catalytic

Hydrogenation

-- 40 40 Pharma

Industrie

s

Benzyl Alcohol Either

/ or

100-51-6

P-Hydroxy

Benzyl Alcohol

Either / or

623-05-2

P-Chloro Benzyl

Alcohol Either /

or

873-76-7

P-Nitro Benzyl

Alcohol Either / or

619-73-8

2,4-Di Nitro

Benzyl Alcohol

Either / or

4836-66-2

49. DISTILLATION OF

MIXED/SPENT

SOLVENT :

(A) ETHYLENE DI

CHLORIDE

(B) TOLUENE

(C) XYLENE

(D) HEXANE

(E)BUTANOL

(F) ETHANOL

(G) METHANOL

(H)AMINES

(I) GLYCOL

(J) ETHERS

(K) TRI CHLORO

PROPANE

(L) IPA

(M)ACETONR

(N)

NITROBNZENE

(O)CYCLOBENZ

ENE

500 -- 500 --

of 167


Page 98 of 167

(P)TETRAHYDR

OFU RAN

(Q)ACETONITRI

L E

(R) METHYL

ISOBUTYL

KETONE/METHY

L ETHYL

KETONE

(S) ETHYL

ACETATE

(T) METHYL

CHLORO

BENZENE

(U)

CYCLOHEXANE

(V) PHENOL

50 AROMATIC

SOLVENTS OF

DIFFERENT

RANGE

500 -- 500 --

51 ALPHABATIC

SOLVENT OF

DIFFERENT

RANGE

500 -- 500 --

52 PRINTING

OIL/RUBBER

PROCESS

OIL

500 -- 500 --

53 TURPENTINE OIL 500 -- 500 --

54 WIRE ENAMELS

& VARNISHES

FOR PRIMARY &

SECONDARY

ELECTRICAL

INSULATIONS

500 -- 500 --

55 WHITE SPRAYOIL 500 -- 500 --

56 THINNERS 500 -- 500 --

Total 4000 170 4170




of 167


Page 99 of 167

Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: 2.17

Proposed: 16.28

Total: 18.45

B Total Plot area

( sq. meter)


Proposed: 0 Sq. m.

Total: 2040 Sq. m.

Green belt area

( sq. meter)


Proposed: 0 Sq. m.

Total: 310 Sq. m.

C Employment generation Existing: 22

Proposed: 52

Total: 74

D Water

i

Source of Water Supply(GIDC Bore well,

Surface water, Tanker supply etc...)

GIDC Bharuch.

Status of permission from the concern authority. Unit have 16 KLD Water permission from

GIDC and for remaining unit have applied.

ii

Water consumption (KLD)

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1 2 3.00

Fresh

(B) Gardening 1 4 5 Fresh

(C) Industrial

Process 0 74 74 53 Fresh+21Recycle

Washing 0 7 7 7 Recycle

Boiler 6 22 28 Fresh

Cooling 8 45 53 53 Recycle

Others 0 6 6 6 Recycle

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Page 100 of 167

Industrial Total 14 154 168 81 fresh+87recycle

Grand Total (A+B+C) 16 160 176 89 fresh+87recycle





Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(C) Domestic 1 2.00 3.00

(D) Industrial

Process 0 84 84

Washing 0 7 7

Boiler 0 3 3

Cooling 0 8 8

Others 0 8 8

Total Industrial waste water 0 110.00 110.00

Industrial+ Domestic wastewater 1 112 113



� ETP-200 KLD (primary, secondary & tertiary treatment)

� RO: 150 KLD

� MEE: 120 KLD


� High Concentrated Effluent ( Process Effluent ) – 84 KLD will be send to stripper after

that it will be send to MEE condensate will be treated in ETP followed byRO.

� Low Concentrated Effluent (Washing, Blow down & Scrubber effluent )– 22 KLD

will be treated in ETP Followed byRO.

� RO Reject – 25 KLD will be send toMEE.


Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and

Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.

� Unit have recently obtain membership of 15 KLD in new allotted NCT capacity 15 MLD

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Page 101 of 167

as per new GPCB Circular. Unit will give full fledge treatment and after achieving the

norm, unit will discharge effluent to NCT. So, direction under section 18 (1) (b) of the

Water (Prevention and Control of Pollution) act, 1974

issued by CPCB regarding compliance of CETP is not applicable.


� Not Applicable.


Domestic: Disposed in soak pit.

Industrial:

127 KL/day effluent is being treated in unit’s own effluent treatment plant. After treatment 15 KLD send to NCT and remaining 112 will be send to RO &MEE.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.

Name of Common facility (CF)(For waste water treatment)

� Narmada Clean Tech



Narmada Clean Tech - 15 KLD




87 KL/Day-RO permeate

MEE Salt

2 KL/Day

NaBr & Sodium

Bisulphide to Actual End

User 4 KLD

Strip Solvent

2 KL/D

Process

74 KL/Day

Effluent from

process

84 KL/Day

Domestic

3.0 KL/Day

Boiler

28 KL/Day

Blow down

3 KL/Day

Washing

7 KL/Day

ETP 127 KL/Day

Soak Pit

2 KL/Day

Cooling

53 KL/Day

Others

6 KL/Day

Blow down

8 KL/Day

RO 112 KL/Day

Stripper

15 KL/D send to NCT

Gardening

5.0 KL/Day

MEE

107 KLD

RO Reject25

KL/Day

Scrubbed Soln.

8 KL/Day

HCl, NaCl &

Ammonium Sulphate

to ETP 4KLD

Total Water Requirement - 176

( FRESH- 89 KL/Day & RECYCLE - 87 KL/Day)

Washing

effluent

7 KL/Day

82 KL/Day 105 KL/Day

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Page 102 of 167

Total reuse 87 KLD

-

Source of waste

water for reuse

with quantity in

KLD (From where it

is coming)

Application area

with quantity in

KLD (Where it is

used)

Characteristics of

waste water to be

reused (COD, BOD,

TDS etc.)

Remarks

regarding

feasibility

to reuse i.e.

87 KLD from RO 87 KLD in

Process, cooling

tower, washing &

Scrubber

pH: 6-8

COD: 0-10 mg/l

TDS: 100-200

mg/l

87 KLD from RO

E Air



Existing & Proposed

-

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter

)

Type of

Fuel

Quantity of

Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

AS Per Existing CCA No:-H-90445

1.

Thermic Fluid Heater 1 Lac Kcal/hr

12

Briquettes OR Natural gas

0.3 MT/day OR 200 Nm3/Day

PM SO2NOX

Cyclone + Water

Scrubber

2.

Baby Boiler 800 kg /hr

12

Briquettes- OR

Natural gas

0.3 MT/day OR 200 Nm3/Day

PM SO2

NOX

After Proposed Expansion

3.

Boiler-1 (5MT/Hr)

12

Briquette OR Natural

Gas

12 MT/day OR

300Nm3/ day

PM SO2NOX

ESP + WATER Scrubber Adequate

stack height 4.

Thermic Fluid Heater (12 Lacs Kcal/Hr)

Briquette- OR Coal

4.4 MT/day OR 10 MT/day

of 167


Page 103 of 167

5. D.G.Set (125 KVA)

Diesel

50 lit/day


Existing & Proposed

-

Sr.

no.

Specific Source of

emission

(Name of the

Product &Process)

Type of

emission

Stack/V

ent

Height

(meter)


Measures

(APCM)

There is no process gas emission.

After Proposed Expansion

1 Reaction vessel -1

HCl 12

Water Scrubber +

Caustic scrubber

2 Reaction vessel -2 NH3 12 Acid Scrubber

3 Reaction vessel -3 Cl2, Br2

12 Water Scrubber +

Caustic scrubber

4 Reaction vessel -4 HCl, SO2

12 Water Scrubber +

Caustic scrubber


Sr.

No.

Source Probable

Pollutant

Emission

Control Measures/ APCM

1 Solvent storage tank Air pollutant

(VOC)

i) Carry out work place area monitoring

to find out concentration level in ambient

air

Close handling system.

ii) Provision of breather valve cum

flamearrester.

2 Solvent recovery

system

Air pollutant

(VOC)

i) Solvent recovery system with steam

condensation system.

Pumps & motors are

Mechanical seal type.

3 Handling of raw

material bags in

storage area

Air pollutant

(PM)

i) Provision of exhaust ventilation

Provision ofPPE.

ii) Provision of Job rotation to

reduceexposure.

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Page 104 of 167

4 Flange joints of

pipeline, pump &

motors

Air pollutant

(VOC)

i) Routine &periodic inspection

to checkleakage.

ii) Preventive maintenance, Follow

SOP formaintenance.

iii) Pumps & motors will be mechanical

sealtype.

iv) LDAR program will be followed.

Provision of Flange guard.

5 Solid raw material

transferring to

reactor

Air pollutant

(PM)

Hopper will be provided with powder

transfer system.

6 Liquid raw material

transferring to

reactor

Air pollutant

(VOC)

Feeding of liquid raw material will be

carried out by closed pipeline and

mechanical seal

pump. 7 Loading /unloading

at storage area

Air pollutant

(VOC)

Unloading through pipeline to

tank in a close system.

F Hazardous waste


Rules 2016.

Existing & Proposed

i

Sr.

no.

Type/Name of

Hazardous

waste

Specific

Source of

generation

(Name of

the

Activity,Pr

oduct etc.)

Categ

ory

and

Sched

ule as

per

HW

Rules.

Quantity

(MT/Annum)

Management of

HW

Existing

Proposed

Total

1. Spent solvents Collection from other industries

20.2 6000 3363 9363

Collection, storage, & Treatment in own SRP plant.

2. Strip solvent Stripper 20.2 0 730 730 Collection, storage and send to SRP plant.


Production process of Amlodipine

20.3 180 277 457 Collection, storage, transportation &

of 167


Page 105 of 167

disposal by co-processing/incineration.

4. Industrial Light Fuel or Dehydrated Coaltar or byproduct

Solvent Recovery Plant

20.3 360 -- 360 Collection, storage, transportation & disposal by co-processing/incineration.

5. Empty barrels/containers/liners contaminate with hazardous chemicals/wastes

From

Packing

Material

33.1 3.60 15.40 19 Collection, storage, transportation & disposal by selling to GPCB authorized recycler

6. Spent Clay containing Oil

4.5 12.00 -- 12.00

Collection, storage, transportation & disposal by reactivation within unit and reuse in process.

7. Used or Spent oil

From Lubrication

5.1 0.06 3.94 4 Collection, storage, transportation & disposal by selling to GPCB authorized recycler/refiner.

8. Spent Carbon Generates from Production process of Clomipramine Hydrochloride

28.3 0 103 103 Collection, Storage & Disposal by sent it to Co-processing /incineration.

9. Process solid waste

Production

process of

Sucralfate

USP

28.1 0 192

192 Collection, Decontamination, Disposal by sent it to Co-processing /incineration.

10. Spent Sulphuric Acid

Generates from 5 Amino Ortho Toluedene

B15 0 1189 1189

Collection, Storage and send to ETP for treatment.

11. HCl Solution 30 Scrub B15 0 587 587 Collection,

of 167


Page 106 of 167

% solution will

be

generates

from Cyclo

Propyl

Carbonyl

Chloride

Storage and send to treatment in ETP.

12. Sodium Bromide Solution: Inorganic Waste

Scrub solution Generates from 4-Bromide Anisole

B15 0 452 452 Collection, Storage and disposal by sell out to authorized vendor under Rule 9 permission.

13. Ammonium Sulphate Solution: Inorganic Waste

Scrub solution Generates from mebendazole

B15 0 730 730 Collection, Storage and disposal and treated in ETP.

14. Sodium Chloride Solution : Inorganic Acid

Generated

from

manufacturi

ng of Para

Anisidine

B15 0 352 352 Collection, Storage and disposal by reuse internally/ send to actual end users.

15. Sodium Bisulphite Solution

Generated

from

manufacturi

ng of 2

Chloro

Ethyl Amine

Hcl

B15 0 1107 1107

Collection, Storage and disposal by sell out to authorized vendor under Rule 9 permission or in house disposal

16. Potassium Hydroxide

Generated

from

manufacturi

ng of 2-

Chloro 1-

Phenoxy

Benzene

B15 0 246 246

Collection, Storage and disposal and treated in ETP.

17. ETP Sludge From ETP 35.3 0 250 250 Collection, storage within factory premises, transportation and Disposal at

18. MEE salt From

Evaporator

35.3 0 700 700

of 167


Page 107 of 167

TSDF operated by e.g. M/s BEIL, Ankleshwar or any authorised TSDF

19. Date expired Product

From

premises

28.4 0 5 5 Collection, storage, transportation , co-processing in cement plants /incineration in common incinerator, landfill in common TSDF (if calorific value is less than 2500 kcal/kg).

20. Off-specification Product

Production

process

28.5 0 5 5 Collection, storage, transportation, co-processing in cement plants /TSDF, incineration in common incinerator, landfill in common TSDF (if calorific value is less than 2500 kcal/kg).


(For HW management)

Membership letter from BEIL is submitted.



All Non-Hazardous waste will give to scrap

vendor




Sr.

No.

Name of Representative Product

Name of Solvent used

Product Quantity in MT/Month

Solvent Quantity used in ton

Solvent recover Quantity in

Solvent Recovered Quantity in MT/Mont

Percentage Recovery

of 167


Page 108 of 167

1. Dothiepine Hydrochloride

Toluene

20

7.32 7.02 140.4 96 %

Isopropyl

alcohol 11.77 11.30 226.06 96 %

Tetrahydrofur

an 1.37 1.32 26.4 96 %

Hexane

2.52 2.42 48.40 96 %

Ethylen

e

dichlorid

e

13.05 12.53 250.66 96 %

2. 5 Amino Ortho Toluedene

Toluene

40

1.5 1.44 57.6 96 %

Methanol

1.25 1.20 48.0 96 %

3. 5-Amino Salicylic Acid

Methanol

40 2.72 2.61 104.72 96%

4. 2,4-Di Nitro Benzyl Alcohol

Benzene

40 2.72 2.61 104.72 96 %


� Provision of mechanical seal in pump.

� Regular inspection of tank roof seals.

� Adequate measures for the minimization/prevention of the fugitive emission.

� Regular maintenance of valves, pumps and other equipment to prevent leakage.

� Entire process to be carried out in the closed reactor with proper maintenance of

temperature.

� Regular periodic monitoring of work area to check the fugitive emission.

� Adequate stack heights as per the GPCB estimation will be provides at all locations to

reduce GLCs of pollutants.

� Air Pollution Control System will be installed in the plant.


of 167


Page 109 of 167


Storage Tank Cyclohexane --

HDPE Storage Tank Formic Acid ---

Storage Tank N hexane --

HDPE Storage Tank Sodium Hydroxide --

Storage Tank O-xylene --

Storage Tank Acetone --

Storage Tank Toluene --

HDPE Storage Tank Acetic Acid --

Storage Tank Thio phenol --

Storage Tank Isopropyl alcohol --

HDPE Liner Bags Thio urea --

Storage Tank Methylene Chloride --

Storage Tank Benzene --

HDPE Storage Tank Aluminium chloride --

HDPE Storage Tank Acetic Anhydride --

HDPE Spiral Tank Phenol --

Aluminium Tank Nitric Acid --

HDPE Storage Tank Sulphuric Acid --

Storage Tank Ortho Toluene --

HDPE Spiral Storage Tank Bromine --

Cylinder Sulphur Dioxide --

Storage Tank Thionyl Chloride --

� Applicability of PESO :

� Unit has PESO license for 80 KLD storage of Petroleum Class A, for additional

quantity as per this proposed project unit will apply amendment application after

granting CCA.


Jyoti Om Chemical Research Centre Pvt. Ltd. during SEAC meeting dated 16/04/2019.



• Low concentration effluent and MEE condensate will be treated in ETP consists of primary,

secondary and tertiary treatment units followed by RO. 15 KLD tertiary treated effluent will be

of 167


Page 110 of 167

sent to NCTL for deep sea disposal. RO permeate will be reused for industrial purpose within

premises.

• High concentration effluent (from process and RO Reject) will be treated in MEE.

• Coal or briquette will be used in proposed TFH and boiler. Common ESP + Water Scrubber will

be provided as APCM with boiler and TFH. Water Scrubber + Caustic scrubber and acid

scrubber will be provided as APCM for process gas emission control.










3. Safety precautions for Chlorine, Ammonia, Hydrogen storage, handling and transportation as

per the prevailing law/rules & regulations.

4. Safety precautions in Hydrogenation as per the prevailing law/rules & regulations.









be made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various

activities therein. The details of fund allocation and activities for CER shall be incorporated in

EIA/EMP report.

7. Explore the use of renewable energy to the maximum extent possible. Details of provisions

to make the project energy-efficient through of energy efficient devices and adoption of

modes of alternative eco-friendly sources of energy like solar water heater, solar lighting etc.



of 167


Page 111 of 167

form.












2006.



14 SIA/GJ/IND2/32892/2019 M/s. J. S. Chemicals

Plot No.4801/A-8,GIDC,Industrial Estate,Ankleshwar,Dist. Bharuch

Screening & Scoping

Category of the unit : 5(f)






• This is existing Synthetic Organic Chemical manufacturing unit and now proposes for expansion as

tabulated below:

Sr.

no.

Name of the

Products

CAS no. /

CI no.



1 Para Nitro Aniline

100-01-6 25 --- 25 Dyes & Dyes

Intermediates Ind.

2 2,4 Di Nitro Aniline

97-02-9 7.5 --- 7.5 Dyes & Dyes

Intermediates Ind.

3 Di Chloro Para Nitro Aniline

99-30-9 5 --- 5 Dyes & Dyes

Intermediates Ind.

4 6 Chloro 2,4 Di Nitro Aniline

3531-19-9 2 --- 2 Dyes & Dyes

Intermediates Ind.

of 167


Page 112 of 167

5 6 Bromo Di Nitro Aniline

1817-73-8 25 --- 25 Dyes & Dyes

Intermediates Ind.

6 P-Carboxy Phenyl Gamma Acid

741486-49-2

---

32.0 32.0

Dyes & Dyes Intermediates Ind.

7 M-Sulfophenyl Gamma Acid

25251-42-7

--- Dyes & Dyes

Intermediates Ind.

8 Sodium-1-Naphthol-5-Sulfonate

5419-77-2 --- Dyes & Dyes

Intermediates Ind.

9 Naphthalene 1,5 Di Sulfonic Acid

81-04-9 --- Dyes & Dyes

Intermediates Ind.

10 Naphthalene 1,5 Di Sulfonic Acid Di Sodium Salt

1655-29-4 --- Dyes & Dyes

Intermediates Ind.

11 1,8 Naphthosultone

83-31-8 --- Dyes & Dyes

Intermediates Ind.

12 4,4-Diamino Diphenyl Cyclohexane

34447-09-1

--- Dyes & Dyes

Intermediates Ind.

13

4,4 Diamino 3,3 Dimethyl Diphenyl Cyclohexane

6442-08-6 --- Dyes & Dyes

Intermediates Ind.

14 N,N Diethyl Metanillic Acid

97-20-1 --- Dyes & Dyes

Intermediates Ind.

15 4-Nitro Ortho PhenyleneDiamine

99-56-9 --- Dyes & Dyes

Intermediates Ind.

16 4-Nitro Meta PhenyleneDiamine

5131-58-8 --- Dyes & Dyes

Intermediates Ind.

17 4-Nitro Para PhenyleneDiamine

5307-14-2 --- Dyes & Dyes

Intermediates Ind.

18 Fast Red ITR Base

97-35-8 --- Dyes & Dyes

Intermediates Ind.

19 Fast Scarlet LG Base

2815-50-1 --- Dyes & Dyes

Intermediates Ind.

20 Para Cresidine N Methyl Sulfonamide

49564-57-0

--- Dyes & Dyes

Intermediates Ind.

Total 64.5 32.0 96.5

Total Production

Capacity 96.5

MT/Month




of 167


Page 113 of 167

Sr.

no.

Particulars Details


(Rs. in Crores):

Existing:1.593

Proposed:2.50

Total: 4.093

B Total Plot area

( sq. meter)


Proposed: 0 Sq. m.

Total: 983.25 Sq. m.

Green belt area

( sq. meter)


Proposed: 0 Sq. m.

Total: 197 Sq. m.

C Employment generation Existing:20

Proposed:30

Total:50

D Water

i



GIDC water Supply

Status of permission from the concern authority. GIDC Water supply letter will be

provided at the time of EIA.


Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 1.0 1.0 2.0

(B) Gardening 1.0 1.0 2.0

(C) Industrial

Process 0.9 0.6 1.5

Washing 4.0 0.6 4.6

Boiler 1.5 6.0 7.5

Cooling 0.5 5.0 5.5

Others 1.1 0.8 1.9

Industrial Total 8.0 13.0 21.0

Grand Total (A+B+C) 10.0 15.0 25.0

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Page 114 of 167



3) Total fresh water requirement:21 KLD


Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 0.55 0.45 1.00

(B) Industrial

Process 1.85 1.4 3.25

Washing 4.00 0.6 4.60

Boiler 0.15 1.0 1.15

Cooling 0.00 2.0 2.00

Others 0.00 0.0 0.00

Total Industrial waste water 6.00 5.0 11.0

6.55 5.45 12.0



� For Existing:-In-house ETP (Primary, Secondary, Tertiary)+Send to NCT � For Proposed :-Primary ETP + In-house MEE � After Proposed Expansion :- Capacity of ETP for Existing:- 6 KLD and Proposed :-

6 KLD


� Effluent is generated from process, washing, and boiler blow down, Cooling bleed off which are subjected to primary treatment. After treatment additional waste water will be treated into the primary ETP and then send to (in-house) MEE for further treatment. After adequate treatment, Condensed water will be recycled within the plant premises.

� Effluent Treatment plant Details.




1. Existing:

ii. For the existing production capacity, the generated effluent is collected, treated into

ETP [Primary, Secondary and tertiary treatment plant] and then discharge to NCTL-

CETP for further treatment. After expansion existing discharge permission of the unit

497

will be continue.

iii. Scrubbing solution is utilized as raw material in manufacturing process of Para

Aniline, 2,4 Di Nitro Aniline.

2. Proposed:

I. For proposed expansion, Industrial waste water will be treated into the primary ETP

and then send to (in-

Condensed water will be recycled within the


� Not Applicable



Industrial: Existing:

I. For the

treated into ETP [Primary, Secondary and tertiary

then discharge to NCTL

existing discharge permission of the unit will be c

II. Scrubbing solution is utilized as raw material in manufacturing process

of Para Nitro Aniline, 2,4 Di Nitro Aniline.

Proposed:

ii. For proposed expansion, Industrial waste water will be treated into the

primary ETP and then send to (in


plant premises.


etc.


� For Existing: - NCT: Narmada Clean Tech

� For Proposed:-Generated additional waste water send to

treatment. After adequate treatment, Condensed water will be recycled within the

plant premises.

Membership of Common


Membership Certificate of waste water [NCT] is attached as



of 167

Scrubbing solution is utilized as raw material in manufacturing process of Para

Aniline, 2,4 Di Nitro Aniline.

For proposed expansion, Industrial waste water will be treated into the primary ETP

-house) MEE for further treatment. After adequate treatment,

Condensed water will be recycled within the plant premises




For the existing production capacity, the generated effluent is collected,

treated into ETP [Primary, Secondary and tertiary treatment plant] and

then discharge to NCTL-CETP for further treatment. After expansion

existing discharge permission of the unit will be continue.

Scrubbing solution is utilized as raw material in manufacturing process

of Para Nitro Aniline, 2,4 Di Nitro Aniline.

Proposed:

For proposed expansion, Industrial waste water will be treated into the

primary ETP and then send to (in-house) MEE for further treatment.


plant premises.



NCT: Narmada Clean Tech-CETP

Generated additional waste water send to (in-house) MEE for further




Membership Certificate of waste water [NCT] is attached as Annexure-II


Page 115 of 167

Scrubbing solution is utilized as raw material in manufacturing process of Para Nitro

For proposed expansion, Industrial waste water will be treated into the primary ETP

house) MEE for further treatment. After adequate treatment,


existing production capacity, the generated effluent is collected,

treatment plant] and

CETP for further treatment. After expansion

ontinue.

Scrubbing solution is utilized as raw material in manufacturing process

For proposed expansion, Industrial waste water will be treated into the

or further treatment.



house) MEE for further


II


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Page 116 of 167



Total reuse:4 KLD

-

Source of waste


quantity in KLD

(From where it is

coming)

Application

area with

quantity in

KLD (Where it

is used)

Characteristics of

waste water to be

reused (COD, BOD,

TDS etc.)

Remarks

regarding

feasibility

to reuse i.e.

MEE(Condensed

Water)

[4 KL/Day]

In Process

[4 KL/Day]

pH 6-8

TDS (mg/lit) 300-500

TSS (mg/lit) 100-150

COD (mg/lit) 100-400

• Condensed water (4 KLD) will be recycle in process.

E Air



etc.

Existing & Proposed

-

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Page 117 of 167

Sr.

no

.

Source of

emission

With Capacity

Stack

Height

(meter)

Type

of Fuel

Quantity

of Fuel

MT/Day

Air Pollution

Control

Measures

(APCM)

Type of

emissions

i.e. Air

Pollutants

Existing

1 Boiler[Cap. 600

kg/hr] 11 LDO

100 Lit/

Day

Adequate

Stack Height

PM

SO2

NOx 2 D.G Set[63 KVA] 11

Proposed

1 Boiler[Cap. 1 TPH] 11 Natural

Gas

1000

Nm3/Day

Adequate

Stack Height

PM

SO2

NOx 2 TFH[Cap. 2 Lakh K

Cal/hr] 11

-


Existing & Proposed

-

Sr.

no.

Specific Source of

emission(Name of the

Product & Process)

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution

Control Measures

(APCM)

Existing

1 Reaction Vessels HCl

NH3 15

Two Stage Water

Scrubber

Proposed

1 Reaction Vessels-1 HCl 11 Two Stage Water

Scrubber

2 Reaction Vessels-2 Cl2 11 Two Stage Alkali

Scrubber

-





� Adequate PPEs

F Hazardous waste


Rules 2016.

Existing & Proposed

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Page 118 of 167

i

Sr

.

n

o.

Type/Name

of

Hazardous

waste

Specific

Source of

generation

(Name of

the Activity,

Product

etc.)

Catego

ry and

Sched

ule as

per

HW

Rules.

Quantity

(MT/Annum)

Management of

HW

Existi

ng

Propos

ed

Tot

al

1. Empty

barrels/

containers/lin

ers

contaminated

with

hazardous

chemicals

/wastes

Raw Material

and Packaging

33.1 24 16 40 Collection,

Storage,

Transportation,

Decontamination,

reuse or send

back to supplier,

and sold to

Authorized

Vendors.

2. Used Oil From Machinery

5.1 0.024 0.976 1.0 Collection, Storage, Transportation and sold to authorized Recyclers.

3. ETP Sludge ETP 35.3 42 138 180 Collection, Storage, Transportation and sent to TSDF site.

4. MEE Salt MEE 35.3 --- 180 180 Collection, Storage, Transportation and sent to TSDF site.

5. Hydrochloric Acid [28-33%]

Scrubber

[1]N,N Diethyl MetanillicAcid [2] Fast Red ITR Base [3] P- Cresidine N Methyl Sulfonamide

--- --- 409 409 Collection, Storage, Captive consumption for the manufacturing process of Product Sr. No. [6,7,12,13,18,19].

6. Sodium Hypo Scrubber --- --- 348 348 Collection,

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Page 119 of 167

Chlorite Sol. [30-40%]

[1] Fast

Scarlet LG

Base

Storage, Captive consumption as cleaning agent in ETP [In-House].

7. Sodium Bisulfite Sol. [30-40%]

Process

[1] P-Carboxy Phenyl Gamma Acid [2]M-Sulfophenyl Gamma Acid [3] Sodium-1-Naphthol-5-Sulfonate

--- --- 406 406 Collection, Storage, Transportation and sell to authorized end users registered under rule-9. LOI copy is attached as Annexure IV.

8.

Ammonium Sulfate [30-40%]

Process [1]1,8 Naphthosultone

--- --- 308 308 Collection, Storage, Transportation and sell to authorized end users registered under rule-9. LOI is attached as Annexure IV.

9. Spent Carbon Process [1] 4-NOPDA [2]4-NMPDA [3]4-NPPDA

36.2 --- 4.6 4.6 Collection, Storage, Transportation and sent to CHWIF Facility.

10.

Spent Catalyst

Process [1] DDC [2] DDDC

26.5 --- 7.6 7.6 Collection, Storage, Transportation and sent to TSDF site.

11.

Bleed /Liquor Ammonia [10-20%]

Scrubber [1]PNA [2]NNA

--- 456 --- 456 Collection, Storage, utilized as Raw Material in manufacturing process of PNA and DNA.

-


(For HW management)

Membership Certificate is attached as

Annexure-III



Not Applicable

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Page 120 of 167




� Not Applicable


• Minimum joints/flanges

• Adequate Condenser

• Brine will be utilised as chilling agent

• Pumps with double mechanical seals

• Proper Ventilation

• PPEs



Storage tanks --- ---

Drum/Barrel storage

1 Amino-8-Napthalene Sulfonic Acid, 2,4 Di Nitro Aniline, Ammonia, Aniline, Benzyl Chloride, Chloro Sulfonic Acid, Cyclohexane, Di Ethyl Amine, DNCB, Ethyl Chloride, G-Salt, H2O2, HCl, HNO3, Meta PhenyleneDiamine,Metanilic Acid, NaCl, NaNO2,NaOH, Naphthalene, Naphthalene 1,5 Disulfonic Acid, O-Anisidine, Oleum, Ortho PhenyleneDiamine, O-Toluidine, Para Amino Benzoic Acid, Para PhenyleneDiamine, PNA, PNCB, Sulfuric Acid

Br2 Bottel

Cl2 Cylinder






• Additional industrial effluent will be treated in ETP consists of primary treatment units followed by

MEE. MEE condensate will be reused in process within premises.

• Natural gas will be used as fuel. Two Stage Water Scrubber will be provided as APCM with

process gas stacks.

of 167


Page 121 of 167

• Bleed liquor ammonia will be utilized as raw material in manufacturing process of PNA and

DNA.ETP sludge and MEE salt will be sent to TSDF for landfilling.







2. Adequacy assessment report of ETP to treated industrial effluent and achieve inlet norms of

M/s. NCTL, CETP. Feasibility report of resue of treated industrial effluent for industrial

purpose within premises.

3. Safety precautions for Oleum, Ammonia storage, handling and transportation as per the

prevailing law/rules & regulations.






measures for common/ captive infrastructure due to proposed production





report.






form.



Industry’ shall be considered as generic TORs for preparation of the EIA report in addition to all

of 167


Page 122 of 167

the relevant information as per the generic structure of EIA given in Appendix III in the EIA

Notification, 2006.



15 SIA/GJ/IND2/31835/2019 Grasim Industries Ltd. (Chemical Division),

Plot No.-1, GIDC Industrial Estate , Vilayat, Dist.: Bharuch

Screening & Scoping

Category of the unit: 4(d)&1(d)






• This is existing Chlor Alkali plant with CPP and now proposes for expansion as tabulated below.

Sr.

no.

Name of the

Products

CAS no. /

CI no.

Quantity End-use of the products


1. Caustic Soda

Lye 1310-73-2

365,000

146,000 511,000

Manufacture of pulp and

paper, alumina, soap and

detergents, petroleum

products and chemical

production. Other

applications include water

treatment, food, textile,

metal processing, mining,

glass making and others.

2. Hydrogen 1333-74-0 102,200,0

00

(Nm3)

40,880,000

(Nm3)

143,080,000

(Nm3)

Industrial application such

as refining, treating metals

and food processing. It is

also used as alternate fuel

in many industries.

3.

Liquid Chlorine / Sodium

Hypochlorite / Hydrochloric

Acid

7782-50-5 328,500 250,390 578,890

It is a disinfectant. It is used to treat drinking water and swimming pool water. It is also used to make hundreds of consumer products frompaper to paints, and from textiles to insecticides. About 20% of chlorine produced is used to make PVC. It can be used Vinyls,

of 167


Page 123 of 167

Chloromethanes, CPW,

Organics Chemicals

4. Aluminium

Chloride 7746-70-0 25,000 5,000 30,000

It finds application in the chemical industry as a catalyst for Friedel–Crafts reactions, both acylationsand alkylations. It can be used in Agrochemicals, Pigments and Dyes, Pharma, Coating Industries

5. Sodium

Sulphate 7757-82-6 0 2,672 2,672

Sodium sulfate is used to

dry organic liquids. As filler

in powdered home laundry

detergents.

6. Captive Power

Plant ---

141 MW

35 MW 176 MW Power Generation

Total

• The project falls underCategory B of project activity 4(d)&1(d)asper the schedule of EIA Notification

2006.



Sr.

No.

Particulars Details


(Rs. in Crores):

Existing: INR 750 Crores

Proposed: INR 290 Crores

Total:INR 1040 Crores

B Total Plot area

( sq. meter)

Existing: 419750Sq. m.

Proposed: 154100Sq. m.

Total:573850Sq. m.

Green belt area

( sq. meter)


Proposed: 50853Sq. m.

Total: 189370Sq. m.

C Employment generation

Existing:

Proposed:

Total:

Direct

--

40

40

Indirect

--

20

20

D Water

i



GIDC

Status of permission from the concern authority. Permission obtained from GIDC.

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Page 124 of 167


Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 158 4 162

(B)Gardening * * * * Treated domestic

wastewater will be

used for

gardening/plantation

on the land area of

189370 m2

(C) Industrial

Process 4220 630 4850

Washing 375 200 575

Boiler 9550 2100 11650 Boiler make up

water

Cooling 5650 24 5674 Cooling make up

water

Others 1430 552 1982 DM Water

Regeneration

Industrial Total 21225 3506 24731

GrandTotal (A+B+C) 21383 3510 24893


2) Quantity to be recycled:13643KLD

3) Total fresh water requirement: 11250KLD


of 167


Page 125 of 167

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 126.4 3 129.4 --

(B)Industrial

Process 170 26 196 --

Washing 375 200 575 --

Boiler 3680 150 3830 Boiler blow down

Cooling 1850 5 1855 Cooling purge

Others 1430 552 1982 DM water

regeneration

Total Industrial

waste water 7505 933 8438 --

Grand Total (A+B)

7631.4 936 8537.4 --

iv Treatment facility within premises with capacity [For existing and Proposed]


• Effluent generated from industry will be treated in our existing effluent treatment plant. Treated effluent will be reused for cooling make-up, washing and DM water and RO reject will be used for Dust suppression in coal handling area, Sprinkling on fly ash, road cleaning.

• Domestic sewage will be treated in STP and treated wastewater will be reused for gardening

within premises.

Treatment scheme including segregation at source. All plants have collection pits constructed in each of the sections. The wastewater generated is collected in the collection pits and after physico-chemical treatment (wherever required) is reused in the respective plant process itself. The effluent mainly is generated from the caustic soda plant utilities that consists of cooling water of accessory equipments like blowers air compressors, air washeries blow down of cooling tower water, steam condensate, wash water from canteen, maintenance, demineralise water plant etc.

Note: (In case of CETP discharge): Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.

� Not Applicable

Brief note on Adequacy of ZLD (In case of Zero Liquid Discharge): � Not Applicable


Domestic:

The existent generated domestic waste water quantum of 126.4 KL/day is being

treated in an STP and the final treated domestic waste water is being used for

gardening purpose within premises. The domestic waste water to be generated

of 167


Page 126 of 167

from the proposed expansion will be to the tune of 3 KL/day, which will also be

treated in the existent STP and will be used for gardening purpose within the

premises.

Industrial:

The industrial effluent generating from the existing 141 MW CPP is 6505 kl/day which along with 400 kl/day of effluent from Chlor Alkali Plant is passed through RO 1. The treated water from the RO 1 which equals 5604 kl/day, out of which 686 kl/day is being used for gardeningwithin premises and 4918 kl/day is beingrecycled for reuse into DM water, cooling (make up) and washing purposes. The RO reject from RO 1is 1301 kl/day will be used for dust suppression in coal handling area, sprinkling on fly-ash and road cleaning. The effluent from the Chlor Alkali Plant which is 600 kl/day is being passed through an ETP and is being discharged into deep sea through DahejVilayat pipeline. For the proposed expansion, the effluent emanating from the ETP will be 933 kl/day. Out of this 662 kl/day of water will be directed into RO 3 and 271 kl/day will be directed to RO 2. The treated water from RO 2 will be 203 kl/day and that from RO 3 will be 496 kl/day. Both these streams will join the common recycle line. The reject from RO 2 and RO 3 will be 68 kl/day and 166 kl/day respectively which will be fed into RO 4. The treated water from it will be 94 kl/day which will join the common recycle line and the reject of 140 kl/day will directed into an MEE. The recovered water to the tune of 112 kl/day will be generated which will also join the common recycle line and the reject will be fed into Agitated Thin Film Dryer. Hence a total recycled water of 905 kl/day will be recycled back. Hence about 97 % generated effluent will be recovered and will be reused in the process reducing the 2nd day water requirement.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.

Name of Common facility

Not applicable, since our effluent generated from industry and domestic will be treated in our existing effluent treatment plant


Not applicable, since our effluent generated from industry and domestic will be treated in our

existing effluent treatment plant


of 167


Page 127 of 167



7820 KL/day steam condensate will be recycled back for boiler make-up, 275 KL/day treated wastewater will be recycled for washing, 5548 KL/day treated wastewater will be used for DM Water Recycle and Cooling Make up. 55% reductions in fresh water consumption by various recycle and reuse of treated wastewater. Specifically reuse details are tabulated below:

Source of waste water for reuse with quantity in KLD

Application area with quantity in KLD

Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.)

7820 KLD steam condensate from boiler

For boiler make-up (7820 KLD)

pH 7.5 – 8.5

BOD <10 mg/l

COD <50 mg/l

SS <5 mg/l

TDS 40 – 200 mg/l

6509 KLD permeate from RO plant (1),(2),(3) and (4) and MEE

For cooling tower make-up, washing, DM plant and for gardening purpose within premises(6509 KLD)

pH 7.5 – 8.5

BOD <10 mg/l

COD <50 mg/l

SS <5 mg/l

TDS 40 – 200 mg/l

1301 KLD reject from RO plant (1)

1. For dust suppression in coal handling area(828 KLD)

2. Sprinkling on fly-ash(428 KLD)

3. Road cleaning (45 KLD)

pH 7.5 – 8.5

BOD <10 mg/l

COD <50 mg/l

SS <5 mg/l

TDS 40 – 200 mg/l

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Page 128 of 167

E Air



Existing & Proposed

- Existing

Sr. No.

Stack / Vent attached to

Type & Quantity of Fuel

Height of the Stack/ Vent (m)

Expected Emission

Air Pollution Control Measures

EXISTING Flue Gas Emission

1. Boiler 1 & 2 Coal [100

MT/hr]

125 PM <150 mg/Nm3

SO2 < 100 ppm

NO2< 50 ppm

ESP and Low NOx Burners

2. Boiler 3 & 4 125 PM <150mg/Nm3 SO2 <100 ppm NO2<50 ppm


3. Boiler-5 (175 TPH)

Coal [29.16 MT/hr]

125 PM <150mg/Nm3 SO2 <100 ppm NO2<50 ppm


4. D.G. Sets (1875 KVA x 2)

HSD [400 lit/hr.

each]

36 PM <150mg/Nm3

SO2 <100 ppm

NO2<50 ppm

NA

5. D.G. Sets (750 KVA x 3)

HSD [200 lit/hr.

each]


6. D.G. Sets (1875 KVA x 2)

HSD [400 lit/hr.

each]


PROPOSED Flue Gas Emission

1. Boiler -6 (250 TPH)

Coal [42

MT/hr]

125 PM <150 mg/Nm3 SO2 < 100 ppm NO2< 50 ppm


2. D.G. Sets (1875 KVA x 1)

HSD [400 lit/hr.

each]


NA

3. Flaker Plant (Stand by)

Hydrogen [447.1 kg/hr.]


NA


Existing & Proposed

-Existing

EXISTING Process Gas Emission

1. Sodium Hypo Stack1(Caustic Plant)

-- 35 Cl2<9 mg/Nm3 Alkali Scrubber

2. HCl stack 1 (Caustic Plant)

-- 35 HCl<35 mg/Nm3 Water scrubber

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Page 129 of 167


-- --

35

having bubble cap tray absorption system.

4. Poly Aluminum Chloride plant

35 HCl<20 mg/Nm3

Cl2<9 mg/Nm3

Water scrubber system

5. Chlorinated Paraffin Plant

-- 35 HCl<20 mg/Nm3 Cl2<9 mg/Nm3

Alkali scrubbing system

6. Aluminum Chloride



7. Stable Bleaching Powder



8. Sodium Hypo Stack 2 (Caustic Plant)

-- 35 Cl2 < 9 mg/Nm3 Alkali Scrubber


-- 35 HCl< 35 mg/Nm3

Water scrubber having bubble cap tray absorption system.


-- 35

11. Poly Aluminum Chloride Liquid

35 HCl<20 mg/Nm3

Cl2<9 mg/Nm3

Water scrubber system

12. Poly Aluminum Chloride Powder

-- 35 3 stage Water scrubber system

13. Chlorinated Paraffin Plant

-- 35 HCl<20 mg/Nm3

Cl2<9 mg/Nm3


14. Aluminum Chloride

-- 35 HCl<20 mg/Nm3

Cl2<9 mg/Nm3


15. Stable Bleaching Powder

-- 35 HCl<20 mg/Nm3

Cl2<9 mg/Nm3


-Proposed

Not Applicable


of 167


Page 130 of 167

Existing fugitive emission mitigation measures: 1.) Material Unloading:

Water is being sprayed to suppress the particles and control the fugitive emission. 2.) Crusher House & transfer point:

All provided measures are provided which take care of the fugitive emissions likely to occur from crusher house and all the transfer points of the belt conveyor system.

3.) Material Bunkers: Bag filters has been provided at bunker to control the fugitive dust emission.

4.) Storage Yard: Air born dust is generated in minor quantity from the material storage yard due to wind, through the storage yard is properly covered. Unit has adopted water sprinkling method in storage yard to suppress dust generation. The unit has also developed plantation around the storage yard to control the fugitive emission.

5.) Silos provided for fly ash. Proposedfugitive emission mitigation measures:

1.) Most of the existing facility used for proposed expansion which already have adequate APCM

2.) Regular water sprinkling will be carried out. � Silos provided for fly ash.

F Hazardous waste

(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules

2016.

Existing & Proposed

i � Management of Hazardous Waste

Sr. No.

Name of Waste

Schedule/ Category

Quantity per Annum Mode of Storage & Disposal

Existing (a)

Proposed (b)

Total (a + b)

1. ETP Sludge 35.3 1524.50 MT

7 MT

1531.5 MT

Will be collected, stored, transported & Disposed at authorized TSDF site.

2. Spent Resin 35.2 0.42 MT 0.33 MT 0.75 MT Will be collected, stored, transported & Disposed at authorized TSDF site.

3. Spent Carbon 36.2 0.33 MT

0.07 MT 0.40 MT

Will be collected in drums, and will be sent for disposal at the designated TSDF site.

4. Used Oil 5.1 128 kl

100 kl

228 kl

Will be collected, stored and sold to authorized recycler.

5. Discarded Containers

33.1 25.2 MT 4.77 MT

30 MT Will be collected, decontamination, stored and reused/ sold to authorized recycler.

6. Discarded Bags/ Liners

33.1 41.8 MT

18 MT

59.8 MT

7. Dilute

Sulphuric

Acid (78%)

0 MT 11,500

MT

11,500

MT

Collection, storage, transportation and will be sold to Authorized actual users as per Rule 9 of Hazardous & Other waste (Management

of 167


Page 131 of 167

� Management of Non Hazardous Waste

&Transboundary Movement)Rules, 2016 as amended.

Sr. No.

Name of Waste

Schedule/ Category

Quantity per Annum Mode of Storage

& Disposal Existing

(a) Proposed

(b) Total

(a + b) 1. Brine/ process

Sludge -- 6066

MT 2934 MT

9000 MT

Will be collected, stored, transported & disposed off to secured landfill site.

2. Fly Ash -- 111600 MT

27702 MT

139302 MT

Will be sold fly ash to M/s. Anmol& Co., J.K. Lakshmi Cement, Ambuja Cement


(For HW management)

We have membership of BEIL-Dahej for TSDF



Waste:Brine Sludge Existing- 6066 MT/Annum Proposed-2426 MT/Annum Disposal:Will be collected, stored, transported &

disposed off to secured landfill site.

Waste: Fly Ash/ Bed Ash Existing- 1116000 MT/Annum Proposed 306000 MT/Annum Disposal: Sold fly ash to M/s. Anmol& Co., J.K.

Lakshmi Cement, AmbujaCement.



� Not applicable


� Not applicable


Anand Consultant, Ahmedabad during SEAC meeting dated 16/04/2019.

• PP presented that industrial effluent generation will be 8537.4 KLD and quantity of industrial

effluent recycled will be 13643 KLD. Upon asking PP could not explained satisfactorily reason of

higher recycled quantity than generation.

• 150 KLD industrial effluent generation is proposed from washing activity in proposed CPP.

Committee asked which type of washing activity will be carried out and what is requirement of

washing activity in CPP to which PP could not replied.

• PP has shown same quality/characteristics of industrial effluent RO Permeate, RO Reject, Boiler

Condensate and MEE condensate which is not convincible.

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• ESP and low NOx burner will be installed with proposed steam boiler.

• PP has addressed hazardous waste management. 7 MT/Year ETP sludge will be increased

against treatment of additional 936 KLD effluent generation which is found not convincible.

After deliberation, SEAC unanimously decided to consider the proposal after submission of the

following details:

1. Revise Water Balance Diagram and stream wise industrial effluent management.

2. Clarification of washing activity in CPP.

3. Adequacy of ETP,RO and MEE for treatment of industrial effluent. Feasibility report of reuse of

industrial effluent.

4. Steam wise characteristic of industrial effluent and ETP stage wise reduction of pollutants.

5. Proposal for reuse of industrial effluent instead of on land discharge.

6. Revise HW matrix and justification of ETP sludge quantity against treatment of industrial effluent.

16 SIA/GJ/IND2/33913/2019 M/s. Panoli Solid Waste Management Ltd.

Plot No. 18, GIDC Estate – Panoli, Tal: Ankleshwar, Dist: Bharuch.

Screening & Scoping

Category of the unit: 7(d)

Project status: New





• This is proposal is for setting up of new TSDF site of capacity as tabulated below.

SR.

NO.

NAME OF FACILITY CAPACITY

1 TSDF (TREATMENT, STORAGE AND DISPOSAL

FACILITY) – SECURED LANDFILL

125000 MT

• The project falls underCategory B of project activity 7(d)asper the schedule of EIA Notification 2006.



Sr.

no.

Particulars Details

A

A Total cost of Proposed Project (Rs. In Crores): 12.70 Crores

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B Total Plot area ( sq. meter) 30130.48 Sq. m.

Green belt area ( sq. meter) 314 Sq. m. + 8726.0 Sq.m


D Water

i


water, Tanker supply etc])

GIDC Water Supply

Status of permission from the concern authority. GIDC Water Supply


Sr.

No.

Usage Proposed Scenario (KL/Day)

Water Consumption

1. Industrial

Laboratory/Washing 0.5

Land Fill /Dumper ashing 8.0

2. Gardening 2.0

3. Domestic 3.0

Total(1+2+3) 13.5


2) Quantity to be recycled: 0.0 KLD



Sr. No. Usage Proposed Scenario (KL/Day)

Waste Water Generation

1. Industrial

Laboratory/Washing 0.5

Land Fill /Dumper ashing 8.0

2. Gardening 0.0

3. Domestic 2.4

Total(1+2+3) 10.9

-



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� No inhouse ETP


� There is no required to segregate stream of effluent




� Not Applicable


� Leachate from landfill site and wastewater from Laboratory/washing will be sent to

common Spray Dryer for further treatment.


Domestic: Domestic waste water will be disposed into soak pit.

Industrial: Leachate from landfill site and wastewater from Laboratory/washing will be

sent to common Spray Dryer for further treatment.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name

of CF

� Common Spray Dryer of M/s. PETL, Panoli



Common Spray Dryer of M/s. PETL, Panoli


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Total reuse-00 KLD

E Air



-

Sr. no.

Source of emission

With Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 DG Set – 250 KVA

11 HSD 500

Liter/Day

SPM SO2 NOx



- There will no process gas emission.

iii Fugitive emission details with its mitigation measures:

As below:

• A regular preventive maintenance schedule will be in place to replace or rectify all

gaskets and joints etc. as a part of ISO systems to ensure no fugitive emissions take

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place.

• Periodic monitoring of work area will be carried out to check the fugitive emission.

• Water sprinkling system will be installed.

F Hazardous wastes


Rules 2016.

i

Sr. no.

Type/Name of Hazardous waste

Specific Source of generation

Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Management of HW

1 User Oil D.G.Set

SCH-1/5.1 0.12 Collection, Storage and sale to approved recycler.

2 Discarded Bags

Materials SCH-1/33.1 2.4 Collection, Storage and sale to approved recycler.

-


(For HW management)

Not Applicable


(MSW and others)

There will no generate non

hazardous waste




� Not applicable as this project is TSDF.


� Not applicable as this project is TSDF.



Hazardous chemicals

Remarks

Storage tanks -- --

Drum/Barrel storage -- --

Applicability of PESO : Not Applicable

• Committee noted that M/s. Panoli Solid Waste Management Ltd proposes to install Treatment,

Storage and Disposal Facility at Panoli Industrial Estate of designed capacity will be about

1,25,000 MT. The volume of hazardous waste generated from the Panoli GIDC estate is

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estimated to be approximately 18,000 - 25,000 MT/annum. The land allocated for treatment and

disposal of hazardous waste (HW) is 17,100 Sq. Meter. Out of this area approximately 7,838 Sq.

Meter will be utilized for the first phase and 10,215 Sq. Meter will be utilized for the second

phase. The first phase shall be only in cutting having disposal below ground level. The second

phase will utilize same cell above ground with construction of bunds above the ground.

• Committee deliberated on size of the proposed TSDF site, Waste Acceptance Criteria,Manifest

System, Transportation of Hazardous Solid Waste from Generation Site to TSDF,Buffer zone,

Operation of TSDF disposal area,Leachate Management System etc.

• Earlier, PP has obtained Environmental Clearance for TSDF site from MoEF&CC. However,

validity of environmental clearance is expired.

• Industrial wastewater generated from laboratory and in the form of leachate will be collected and

send to Common Spray Dryer of M/s. PETL, Panoli.

• One HSD fired DG Set of capacity 250 KVA will be installed as standby power arrangement.

• After deliberation on various issues, following additional TORs were prescribed for the EIA

study to be carried out for proposed TSDF project:

1. Executive summary of the project – giving a prima facie idea of the objectives of the proposal, use

of resources, justification, etc. In addition, it should provide a compilation of EIA report, including

EMP and post project monitoring plan in brief. Need for the proposed TSDF site shall be justified in

detail.

2. The study area shall be up to a distance of 10 Km for air quality, soil, surface and ground water

quality from the boundary of the proposed project site.

3. Project sitespecific details such asdistance of the project site from the nearest (1) Village or human

habitation (2) Water Body : Creek / Nallah / Lake / Pond / Reservoir / Canal (3) NationalHighway

(4) State Highway (5) Railwayline(6) Heritage site (7) NationalPark / Wild LifeSanctuary / Reserve

Forest shall beincluded in the EIA reportto be prepared covering one season (other than monsoon)

data.

4. Present land use pattern of the study area shall be given based on recent satellite imagery as well

as field investigation clearly indicating, residential area, industries, vegetation (agricultural land,

irrigated, un-irrigated, un-cultivable land-as per the revenue records, forest land- as per the

records) grazing and waste land.

5. Comparison of alternate sites considered and the reasons for selecting the proposed site.

Conformity of the site with the prescribed guidelines in terms of habitation, river, highways,

railways, etc.

6. Justification for selecting particular capacity of the TSDF.

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7. Point wise compliance of guidelines published by MoEF & CPCB for siting and designing of the

proposed TSDF.

8. Land requirement for the facility including its break up for various purposes, its availability and

optimization.

9. Details of proposed layout clearly demarcating peripheral open path for unobstructed movement of

fire tender as well as various activities such as security, weighbridge, laboratory facility, temporary

hazardous waste storage areas, stabilization units, landfill, vehicle tyre wash areas, leachate

collection pits / wells and others such as admin building, canteen, worker’s room, health centers,

vehicle cleaning areas/ maintenance areas, greenbelt, internal roads, etc.

10. Water requirement for the project and permission from the concern authority.

11. Details on proposed recovery and recycling options, if any.

12. Details on hazardous waste inventorisation, segregation at source for compatibility with

transportation system and subsequent treatment.

13. Details on compliance program to the manifestation corresponding to waste transportation from

source to TSDF – adequate number of trucks, authorized dealers if any, features of the vehicles,

trained manpower, health and safety measures, identification of transportation routes by avoiding

vulnerable installations, frequency of truck movements, etc.

14. Details on proposed protocol for waste acceptance (verifying the waste quantity through weigh

bridge, frequency of calibration of weighing machine, system for sampling, testing parameters,

analysis methods, time lags, criteria for identifying the wastes which require stabilization prior to the

landfill, no. of people, qualifications, manifestation systems, etc.)

15. Details of the laboratory facilities and statement on adequacy including proposals for accreditation,

etc.

16. Design details of hazardous waste storage facilities (capacities, protocol for storing the segregated

hazardous waste, compliance to the statutory requirements and proposed safety precautions).

17. Details on proposed protocol for establishing the requirement of stabilization for various types of

hazardous waste.

18. Details of stabilization process (step by step procedure, proposed structures, equipments,

operations, general list of chemicals/material use, handling, personal protective equipments,

occupational health and safety measures, emergency preparedness, etc.

19. Details of the secured landfill (design, construction, operational and post closure maintenance)

including waste volume, landfill capacity, phase-wise landfill capacity development and utilization

plan, groundwater table, slope stability, compaction levels, liners, waste layers, capping

arrangement, gas collection, leachate collection, equipments, stability considerations,

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troubleshooting mechanism, peizometric wells, health and safety measures, etc.

20. Specification of liners (for bottom & sides) and covers to be used for the proposed landfill site.

21. Details on landfill gas collection / venting system and its management.

22. Details of leachate collection system – leachate generation rates, leachate collection network within

the landfill, external collection tanks (if any), treatment and disposal options (recirculation,

evaporation, treatment, discharge, etc.), overflow control measures during flood/heavy rains, etc.

23. Details on landfill closure and its post closure monitoring plan including leachate, landfill gas, etc.

24. Possibilities of seepage&soilcontamination and mitigation measureproposed to prevent the same.

25. Technical details of proposed Spray dryer including capacity, fuel to be used, adequacy etc.

Techno-economical viability of the proposed spray dryer. Control measures proposed for the spray

dryer unit in order to avoid/reduce gaseous emission/VOC from spray drying of leachate & washing

waste water.

26. Action plan for complete “Zero Liquid Discharge” (ZLD) system for proposed project.

27. Details of the existing access road(s)/walkways to the development site and its layout.

28. Details of vehicular traffic management within and outside the project area during waste

transportation.

29. Proposed financial model, creation of fund for future liabilities till 30 years of post-closure including

monitoring, etc.

30. Specific details of (i) Details of the utilities required, (v) Types & quantity of fuel to be used in each

of the utilities, (vi) Flue gas emission rate from each utility along with stackheight, (vii) Air Pollution

Control Measures proposed along with its adequacy, (viii) List the sources of fugitive emission from

the unit along with its quantification and proposed measures to control it.

31. Specific details of fugitive emission from the proposed TSDF project and proposed measures to

control it along with measures proposedtomonitor VOC within workarea.

32. Details of management of the hazardous wastes tobe generated from the project stating detail of

storageareafor each type of waste, its handling, its utilization and disposal etc. How the manual

handling of the hazardous wastes will be minimized.

33. Survey and topography details of the project area with appropriate contour interval.

34. Details of site topography along with the contour plan of the project area. Details of change in

topography of the area due to the project. Details of the management of the run off / rainwater

flowing through the existing natural drain / nallah / streams within the project site if any. Impacts on

the surface hydrology pattern due to the proposed project. Details of measures proposed to ensure

that natural drainage of the site will not be disturbed obstructed / disturbed and measures proposed

to protect existing natural drain / nallah / streams within the project site.

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35. Detailed plan to manage surface runoff in monsoon season. Measures proposed to avoid

contamination of surface runoff from the TSDF in monsoon season. How it will be ensured that

contaminated runoff won't flow outside the premises during rainy days.

36. Baseline data to be collected from the study area w.r.t. different components of environment viz.

air, noise, water, land, biology and socio-economics.

37. Soil map up to 5 feet prepared by concerned Government Authority.

38. Details on geological and hydro-geological features of the project area such as type of soil, nature

of soils, soil quality, soil properties including compressive strength, soil bearing capacity,

consolidation, etc.

39. One season site-specific meteorological data for temperature, relative humidity, hourly wind speed

and direction, rainfall, etc.

40. One complete season base line ambient air quality data (except monsoon) to be given along with

the dates of monitoring. The parameters to be covered shall be in accordance with the revised

National Ambient Air Quality Standards as well as project specific parameters (SO2, NOx, PM10,

PM2.5, VOC, Methane, CO2 etc.). The locations of the monitoring stations should be so decided so

as to take into consideration the pre-dominant downwind direction, population zone and sensitive

receptors. There should be at least one monitoring station in the upwind direction. There should be

at least one monitoring station in the pre dominant downwind direction at a location where

maximum ground level concentration is likely to occur.

41. Impact of the project on the AAQ of the area. Details of the model used and the input the

parameters used for modeling should be provided. The air quality contours may be plotted on a

location map showing the location of project site, habitation, sensitive receptors, if any. The wind

roses should also be shown on this map.

42. Details on noise levels at sensitive/commercial receptors.

43. Impact of the TSDF installation on the environment including the local hydrology, soil condition,

floral and faunal bio-diversity of the region and the mitigation measures proposed.

44. Details of flora and fauna duly authenticated should be provided. In case of any scheduled fauna,

conservation plan should be provided.

45. Demography details of all the villages falling within the study area.

46. While identifying the likely impacts, also include the following for analysis of significance and

required mitigation measures:

− impacts due to hazardous waste carrying trucks movement

− impacts due to leachate on surface water, soil and groundwater

− impacts due to air pollution including landfill gas

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− impacts due to odour pollution

− impacts due to noise

− impacts due to fugitive emissions

− impact on health of workers due to proposed activities

47. Proposed odour control measures

48. Detailed five year greenbelt development program including types &number of trees to be planted,

width of plantation, areaunder green belt development [with map], budgetary outlay; along with

commitment of the management to carry out the tree plantation activities outside the premises at

appropriate places in the nearby areas and elsewhere.

49. Details of existing trees to be protected / preserved / transplanted / removed. Permission of

concerned authority for cutting the trees within the premises. Time bound action plan for

compensatory tree plantation including details like number and type of trees to planted, area of tree

plantation, budgetary allocation for the same etc. should also be submitted.

50. Details of top soil management plan during construction phase. If the topsoil is proposed to be

preserved, the details relating to the quantity of topsoil stored, demarcated area on plan where it is

stored along with preservation & reutilization plan is to be given.

51. Monitoring of pollutants at receiving environment for all the appropriate notified parameters

– air quality, groundwater, surface water, leachate, gas quality, etc. during operational phase of the

project

− Leachate within the landfill and after treatment

− Groundwater quality around the landfill

− Surface water quality

− Gas quality within landfill (VOCs, H2S, etc.)

− Air quality above landfill

52. Details on monitoring of qualitative parameters – air quality, groundwater, surface water, leachate,

gas quality, etc. – location, frequency, parameters, etc. for all the appropriate notified parameters

for monitoring after landfill closure

− Leachate quality after treatment and at receiving environment

− Groundwater quality around the capped landfill

− Surface water quality

− Air quality above landfill and at gas vents

53. Details of in-house monitoring capabilities and the recognized agencies if proposed for conducting

monitoring.

54. Occupationalhealth impacts on the workers and mitigation measures proposedto avoid the human

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health hazards along with the personalprotectiveequipment to be provided to the workers. Plan for

pre-employment and periodicalmedical checkup of the workers.

55. Details on landfill closure and its post closure monitoring plan including leachate, landfill gas etc.

56. Details of the proposed overall safety and health protection measures during the project design,

construction and operation phases.

57. Details on surface/storm water management.

58. Risk assessment including prediction of the worst-case scenario and maximum credible accident

scenario. The worst-case scenario should take into account the maximum inventory of storage at

site at any point in time. The risk contours should be plotted on the plant layout map clearly

showing which of the activities would be affected in case of an accident taking place. Measures to

guard against fire hazards including details of firedetection and controlsystem and fire controlplan

showing hydrantpipeline network, provision of DG Sets, fire pumps, jockey pump, toxic gas

detectors etc.

59. Details of the emergency preparedness plan and on-site & off-site emergency management plan

and disaster management plan.

60. Details of disaster management plan during operation phase of the project should include also

scenario of natural catastrophe like earth quake, cyclone and floods in addition to other disasters.

The plan should include the details of (i) Emergency lighting plan (ii) details of power back up

system in the case of emergency (iii) firefighting arrangements (iv) first aid arrangement (v)

Training and Mock drill (vi) Emergency announcement system (vii) Signages (viii) location of

emergency stair cases and pathways etc.

61. Details of seismic zone of the project site and design aspects required to be adhered to as per

National standards.

62. Proposal for socio-economic development activities including communitywelfare program most

useful in the projectareafor the overallimprovement of the environment. Submit a detailed plan for

social corporate responsibilities, with appropriate budgetary provisions for the next five years and

activities proposed to be carried out; specific to the current demographic status of the area.

63. Detailed EMP including the protection and mitigation measures forimpact on human health and

environment as well as detailed monitoringplan and environmental managementcellproposed for

implementation and monitoring of EMP. The EMP should also include the concept of waste-

minimization, recycle/reuse/recover techniques, energy conservation, and naturalresource

conservation. Totalcapitalcost and recurring cost/annum earmarkedforenvironmentpollutioncontrol

measures.

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64. Plan for reuse / recycling of gypsum sludge and iron sludge along with the agreement letters of

end-users.

65. (a) Does the company have a well laid down Environment Policy approved by its Board of

Directors? If so, it may be detailed in the EIA report.

(b). Does the Environment Policy prescribe for standard operating process / procedures to bring

into focus any infringement / deviation / violation of the environmental or forest norms / conditions?

If so, it may be detailed in the EIA.

66. What is the hierarchical system or administrative order of the company to deal with the

environmental issues and for ensuring compliance with the EC conditions. Details of this system

may be given.

67. Does the company have a system of reporting of non-compliances / violations of environmental

norms to the Board of Directors of the company and / or shareholders or stakeholders at large?

This reporting mechanism should be detailed in the EIA Report.

68. Certificate of accreditation issued by the NABET, QCI to the environmental consultant should be

incorporated in the EIA Report.

69. A tabular chart with index for point-wise compliance of above TORs.

• The above mentioned project specific TORs/additional TORs and the model TORs available in the

MoEF&CC’s sector specific EIA Manual for “Common Hazardous waste TSDF” shall be considered

as generic TORs for preparation of the EIA report in addition to all the relevant information as per

the generic structure of EIA given in Appendix III in the EIA Notification, 2006.



Validity of ToR:

• The ToRs prescribed for the project will be valid for a period of three years for submission of EIA &

EMP report accordingly.

• The period of validity could be extended for a maximum period of one year provided an application

is made by the applicant to the Regulatory Authority, at least three months before the expiry of valid

period together with an updated Form-I, based on proper justification and also recommendation of

the SEAC.

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17 SIA/GJ/IND2/32982/2019 M/s. Janiya Fine Chem

Plot No. 718, GIDC, Palej,

Dist: Bharuch.

Screening & Scoping


Project status: New





• This is new unit proposes for manufacturing of synthetic organic chemicals as tabulated below.

SR. NO.

NAME OF PRODUCT CAS No. QUANTITY

(MT/MONTH) End Use of Products

GROUP A

1 Atorvastatin Calcium 134523-00-5

30

Dyslipidemia

2 Torsemide 56211-40-6 Edema

3 Amisulpiride 53583-79-2 Antipsychotic

4 BisoprololFumarate 66722-44-9 Antihypertensive

5 Topiramate 97240-79-4 Anticonvulsant

6 Levitiracetam 102767-28-2 Antiepileptic

7 Indole 120-72-9 Perfumery Product

8 Gama -Methyl Ionone 13720-12-2 Perfumery Product

9 Ionone 127-51-5 Perfumery Product

10 N- Methyl Ionone 1335-46-2 Perfumery Product

11 Alpha/beta Ionone- Product 127-41-3 Perfumery Product

12 7-Nitro indole 6960-42-5 Perfumery Product

13 5-Nitro indole 6146-52-7 Perfumery Product

OR GROUP B

1 Dabigatran 211915-06-9

10

Anticoagulant

2 Strontium Renelate 135459-90-4 Osteoporosis

3 Phenylepherine HCl 61-76-7 Decongestant

4 AzilsartanKamedoxomil 863031-21-4 Antidepressant

5 Dapoxetine 129938-20-1 Antidepressant

6 Rosuvastatin Calcium 147098-20-2 Dyslipidemia

7 Bromo Indole 10075-50-0 Perfumery Product

OR GROUP C

1 Levosulpiride 23672-07-3

3.75

Antipsychotic

2 Telmisartan 144701-48-4 Antihypertensive

3 Pregabaline 148553-50-8 Antiepileptic

4 Moxifloxacin 186826-86-8 Antibiotic

5 Glimepiride 93479-97-1 Antidiabetic

6 Losartan 114798-26-4 Antihypertensive

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7 Clopidogrel 113665-84-2 Antiplatelet

8 QuitiapineHemifumarate 111974-69-7 Schizophrenia

Total 30




Sr. no.

Particulars Details

A



Green belt area ( sq. meter) 300 Sq. m.

C Employment generation Direct = 15 Employees Indirect = 5 Employees

D Water

i


GIDC – Panoli


Category

Total Water Req. Quantity

KLD

Reuse Quantity

KLD

Fresh Water Quantity

KLD

(A) Domestic 2.5 - 2.5

(B) Gardening 1.5 - 1.5

(C) Industrial

Process 5.0 - 5.0

Washing 0.5 - 0.5

Boiler 12.0 - 12.0

Cooling 0.5 - 0.5

Other (Scrubbing) 2.0 - 2.0

Industrial Total 20.0 - 20.0

Total (A + B + C) 24.0 - 24.0

1) Total water requirement for the project: 24.0 KLD 2) Quantity to be recycled:--- KLD 3) Total fresh water requirement: 24.0 KLD


Category Waste water KLD

Remarks

(A) Domestic 2.2 Septic tank & Soak pit

(B) Industrial

Process 5.0 Total Waste Water 6.5 KLDwill be treated in ETP & sent to Common MEE (M/s. BEIL, Ankleshwar).

Washing 0.5

Boiler 0.4

Cooling 0.1

Other (10% NaCl) 0.5

Scrubbing Solution (NaBr/HBr) 0.5 To End User

Scrubbing Solution (Na2HSO3) 0.5 To End User

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Scrubbing Solution (Liq. Ammonia) 0.5 Reuse within premises

Total Industrial waste water 8.0 -

Total [A + B] 10.2 -

-

iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.

� In-house ETP (Primary Treatment) – 10.0 KLD

Treatment scheme including segregation at source. � 5.0 KLD from Process, 0.5 KLD from Washing, 0.4 KLD from Boiler & 0.1 KLD from Cooling

Tower & 0.5 KLD from Scrubber – Waste Water will be treated in in-house ETP and then final treated water i.e 6.5 KLD will be sent to common MEE of M/s. BEIL – Ankleshwar.

Note: (In case of CETP discharge) : Management of waste water keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.

� Not Applicable, Treated Effluent 6.5 KLD will be sent to Common MEE of M/s. BEIL-Ankleshwar.

Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): � Not Applicable, Treated Effluent 6.5 KLD will be sent to Common MEE of M/s. BEIL-

Ankleshwar.


Domestic: Domestic wastewater 2.2 KLD will be treated & discharged through Septic Tank &

Soak Pit System.

Industrial:

• Ind. Effluent @ 6.5 KLD

• Waste Water 6.5 KLDwill be treated in ETP & sent to Common MEE (M/s. BEIL, Ankleshwar).

• Scrubbing solution i.e., 10% NaCl @ 0.5 KLD combined with effluent &sent to Common MEE (M/s. BEIL, Ankleshwar)

• Scrubbing solution i.e, NaBr / HBr @ 0.5 KLD will be sell to end user.

• Scrubbing solution i.e., Na2HSO3 @ 0.5 KLD will be sell to end user.

• Scrubbing solution i.e, Liq. Ammonia @ 0.5 KLD will be reused within premises.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name of CF � M/s. BEIL- Ankleshwar (Common-MEE)

Membership of Common facility (CF) (For waste water treatment)

Unit has obtained membership of Common MEE of M/S BEIL, Ankleshwar


497


Total reuse:- NIL KLD

E Air

i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

-

Sr. no.

Source of emission

With Capacity

Height (meter)

1 Steam Boiler

(1.0 TPH) 12/0.250

2

Thermic Fluid

Heater (5 Lac

KCal/Hr.)

11/0.5

3 D.G. Set

(100 KVA) 11/0.25

-

ii Process gas emission details i.e. Type of pollutant gases (SO


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Reuse/Recycle details (KLD)



Type of Fuel


Type of emissions

i.e. Air Pollutants

12/0.250

Bio Coal/ Wood

Briquette OR

Natural Gas

1 T/Day

OR 500

SCM/Day

PM SO2 NOX

11/0.5 Natural

Gas 500

SCM/Day

PM SO2 NOX

11/0.25 Diesel 15 lit/Hr. PM SO2 NOX

Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl

Page 147 of 167


Type of emissions

i.e. Air Pollutants


Measures (APCM)

MCS + Bag Filter

OR Adequate

Stack Height



Cl2, NOx etc.)

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-

Sr. no.

Specific Source of emission

(Name of the Product & Process)

Type of emission

Stack/Vent

Height (meter)


Measures (APCM)

1 Bromo Indole - Reaction Vessel

(Bromination) HBr: 20 mg/Nm3

11 / 0.2 Two Stage

Water+Alkali Scrubber

2 Dapoxetine HCl - Reaction Vessel

(Ammonia) NH3: 175 mg/Nm3

11 / 0.2 Two Stage

Water Scrubber

3 Dabigatran - Reaction Vessel

(Sulphonation) SO2: 40 mg/Nm3

11 / 0.2 Two Stage

Alkali Scrubber

4 Glimepiride - Reaction Vessel

(Chlorination) HCl: 20 mg/Nm3

11 / 0.2 Two Stage

Alkali Scrubber

-

Iii Fugitive emission details with its mitigation measures: As below:

- Whole process will be carried out in close loop. - Pipe line will be having minimum flange. - Pump with double mechanical seals - Proper ventilation.

F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.

I

Sr.

No.

Type of

Hazardous

Waste

Hazardous

Waste

Category &

Schedule

Source Qty.

(MT/

Annum)

Mode of disposal

1 ETP Sludge 35.3/SCH-I ETP 200 Collection, Storage,

Transportation, disposal at

nearest TSDF site. (M/s.

BEIL, Ankleshwar)

2 Used

Oil/Spent Oil

5.1/SCH-I TFH, DG &

Other

Utilities

0.15 Collection, Storage,

Transportation & Reuse or

sale to authorized

reprocessors.

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Page 149 of 167

3 Discarded

Containers/

Bags/Liners

33.1/SCH-I Raw

Material

Supplier

2.0 Collection, Storage,

Transportation & Reuse/

Sale to Authorized Vendor.

4 Distillation

Residue

20.3/SCH-I Mfg.

Process

600 Collection, Storage,

Transportation & given to

cement industries for co-

processing or disposal at

nearest CHWIF ((M/s.

BEIL, Ankleshwar).

5 Process

Waste

(Organic)

28.1/SCH-I Mfg.

Process


Transportation & given to

cement industries for co-

processing or disposal at

nearest CHWIF ((M/s.

BEIL, Ankleshwar).

6 Process

Waste

(Inorganic)

28.1/SCH-I Mfg.

Process


Transportation, disposal at

nearest TSDF site. (M/s.

BEIL, Ankleshwar)

7 Spent Solvent 28.6/SCH-I Mfg.

Process


Transportation recovered

& recycled by Solvent

Distillation Plant within

premises.

8 Spent Carbon 28.3/SCH-I Mfg.

Process


Transportation send to

cement industries for co

processing or send to

CHWIF site (M/s. BEIL,

Ankleshwar).

9 Spent

Catalyst

28.2/SCH-I Mfg.

Process


Transportation & disposal

at nearest CHWIF or

TSDF site (M/s. BEIL,

Ankleshwar).

10 Scrubbing

Solution

10% NaCl

- Mfg.

Process of

Glimepiride

180 KL Treated with effluent,

Collection, Storage,

Transportation Send to

Common MEE (M/s. BEIL-

Ankleshwar).

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Page 150 of 167

-

11 Scrubbing

Solution

Sodium

Bromide

(NaBr)/

Hydrogen

Bromide

(HBr)

- Mfg.

Process of

Bromo

Indole

180 KL Collection, Storage,

Transportation Sell to End

Users having permission

under Rule-9. (Bromine

Recovery)

12 Scrubbing

Solution

Sodium Bi

Sulphite

(Na2HSO3)

- Mfg.

Process of

Dabigatran

180 KL Collection, Storage,

Transportation Sell to End

Users having permission

under Rule-9.

13 Scrubbing

Solution

Liq. Ammonia

- Mfg.

Process of

Dapoxetine

HCl

180 KL Collection, Storage &

Reuse within premises.

(In the Mfg. process of

Glimperidine – 495 MT)

ii Membership details of TSDF, CHWIF etc. (For HW management)

Unit has membership of Common TSDF & Incineration Facility of M/s. BEIL, Ankleshwar.


No such waste will generate


i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)

Product Spent solvent Qty.(MT)/

month Reuse /

Recovered %

Recovery

GROUP A

Atorvastatin Calcium Methanol 210 205.5 97.9

Isopropyl alcohol 96 93.9 97.8

Torsemide mix. Xylene 72 70.5 97.9

Isopropyl alcohol 82.8 81.0 97.8

Amisulpiride Acetone 94.5 92.55 97.9


BisoprololFumarate

Toluene 82.5 80.7 97.8

Methanol 93.75 89.25 95.2

Methylene chloride 63.75 62.4 97.9

Acetone 120 117.6 98.0

Topiramate

Acetone 126 123.3 97.9

n-Hexane 82.2 80.4 97.8

Toluene 96 93.9 97.8

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Ethyl Acetate 96.6 94.59 97.9

Isopropyl Alcohol 84.9 83.1 97.9

Levetiracetam Ethyl Acetate 484.8 473.1 97.6

Indole Toluene 157.51 155.4 98.7

Ionone Acetone 9.06 8.86 97.8

Alpha/beta Ionone Acetone 9.06 8.86 97.8

5-Nitro indole Ethanol 240.64 235.8 98.0

OR GROUP B

Dabigatran

Toluene 60 55 91.7

Methylene chloride 50 46 92.0

Acetone 58 52.6 90.7

Ethyl Acetate 70 65.2 93.1

Cyclo Hexane 20 19 95.0

Ethanol 6.4 5.6 87.5

Strontium Renelate


Cyclo Hexane 56.5 55.3 97.9

Acetone 40 39.2 98.0

Phenylepherine HCl

Toluene 26.3 25.7 97.7

Methanol 50.5 45.4 89.9

Isopropyl alcohol 64 62.7 98.0

Dapoxetine

Methanol 50 47.5 95.0

Toluene 83.33 81.7 98.0

Acetone 83.33 79.2 95.0

Rosuvastatin Calcium


Acetone 33.39 33.0 98.8

Toluene 82.54 81.42 98.6

Methanol 50.8 50.41 99.2


Bromo Indole Methanol 26.9 26.3 97.8

Acetone 12.5 12.3 98.4

OR GROUP C

Levosulpiride

Methanol 43.5 40.125 92.2


Toluene 12.375 11.625 93.9

Telmisartan Methanol 13.24 12.8 96.7


Pregabaline Isopropyl alcohol 26.46 25.15 95.0

Moxifloxacin Methanol 6.19 5.941 96.0

Glimepiride n-Hexane 16.13 15.375 95.3

Methanol 29.82 28.3125 94.9

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Page 152 of 167

Acetone 71.25 67.875 95.3

Dimethyl Formamide 49.31 46.875 95.1

Di isopropyl Ether 1.61 1.5375 95.5

Losartan Toluene 77.18 75.1 97.3

Clopidogrel


Methanol 3.46 3.392 98.0

Acetone 4.62 4.5 97.4


QuitiapineHemifumarate

Toluene 51.03 48.988 96.0

Methanol 90.72 87.068 96.0

Acetone 18.9 18.143 96.0

Dimethyl Formamide 15.12 14.511 96.0

Ii VOC emission sources and its mitigation measures

• Sources - Charging Materials

• Measures

- Enclose Process

- Minimum flanges & joints

- Handled by pump with double mechanical seals

- Proper Ventilation

- Adequate PPEs



Storage tanks HCL, H2SO4, Acetone, Isopropyl alcohol, Methanol, Mix Xylene, n-Hexane, Toluene

Storage condition as ATP

Drum/Barrel storage

Acetic Acid, Ethanol, Methylene Chloride, Methyl Ethyl Ketone, Poly Phosphoric Acid, Thionyl Chloride, Triethyl amine, Bromine (Glass Bottle)


Cylinder Ammonia Gas, Hydrogen Gas & HCl Gas




Green Leaf Envirotech Pvt. Ltd., Surat during SEAC meeting dated 16/04/2019.

• Committee noted that this proposal is for manufacturing of Synthetic Organic Chemicals at GIDC

Palej, Bharuch.

• Industrial effluent will be treated in ETP consists of primary treatment units and then sent to

CMEE of M/s. BEIL for further treatment & disposal.

• Bio coal/agro waste briquette, natural gas and diesel will be used as fuel. Cyclone separator and

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Page 153 of 167

bag filter will be provided as APCM with steam boiler.Two stage alkali scrubber will be provided

with chlorination and sulphonation reactors.

• Liq. Ammonia (bleed liquor) will be reused in mfg of process of Glimperidine within premises.

Sodium Bi Sulphite and Sodium Bromide (bleed liquors) will be sent to actual end users having

rule-9 permission as per the HWM Rules.







2. Explore possibility of reuse of treated effluent for industrial purpose within premises.

3. To address management of off specification and date expired products as per the HWM

Rules, 2016.

4. Safety precautions for Hydrogen,Ammonia, HCl gas storage, handling and transportation as

per the prevailing law/rules & regulations.





report.






form.








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Page 154 of 167

• The TOR prescribed as above and as per the standard TOR approved bySEIAAand the model ToRs

available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’

shall be considered as generic TORs for preparation of the EIA report in addition to all the relevant

information as per the generic structure of EIA given in Appendix III in the EIA Notification, 2006.



18 SIA/GJ/IND2/30839/2019 M/s. Meghmani Dyes & Intermediates LLP

Plot No.: 96, 97, 98, 99, 100, 102 & 84

Phase - II, GIDC Vatva, Dist.: Ahmedabad

Screening & Scoping







• This is an existing unit engaged in manufacturing of synthetic organic chemicals and now proposes

for expansion as tabulated below.

Sr.

no.

Name of the Products CAS no. /

CI no.

Quantity, MT/Month End-use of

the products Existing Proposed Total

Existing Products

1 to

100

• REACTIVE RED 3BX, E4BA,

ME6BL - 6BX, BORDEAUX,

HE3B, HE7B, ME3GL, BB,

M8B - C & B, BX – R, BX- NEW

– RB, 23, PB, 5-B-R, P3B – R,

7BX – R, M5B-C5B, H8B, BSX,

RR, HE8BA, C2G, 81, DIRECT

RED 227(ROSE FR), ACID

RED 57, 131, ACID SCARLET

4 BS,

• REACTIVE ORANGE 2 RX, 3

R, HER, H2R, M2R, 78,

-- 125 -- 125 Dyeing &

Printing

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Page 155 of 167

• REACTIVE BROWN GR, MIX,

• REACTIVE GREEN B-HE4BD,

• REACTIVE MAGENTA HB,

MB,

• REACTIVE VIOLET 5R, M4R-

C4R,

• REACTIVE TURQ BLUE G,

H5G, HA,

• REACTIVE BLUE 5 RH-H5R,

HER, 3 R, BRF, 4 GX-F2G-RB,

HERD, BB, 38-GREEN HE6BL,

199, R, M2R, MR-2B, GG-H

H2GL, M4GD, RR, MX7RX,

ACID BLUE 45

• REACTIVE NAVY BLUE RGB,

HE2R-HR, RX-BFN, RNX-3GX,

• REACTIVE PURPLE H3R,

• REACTIVE YELLOW 3RX,

ME4GL-4GL, H4G, FG, RNL,

GR, M4R, HE4G, GL, HE6G,

M8G, RJ, RL, GCH, SWT, GN,

ACID YELLOW H2, REACTIVE

GOLDEN YELLOW HR, HER-

HE4R-HEXL, MR,

• REACTIVE BLACK B, GR-

HFGR, GRD-RD, GF-B-N, RL,

GRP, HN, MIX, GL, PL, BB,

ACID BLACK 107, 194, 52,

DIRECT BLACK B

Proposed Products

101 REACTIVE BLACK -- -- 500 500 Dyeing &

Printing a. REACTIVE BLACK B 17095-24-8

b. REACTIVE BLACK MIX – --

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Page 156 of 167

WNN/R/G/XLW/DN/GHF/CL5/

GR/GF/ MNM/MNG

102 REACTIVE YELLOW -- -- 220 220

a. REACTIVE YELLOW 3RX 80156-97-4

b. REACTIVE YELLOW 4GL 84000-63-5

c. REACTIVE YELLOW XL 780759-89-9

d. REACTIVE YELLOW WNN 607724-40-3

e. REACTIVE YELLOW MIX –

MGB/HB/ULTRA YELLOW

MGB/ HW/ S3R

--

103 REACTIVE ORANGE -- -- 45 45

a. REACTIVE ORANGE H2R 12225-85-3

b. REACTIVE ORANGE 2RX 79809-27-1

c. REACTIVE ORANGE 3R (RR) 12225-83-1

d. REACTIVE ORANGE WNN

(XLR) 71902-15-3

e. REACTIVE ORANGE CD 292827-64-6

f. REACTIVE ORANGE HER --

g. REACTIVE ORANGE MIX --

104 REACTIVE RED -- -- 150 150

a. REACTIVE RED CD 12226-12-9

b. REACTIVE RED 5BX 111211-40-6

c. REACTIVE RED 3GX 80019-42-7

d. REACTIVE RED 3BX 93050-79-4

e. REACTIVE RED CRIMSON

HEXL 71002-20-5

f. REACTIVE RED RUBIN XL 125830-50-4

g. REACTIVE RED BS 94158-79-9

h. REACTIVE RED RB 125830-50-4

i. REACTIVE RED 2GX 93051-42-4

j. REACTIVE RED CAR --

k. REACTIVE RED MIX – --

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Page 157 of 167

XL3B/MGB/MD/MGB/XL/XL4B/

K3BS/ RGB

105 REACTIVE BLUE -- -- 75 75

a. REACTIVE NAVY BLUE

RGB 100 93951-21-4

b. REACTIVE NAVY BLUE GG 84229-70-9

c. REACTIVE BLUE BB 90341-71-2

d. REACTIVE BLUE 3GX 80315-17-9

e. REACTIVE BLUE BRX 86024-59-1

f. REACTIVE BLUE HEGN --

g. REACTIVE BLUE MIX –

XL/ Navy Blue XL/ MGB/ SG/

BLRB/ BFN

--

106 OPTICAL BRIGHTENING AGENT

– 2 B 27344-06-5

-- 10 10 Fluorescent

Whitening

agent for

paper, textile,

detergent and

polymers.


– BSU 68971-49-3

-- 30 30


– DMX 16090-02-1

-- 250 250


– BBU 16470-24-9

-- 35 35


– BA 4193-55-9

-- 40 40


– 4BB 4404-43-7

-- 225 225


– DT 27344-41-8

-- 20 20

Total 125 1600 1725




Sr.

no.

Particulars Details

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Page 158 of 167


(Rs. in Crores):

Existing: 11.8 Crores

Proposed: 6.0 Crores

Total: 17.8 Crores

B Total Plot area

( sq. meter)


Proposed: 0 Sq. m.(Existing

undeveloped area will be used for

proposed expansion)

Total: 16,802 Sq. m.

Green belt area

( sq. meter)


Proposed: 150 Sq. m.

Total: 2,650 Sq. m.

C Employment generation Existing: 216 nos.

Proposed: 135 nos.

Total: 351 nos.

D Water

i



GIDC


In Process

ii

Water consumption (KLD)

Sr.

No. Description

Water Consumption (KL/day)

Existing

Proposed Total

Fresh Recycle

d Water Fresh

Recycle

d Water

A Domestic 10 3 7 13 7

B Industrial

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Page 159 of 167

*After proposed expansion entire washing requirement will be met by recycled

water



3) Total fresh water requirement: 353 KLD v

1. Process 46 204 20 250 20

2. Boiler 45 12 38 57 38

3. Cooling

(make-up) 10 3 7 13 7

4. Washing 40 0 80 0* 80

Total (B) 141 219 145 320 145

C Gardening -- 20 -- 20 --

Total (A+B+C) 151 242 152 353 152

iii

Waste water generation (KLD)

Sr.

No. Description

Wastewater Generation (KL/day)

Mode of Disposal


A Domestic 7 7 14 Septic Tank/Soak

Pit

B Industrial

1. Process 35 108 143

Treated in

MEE/ETP

2. Boiler (Blow-down) 38 3 41 Pass through RO

System 3. Cooling (Purge) 10 2 12

4. Washing 40 40 80

5. Reject of RO +

Nutch Filter -- 30 30

Treated in MEE

Total (B) 123 183 306 --

C Gardening -- -- -- --

Total (A+B+C) 130 190 320 --

iv Treatment facility within premises with capacity [For existing and Proposed]

[In-house ETP (Primary, Secondary, Tertiary), MEE, RO, STP etc.

of 167


Page 160 of 167

� Existing: ETP – 130 KLD

� Proposed: ETP – RO – 140 KLD , MEE – 50 KLD, ETP – 123 KLD (Chlorination

stage is included)

(152 KLD will be recycled after treatment)


Domestic: 14 KLD (existing + proposed) domestic waste water generated will

be disposed into septic tank /soak pit system.

Industrial: 20 KLD OBA- DT product waste water along with 30 KLD (RO +

Filter Nutch Reject) will be treated in MEE, 123 KLD remaining

process wastewater will be passed through chlorination stage

before its treatement in ETP. 133 KLD (12 KLD Cooling purge + 41

KLD Boiler Blow-down + 80 KLD Washing waste water) will be

treated in RO. Out of 133 KLD, 104 KLD permeate will be recycle

with 48 KLD MEE in boiler, cooling, process, domestic and washing

activity.


etc.

Name of Common facility

� CETP, Vatva



We have membership to send 250 KL/day wastewater to CETP, vatva.


Water Balance Diagram(Existing + Proposed)(all numeric values are in KLD)

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Page 161 of 167



Total reuse 152 KLD

Source of waste water

for reuse with

quantity in KLD

Application area


Remarks regarding

feasibility to reuse i.e.

w/w characteristics

(COD, BOD, TDS etc.)

48 KLD MEE

condensate and 104

KLD RO permeate will

be recycled.

Total 152 KLD (48

KLD MEE

condensate and 104

KLD RO permeate)

will be recycled in

boiler, cooling,

process, domestic

and washing activity.

� pH : 7- 8.5

� Suspended Solids :

150 – 200 mg/l

� TDS :1500 – 2000

mg/l

� Oil & Grease : 5-10

mg/l

� COD : 80-100 mg/l

� BOD : 10-20 mg/l

E Air



Existing & Proposed

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Page 162 of 167

- Existing

Sr.

no

.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

1 Steam

Boiler 33

Natural

Gas 390

m3/hr

PM

SOx

NOx

--

2 D.G. Set

(1000

KVA)

11 Natural

Gas

PM

SOx

NOx

--

- Proposed

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

1 Steam

Boiler

(4 MT/hr )

40

Importe

d Coal/

Agro

waste

540

Kg/Hr

PM

SOx

NOx

Cyclone

Separator

& Bag filter

2

Hot air

Generator

(20 Lac

Kcal)

40

Importe

d Coal/

Agro

waste

280

Kg/Hr

PM

SOx

NOx

Cyclone

Separator

& Bag filter

3

Hot air

Generator

(11 Lac

Kcal)

35

Importe

d Coal/

Agro

waste

160

Kg/Hr

PM

SOx

NOx

Cyclone

Separator

& Bag filter


Existing & Proposed

- Existing

Sr.

no.

Specific

Source of

emission

(Name of the

Type of

emission

Stack/Vent

Height

(meter)


Measures

(APCM)

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Page 163 of 167

Product &

Process)

1 Spray Dryer

(2 Nos.) PM 22 each

Cyclone Separator

followed by Water

Scrubber

- Proposed

Sr.

no.

Specific Source

of emission

(Name of the

Product &

Process)

Type of

emission

Stack/Vent

Height

(meter)


Measures

(APCM)

1 Spin Flash Dryer

(PNG based- In

Built HAG)

PM 15

Cyclone Separator

followed by Bag Filter in

closed system

2 Spin Flash Dryer

(PNG based- In

Built HAG)

PM 15

Cyclone Separator


closed system

3 Spray dryer

(PNG based- In

Built HAG)

PM 21

Cyclone Separator


closed system

4 Spray dryer PM 25

Cyclone Separator

followed by two stage

Water Scrubber


� Concrete road will be developed within plot premises to avoid fugitive dust due to

vehicle movement.

� Manufacturing activity will be carried out in closed reactors / vessels and regular

checking and maintenance of the same will be carried out to avoid any leakage and

relative fugitive emissions.

� All the raw materials will be stored in closed containers and in sealed bags and will

be handled through closed system to avoid the handling losses and relative fugitive

emissions.

� Water sprinkling will be done to avoid dust emission.

F Hazardous waste


Rules 2016.

i Existing & Proposed

Sr. Type/Name Specific Category Quantity Management of

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Page 164 of 167

no. of

Hazardous

waste

Source of

generation

(Name of

the Activity,

Product

etc.)

and

Schedule

as per

HW

Rules.

(MT/Annum)

HW


1 ETP sludge

From ETP 35.3

(Sch-I)

50 MT 90 MT 140

MT

Will be collected,

stored,

transported and

disposed at

GPCB approved

TSDF site.

MEE

residue

From MEE -- 30 MT 30

MT

Will be collected,

stored,

transported and

disposed at

GPCB approved

TSDF site.

2 Used oil From

Equip-

ments or

D.G. Set

5.1

(Sch-I)

0.2MT 0.3 MT 0.5

MT

Will be collected,

stored and

disposed by

selling it to

registered

recyclers/refiner

s.

3 Discarded Container/ liners/ Bags

From raw

material

handling

33.1

(Sch-I)

8100 Nos.

10,000

Nos.

18,100

Nos.

Will be collected,

stored and

disposed by

selling it to

registered

vendors.

4 Spent Ion Exchange resin

From

Water

Softener

Plant

35.2

(Sch-I)

-- 8.4 Kgs 8.4 Kgs Will be collected,

stored,

transported and

disposed at

GPCB approved

TSDF site.

-


(For HW management)

M/s. Ecocare Infrastructure Pvt. Ltd.

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Page 165 of 167



--



� Dimethyl Sulfoxide – 98 %


� Closed loop systems, double mechanical seal pumps will be provided to reduce

VOC emission as much as possible.

• Technical presentation was made by the project proponent along with their consultant/expert Anand

Consultant, Ahmedabad during SEAC meeting dated 16/04/2019.

• Committee noted that this unit has proposed expansion in Dye manufacturing at GIDC, Vatva.

• Wastewater generated from OBA – DT production along with RO reject and Nutch Filter reject will

be treated in Multiple Effect Evaporator (MEE). Concentrated slurry from MEE will be filtered in filter

nutch and filtrate will be taken back to MEE. Condensate will be reused. Process stream other than

OBA-DT will be passed through chlorination stage (to reduce COD load) followed by ETP before its

discharge to CETP vatva for further treatment.

• Due to chlorination process COD of approximately 12000 ppm will reduced to 3000 ppm and will

therefore made the 3000 ppm effluent amenable to biological treatment.

• Cooling purge, boiler blow-down and washing stream will be treated in RO plant. RO reject will be

treated in MEE while permeate from said RO will be recycled in washing, boiler, cooling and

domestic activity. Sludge generated from ETP along with MEE salt will be sent to TSDF site.

• PP assured that there will be no increase in organic load of effluent being discharged to CETP,

Vatva after proposed expansion.

• Imported coal/ agro waste will be used in proposed boiler and HAG. Cyclone separator followed by

bag filter will be provided as APCM with proposed boiler and HAG. Cyclone Separator followed by

two stage water scrubber will be provided as APCM with proposed spray dryer.

• ETP sludge and MEE salt will be sent to TSDF for landfilling.

• Considering the above project details, after detailed discussion, the terms of reference (ToR)

were prescribed as below and as per the standard TOR for the Synthetic Organic Chemical

projects recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and

approved by SEIAA in its 12th meeting dated 16/09/2017 for the EIA study to be done covering

10 Km radial distance from the project boundary.


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Page 166 of 167



3. Stream wise existing and proposed effluent characteristics and its treatability study.

4. Adequacy assessment report of Chlorination Treatment for High COD effluent treatment and

technical justification on ETP treated effluent will confirm CETP, Vatva inlet norms prescribed

by GPCB with reference to FDS/TDS parameter after proposed expansion duly certified by

GPCB recognized Auditor.

5. Provide STP considering 14 KLD sewage generation or treat along with industrial effluent in

ETP.

6. Safety precautions for Chlorine storage, handling, transportation and incase of accident as

per prevailing law/rules & regulations







8. Compliance of MoEF&CC’s OM dated 01/05/2018 regarding “Corporate Environment


be made as per MoEF&CC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various

activities therein. The details of fund allocation and activities for CER shall be incorporated in

EIA/EMP report.






form.



12. Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent proposed

for use in-house with detailed chemical properties including vapor pressure. LDAR shall

endeavour prevention of losses of solvents to the best minimum extent.

13. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard during

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Page 167 of 167

unloading, storage, transportation, handling and processing of Solvents.

14. Segregation of waste water streams based on characteristics and its proper management

keeping in view direction under section 18 (1) (b) of the Water (Prevention and Control of

Pollution) act, 1974 issued by CPCB regarding compliance of CETP.





2006.



Meeting ended with thanks to the Chair.

Minutes approved by:

1. Shri Dinesh Misra, Chairman, SEAC

2. Shri S. C. Srivastav, Vice Chairman, SEAC

3. Shri R. J. Shah, Member, SEAC

4. Shri V. N. Patel, Member, SEAC

5. Dr. V. K. Jain, Member, SEAC

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