Minutes of the 476 meeting of the State Level Expert ... Minutes of the 476th I.pdf · Page 2 of 92 476th meeting of SEAC-Gujarat, Dated 23.01.2019 Page 2 of 92 Sulpho Succinate (DOSS)

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476th meeting of SEAC-Gujarat, Dated 23.01.2019

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Minutes of the 476th meeting of the State Level Expert Appraisal Committee held on 23/01/2019

at Geer Foundation, Sector 9, Indroda Park, Gandhinagar.

The 476th meeting of the State Level Expert Appraisal Committee (SEAC) was held on 23rd January

2019 at Geer Foundation, Sector 9, Indroda Park, Gandhinagar. Following members attended the

meeting:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

4. Shri A.K. Muley, Member, SEAC

5. Shri K. C. Mistry, Member Secretary, SEAC

The agenda of TOR/Scoping cases and Appraisal was taken up. The applicants made presentations on

the activities to be carried out along with other details furnished in the Form-1, PFR, EIA-EMP reports

and other reports.

1. SIA/GJ/IND2/22191/2018 M/s. Navkar Chmicals Plot No. 3010, GIDC Panoli,

Tal,: Ankleshwar, Dist.: Bharuch

Appraisal

Category of the unit : 5(f)

Project status: New

• Project Proponent (PP) has submitted online application vide no. SIA/GJ/IND2/22191/2018 dated 15/01/2019

for obtaining Environmental Clearance.

• The SEAC had recommended TOR to SEIAA and SEIAA issued TOR to PP vide their letter dated 13/06/2019.

• Project proponent has submitted EIA Report prepared by M/s. Aqua Air Environmental Engineering Pvt Ltd.

based on the TOR issued by SEIAA

• This is an existing unit and now proposes 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

Existing

1 Dispersing Agents - 20 Textile / Construction

2 Dry Sodium Sulphate 7757-82-6 15 --

After getting EC and CTE for proposed products, company will discontinue the existing

production.

Proposed

1

Naphthalene

Formaldehyde Sodium

Sulphonnate

36290-04-7 100 Textile / Construction

2 Di-Octyle Sodium 577-11-7 100 Textile

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Sulpho

Succinate (DOSS)

Total 200

• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.

• PP was called for presentation in the SEAC meeting dated 23/01/2019.

• 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):

1 Crores

B Total Plot area( sq. meter) 1000 Sq. m.

Green belt area ( sq. meter)

330 Sq. m.

C Employment generation 10

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. Unit has obtained permission for water supply.

ii Water consumption (KLD)

Category KLD Remarks

(A) Domestic 3

(B) Gardening 1.5

(C) Industrial

Process 3 Washing 0.2

Boiler 1

Cooling 0.5

Others (Scrubbing) 0.3

Industrial Total 5.0

Total (A + B + C) 9.5 0.7 KL/day will be reuse in process and Boiler

1) Total water requirement for the project: 9.5 KLD

2) Quantity to be recycled: 0.7 KLD

3) Total fresh water requirement: 8.8 KLD

iii

Waste water generation (KLD)

Category

Waste water KLD

Remarks

(A) Domestic 2.5 Disposed through Septic Tank & Soak Pit

(B) Industrial

Process Nil

Washing (equipment) 0.2 reuse in process for next batch

Boiler 0.1 reuse in Boiler

Cooling 0.1

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Others (scrubber) 0.3 reuse in process

Total Industrial waste water

0.7

Total [A + B] 3.2

-

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

Soak Pit/Septic Tank: 2.5 KLD

v Mode of Disposal & Final meeting point

Domestic:

Domestic wastewater (2.5 KL/Day) will be disposed through Soak Pit/Septic Tank.

Industrial: All effluent will be reused within premises.

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

All effluent will be reused within premises.

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

Not Required

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

viii Reuse/Recycle details (KLD)

Total reuse 0.7 KLD

Source of waste water for reuse with quantity in

KLD

Application area with quantity in KLD

Remarksregarding feasibility to reuse

i.e. w/w characteristics

(COD, BOD, TDS etc.)

Boiler & Cooling: 0.2 KLD

Boiler: 0.2 KLD COD: 250 mg/L BOD: 50 mg/L

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TDS: 450 mg/L

Washing: 0.2 KLD Process: 0.2 KLD COD: 1000 mg/L BOD: 200 mg/L TDS: 1500 mg/L

Scrubbing Media

Reuse in process (Di-

Octyle Sodium Sulpho

Succinate (Doss)

Sodium Bisulfite Solution (25%)

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

Stack Height (meter)

Type of Fuel

Quantity of Fuel

MT/Day

Type of

emissions

i.e. Air Polluta

nts

Air Pollution Control

Measures (APCM)

1 Boiler

(0.4 TPH) 11

Natural Gas

5000 SCM/Month

SPM < 150

mg/Nm3

SO2 < 100 ppm

NOX < 50 ppm

Adequate Stack Height 2

D.G Set (50 KVA)

11 Diesel 10 Liter/Hr

-

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

-

Sr. no.

Source of emission

Type of emission

Stack/Vent Height (meter)

Air Pollution Control Measures (APCM)

1 Reaction Vessel

(Sulfonation) SO2 9 2 Stage Alkali Scrubber

-

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

Following measures will be adopted to prevent and control fugitive emissionsC 1. Airborne dust at all transfers operations/ points will be controlled either by

spraying water or providing enclosures.

2. Care will be taken to store construction material properly to prevent fugitive

emissions, if any.

3. Regular maintenance of valves, pumps, flanges, joints and other equipment

will be done to prevent leakages and thus minimizing the fugitive emissions of

VOCs.

4. Entire process will be carried out in the closed reactors with proper

maintenance of pressure and temperature.

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5. Periodic monitoring of work area will be carried out to check the fugitive

emission.

6. Breather valves will be provided on solvent tanks.

7. Solvent tank vents will be connected to vent chillers.

8. To eliminate chances of leakages from glands of pumps, mechanical seal will

be provided at all solvent pumps.

9. Close feeding system will be provided for centrifuges. Centrifuge and filtrate

tank vents will be connected to vent chillers.

10. Minimum number of flanges, joints and valves in pipelines.

11. Enclosures to chemical storage area, collection of emission from loading of

raw materials in particular solvents through hoods and ducts by induced draft,

and control by scrubber / dust collector to be ensured.

12. Nitrogen blanketing will be provided, besides special care needs to be taken

for control in respect of odorous chemicals.

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

i

Sr. no.

Type/Name of

Hazardous waste

Source of generation

Category and

Schedule as per

HW Rules.

Quantity (MT/Annum)

Disposal Method

1 Discarded

Containers/ Barrels/ liners

Raw Material & Storage

33.1/ SCH-I

2.0

Collection, Storage, Transportation and disposal by selling to registered recycler.

2 Used

Oil/Spent Oil

Equipments &

machineries 5.1/ SCH-I 0.6 KL

Collection,

Storage, reused

or sale to

authorized

reprocessors

3 Sodium Bisulfite

Process (from

scrubber)

26.1/ SCH-I

180 MT

Collection,

Storage and

reuse in process

(Di-Octyle

Sodium Sulpho

Succinate (Doss)

- ii Membership details of TSDF, CHWIF etc.

(For HW management) Not Required

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

No such waste will be generated.

G Solvent management, VOC emissions etc.

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

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Solvents

Company will not use any solvent in the manufacturing of proposed project. Ii VOC emission sources and its mitigation measures

Company will not use any solvent in the manufacturing of proposed project.

Committee Deliberation & Discussion:

• During the meeting dated 23/01/2019, technical presentation made during the meeting by project proponent.

• 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. The baseline environmental study has been conducted for

the study area of 10 km radial distance from project site for the period March to May, 2017. Ambient Air Quality

monitoring was carried out for PM10, PM2.5, SO2, NO2, NH3, CO, O3, Pb, C6H6, BaP, As, Ni, HC & VOC at

eight 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. The resultant

concentrations are within the NAAQS. 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.

• During SEAC meeting on 23/01/2019, committee noted that the proposal is for new project. Industrial effluent

will be completely reused within premises. There will be no effluent discharge. Exhausted scrubbing media will

be reused in mfg. process of Di Octyle Sodium Sulpho Succinate.

• Natural gas and diesel will be used as fuel. Two stage alkali scrubber will be provided with reaction vessel as

APCM.

• PP addressed Hazardous Waste as per HWR – 2016. PP addressed EMP, CER with details of budgetary

provisions was found satisfactory.

• Compliance of the ToR was found satisfactory.

After detail deliberation the committee unanimously decided to recommend the proposal for grant of EC to

SEIAA with following specific conditions.

1. After expansion, unit shall discontinue manufacturing of Dispersing Agents and Dry Sodium Sulphate

2. There shall be no drainage connection within premises.

3. Necessary approvals from PESO and concerned Govt. Authorities shall be obtained.

4. Unit shall provide spare tank as a safety precaution for Oleum storage as per the prevailing

Rules/guidelines.

5. Emergency transfer facility for Oleum shall be provided.

6. Spare tank & Emergency facility for Oleum storage & handling shall be provided.

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2. SIA/GJ/IND2/23037/2018 M/s. Paras Enterprise Plot No: C1B/2 & C1B/3, Phase - I, Notified Industrial Area, GIDC, Tal.: Pardi, Dist.: Valsad.

Appraisal


Project status: Expansion

• Project Proponent (PP) has submitted online application vide no. SIA/GJ/IND2/23037/2018 dated 24/12/2018

for obtaining Environmental Clearance.


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

issued by SEIAA.

• This is an existing unit engaged in Synthetic organic chemicals and now proposes for expansion as tabulated

below:

Sr. No

Product CAS No. Capacity, TPM Remarks

Existing Proposed Total

1.0 Reactive Turquoise Blue-

H5G 12236-87-2 2.50 - 2.50 00

Will be discontinued and incorporated in

group 2.0

2.0 Synthetic Organic Dyes like

2.1 Reactive Black-5 17095-24-8

00 60.00 60.00 Proposed either of the product

2.2 Reactive Yellow-2 50662-99-2

2.3 Reactive Orange-4 12225-82-0

2.4 Reactive Red-11 12226-08-3

2.5 Acid Brown-432 119509-50-1

2.6 Direct Green-26 6388-26-7

2.7 Direct Turquoise Blue- 86 1330-38-7


21 12236-86-1

2.9 Direct Turquoise Blue 199 12222-04-7


H5G 12236-87-2

Total 2.50 57.50 60.00

3.0 Standardization of

Reactive Dyes (only Blending & mixing)

- 25.00 00 25.00 Existing




Sr.

No

.

Particulars Details

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A Total cost of Proposed Project

(Rs. in Crores):

Existing: 0.674 Crores

Proposed: 1.13 Crores

Total: 1.804 Crores

B Total Plot area

( sq. meter)

Existing: 1738 sq. meter

Proposed: 0 sq. meter

Total: 1738 sq. meter

Green belt area

( sq. meter)

Existing: 100 sq. meter

Proposed: 350 sq. meter

Total: 450 sq. meter

C Employment generation Existing: 20 Nos.

Proposed: 30 Nos.

Total:50 Nos.

D Water

i

Source of Water Supply

(GIDC Bore well, Surface water, Tanker supply

etc...)

GIDC - Vapi Water Supply

Status of permission from the concern authority.

Permission issued by GIDC Vapi vide letter No. GIDC/DEE(W/S)/NA/VAPI/1148 on 01/03/2018


# Particulars

Water Consumption, KLD Remar

k Existing

Proposed

Total

A. Domestic 1.00 1.00 2.00

B. Industrial

1. Processing and Washing 2.00 7.00 9.00

3. Boiler 0.50 9.50 10.00

4. Floor/Container Washing 1.00 0.00 1.00

5. Gardening 00 1.0 1.00

Total Industrial 3.50 17.50 21.00

C. Total (A+B) 4.50 18.50 23.00




iii


# Particulars

Wastewater Generation, KLD

Remark Existin

g Propose

d Total

A. Domestic 1.00 1.00 2.00 Septic

tank/Soak Pit

B. Industrial

1. Processing and Washing 1.40 6.60 8.00 Spray

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3. Boiler 0.10 0.40 0.50 dryer & ETP 4. Floor/Container Washing 1.00 0.00 1.00

Total Industrial 2.50 7.00 9.50

C. Total (A+B) 3.50

8.00 11.5

0

iv Treatment facility within premises with capacity [For existing and Proposed]

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

ETP : 9.5 KLD Effluent Treatment Capacity Spray dryer: 500 Kgs/hr

Septic tank/soak pit: 5 KLD


Domestic:

Domestic: Domestic waste water (2 KLD) will be disposed-off through Septic Tank/soak pit.

Industrial:

Industrial: After proposed expansion total 9.5 KLD of process and utility effluent will be generated, Out of which 7.0 KLD of process effluent will be treated in spray dryer and balance 2.5 KLD will be treated in existing primary followed by tertiary effluent treatment plant and discharge into CETP Vapi for further treatment. No additional effluent will be discharged to CETP due to proposed expansion

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

CHWIF etc.

Name of Common facility

Industrial: CETP, Vapi

1. Membership of Common facility (CF): Vapi Green Enviro limited Vide Ref. No. CETP_Memb. Certi/120 on dated 8th March, 2018

(For waste water treatment)


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vii Reuse/Recycle details (KLD)

[Source of reuse & application area] Not Applicable

Total reuse C 0 KLD

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.)

- - -

-

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.

Existing & Proposed

Sr. No

Source of Emission

With Capacity

e.g. Boiler (8 TPH)

Stack Heig

ht (mete

r)

Name of the fuel

Quantity of Fuel

MT/h & MT/Day

Type of emissions i.e.

Air Pollutan

ts

APCM Emission Standard

EXISTING

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1.

Steam Boiler: I

(200 kg/h) 11

Natural Gas

50 SCM/h

PM SOx NOx

Adequate

Stack Height

<PM: 150 mg/Nm3,

<SOx:100 ppm

<NOx: 50 ppm

2.

Hot Air Generator: I (2 Lacks K

Cal)

- Natural

Gas 250

SCM/h

Not Require

d

PROPOSED

1.

Steam Boiler: II

(800 kg/h) 11

Natural Gas

250 SCM/h

PM SOx NOx

Adequate

Stack Height <PM: 150

mg/Nm3, <SOx:100

ppm <NOx: 50

ppm

2.

Hot air Generator: II (10 Lacks K

Cal)

15 Natural

Gas 500

SCM/h Scrubb

er

3.

DG Set (500 KVA)

11 HSD 75 kg/h

Adequate

Stack Height


Existing & Proposed

Sr. No

Source of Emission

Stack Height (meter

)


Air Pollutan

ts

APCM Emission Standard

EXISTING

1.

Chloro sulphonation reaction and Oleum

Storage 11

SO2 HCl

Two Stage Acid followed by Alkali

Scrubber

<SO2:40 mg/Nm3 <HCl: 20 mg/Nm3

PRPOSED

1.

Spray Dryer 15 PM Alkali Scrubber <PM: 150 mg/Nm3,

iii Fugitive emission details with its mitigation measures.

We will provide two storage tanks for standby storage facility of oleum. Suitable

control measures will be taken to control the fugitive emission (primary and

secondary) during loading/ unloading, storage and handling of Oleum. Some fugitive

emissions control measures are described below:

� All the joints, flanges, pumps, glands, seals, valves are/ will be maintained in

good conditions through timely predictive and preventive maintenance;

� All tanks being used for storage of odorous chemicals/ products will be

connected to vacuum system. The vacuum will be monitored on daily basis

and actions will be taken accordingly.

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� All pumps handling hazardous chemicals shall be provided with mechanical

seals to prevent fugitive emission.

� Phase-wise development of green belt will be undertaken in which green belt

will be developed along with construction activity.

� Manual Handling of various chemicals will be avoided and will be designed by implementing latest automation technology.

F Hazardous waste

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

Movement) Rules 2016.

Existing & Proposed

i

-

S. No.

Type Source Quantity, TPA

Disposal Existing Proposed Total

1. Used Oil

(5.1)

D.G.Set 0.012 00 0.012

Sell to registered recycler

2. Discarded Containers

(33.1)

Raw/Product/ Utilities 2.00 3.00 5.00

Sell to registered recycler

3. Waste from ETP (35.3)

ETP 24.00 26.00 50.00

Dispose off into TSDF, Vapi

4.

Sludge from Wet

Scrubber (37.1)

Scrubber

0.024 00 0.024 Dispose off into TSDF, Vapi

5. Salt from

Spray Dryer (35.3)

Spray Dryer 00 109.20 109.20

Dispose off into TSDF, Vapi

ii Membership details of TSDF, CHWIF etc.

(For HW management)

VGEL certificate for CETP for acceptance of additional effluent vide letter No. VGEL/Mem. Corr-BV/2017-2018/0250 dated 19/06/2017 Common Solid waste disposal membership No. Mem. No. 69 B V -15 KL/D dated 08/03/2018.

iii Details of Non-Hazardous waste & its

disposal(MSW and others)

Nil



Solvents

No Solvents is being/will be used

ii VOC emission sources and its mitigation measures

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Not Applicable







the study area of 10 km radial distance from project site for the period1st March to 31st May 2018. Ambient Air

Quality monitoring was carried out for PM2.5, PM10, SO2, NOx , CO, Cl2 and HCl at eight 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 Aermode view (version 8.9.0). The resultant concentrations

are within the NAAQS. The ambient air quality around the proposed project site will remain within the National

Ambient Air Quality Standards (NAAQS).




• During SEAC meeting on 23/01/2019, committee noted that this proposal is for expansion. This unit has valid

CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP ensured that there are no court

cases pending and no public complaints against the project. After proposed expansion process and utility

effluent will be generated which will be treated in in house spray dryer and balance industrial effluent will be

treated in existing primary followed by tertiary effluent treatment plant and treated industrial effluent will be

discharged into CETP Vapi for further treatment. Upon asking, PP ensured that there will be no increase in

organic load and hydraulic load of effluent being discharged to CETP, Vapi after proposed expansion.

• Natural gas and HSD will be used as fuel. Acid scrubber and alkali scrubber will be provided as APCM for

process gas emission control. Alkali scrubber will be provided with spray dryer as APCM.

• PP addressed Hazardous Waste as per HWR – 2016 including bleed liquor. PP addressed EMP, CER with

details of budgetary provisions was found satisfactory.



SEIAA.

1. Unit shall fed industrial effluent to spray dryer only after giving adequate treatment to ensure no adverse impacts on Environment and Human Health.

2. There shall be no increase in hydraulic load and organic load of effluent being discharged to CETP, Vapi after expansion. 3. Necessary approvals from PESO and concerned Govt. Authorities shall be obtained. 4. Unit shall provide spare tank as a safety precaution for Oleum storage as per the prevailing

Rules/guidelines. 5. Emergency transfer facility for Oleum shall be provided. 6. Spare tank & Emergency facility for Oleum storage & handling shall be provided.

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3. SIA/GJ/IND2/20480/2018 M/s. Meghmani Speciality Chemicals LLP Plot No. CH-22, GIDC Estate, Dahej, Tal: Vagra, Dist.: Bharuch.

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/20480/2018 dated 16/01/2019 for obtaining

Environmental Clearance.

• The SEAC had recommended TOR to SEIAA and SEIAA issued TOR to PP vide their letter dated

07/07/2018.

• Project proponent has submitted EIA Report prepared by San Envirotech Pvt. Ltd., Ahmedabad based on

the TOR issued by SEIAA

• This is a new unit proposes for manufacturing of Synthetic Organic Chemicals as tabulated below:

Sr.

No.

Name of the Products CAS/CI no. Quantity

MT/Month

End-use of

product

A Reactive Dyes – 1000 MT/month

1 Reactive Black

a Reactive Black B - 400

Dyeing &

Printing

b Reactive Black Mix –

WNN/R/G/XLW/DN/GHF/CL5/GR/GF

-

2 Reactive Yellow

a Reactive Yellow 3 RX - 250

b Reactive Yellow 4GL -

c Reactive Yellow XL -

3 Reactive Orange

a Reactive Orange H2R 12225-85-3 50

b Reactive Orange 2 RX -

c Reactive Orange 3R 12225-83-1

d Reactive Orange WNN -

e Reactive Orange CD -

4 Reactive Red

a Reactive Red CD - 200

b Reactive Red 5 BX -

c Reactive Red 3 GX -

d Reactive Red RGB (Blending) -

e Reactive Red Crimson HEXL -

f Reactive Red Rubin XL -

g Reactive Red BS 88232-20-6

h Reactive Red RB 145017-98-7

i Reactive Red 2 GX -

5 Reactive Blue

a Reactive Navy Blue RGB 100 - 100

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b Reactive Navy Blue GG -

c Reactive Blue BB -

d Reactive Blue 3 GX -

e Reactive Blue BFN (Blending) -

f Reactive Blue BRX -

Optical Brightening Agent – 750 MT/month

Detergent

whitener,

paper

whitening and

fibre

brightening

1 Optical Brightening Agent -2 B OBA 24 15

2 Optical Brightening Agent - BSU OBA 264 100

3 Optical Brightening Agent - DMX OBA 71 350

4 Optical Brightening Agent - BBU OBA 220 50

5 Optical Brightening Agent - BA OBA 113 50

6 Optical Brightening Agent - DT OBA 351 185

TOTAL (A) 1750

B Dye Intermediates

Dyeing and

printing

1 PBVS 2494-89-5 200

2 PCVS 21635-69-8 20

3 DMAVS 26672-24-2 20

4 OAVS 26672-22-0 25

5 SOAVS - 25

6 SVS 3039-83-6 25

7 MUA 59690-88-9 30

8 MPDSA 88-63-1 25

9 Bromamine Acid 116-81-4 20

10 Sulpho Tobias Acid 171570-11-9 20

11 Gamma Acid 90-51-7 25

12 NMJ Acid 22346-43-6 10

13 K - Acid 118-03-6 40

14 BCMB - 150

15 OSB 200

16 H-Acid 90-20-0 165

17 DASDA 81-11-8 200

TOTAL (B) 1200

TOTAL (A+B) 2950




Sr. no.

Particulars Details


(Rs. in Crores):

200 Crores

B Total Plot area( sq. meter) 52400 Sq. m.

Green belt area

( sq. meter)

17290 Sq. m.

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C Employment generation 300 Nos.

D Water

i


(GIDC Bore well, Surface water, Tanker

supply etc.)

GIDC water supply

Status of permission from the concern

authority.

Permission is obtained from GIDC.


Category Quantity, KLD Remarks

(D) Domestic 22 Fresh

(E) Gardening 80 Fresh

(F) Industrial

Process 436 Fresh

Washing 200 Fresh

Boiler 250 248 KLD water reused +

202 KLD fresh water Cooling 200

Others

Lab 5 Fresh

Scrubber 24 Fresh

Water treatment 20 Fresh

Industrial Total 1135

Total (A + B + C) 1237



9) Total fresh water requirement:989.0 KLD

iii Waste water generation (KLD)

Category Waste water, KLD Remarks

(C) Domestic 20

(D) Industrial

Process 464

Washing 200

Boiler 25

Cooling 45

Others

Lab 5

Scrubber 1

Water treatment 20

Total Industrial waste water 760

Total [A + B] 780 520 KLD to GIDC-

drainage,

260 KLD to Zero Liquid

Discharge

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iv Treatment facility within premises with capacity

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

ETP-1 : 600 KLD, ETP-2: 300 KLD, MEE-1: 2.5 m3/hr (G salt recovery), MEE-2: 15 m3/hr, Spray dryer: 9 m3/hr


Domestic: Treated in ETP along with other industrial effluent (of Dyes & OB plant),

and discharged to GIDC drainage for final disposal.

Industrial: Dyes & OB plant:

Wastewater from Dyes & OB plant (349 KLD) along with domestic

wastewater (20 KLD) will be treated in “ETP-1”. After achieving

prescribed norms, it will be discharged to GIDC drainage for final

disposal.

Dyes intermediate plant:

Wastewater from Dyes intermediate plant will be divided into two streams

- high COD/high TDS and dilute stream.

• High COD/high TDS stream will be 396 KLD. Out of which, 48 KLD

of EO condensate will be subjected to “MEE-1” for Glauber salt

recovery. Condensate of MEE-1 (40 KLD) will be taken into “ETP-2”.

Recovered Glauber salt will be sold to actual users.

• Remaining 260 KLD (after recovery of H2SO4 and drying loss) and

Condensate of MEE-1 (40 KLD) will be treated in “ETP-2” followed

by “MEE-2” (Total: 260+40 = 300 KLD). Condensate of MEE-2 (248

KLD) will be reused and rejected 52 KLD will be spray dried in in-

house spray dryer to achieve zero liquid discharge (ZLD).

• Dilute stream of utility, washing and scrubber (151 KLD) will be taken

to “ETP-1” of Dyes & OB plant for final treatment and disposal.

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

Name of CF

Discharged to GIDC drainage

Membership of Common facility (CF)

GIDC drainage of 550 KLD is available.


(a) Reactive Dyes and Optical Brightening Agents Plant

Page 18 of 92


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(b) Dye Intermediate Plant

Page 19 of 92


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Page 20 of 92

i Total reuse: 204 KLD

Source of waste water for reuse with quantity in KLD


Remarks regarding feasibility to reuse i.e.

w/w characteristics (COD, BOD, TDS etc.)

MEE-2 Condensate: 248 KLD

(Total Recycle waste water :

248 KLD)

Utilities : 248 KLD Source of wastewater is condensate water from

MEE-2, which can be used in the utilities without affecting the industrial

operations.

Estimated quality of MEE Condensate

Parameters Unit MEE-2 (ETP)

pH pH Unit 7.2-7.8

Color Co-Pt Unit <15

SS mg/L <10

TDS mg/L 150-250

COD mg/L 150-200

BOD mg/L <250

Oil & Grease mg/L <10

Ammonical Nitrogen mg/L <10

Volume in KLD 248

E Air



KVA etc.

Sr. no.

Source of emission

With Capacity


Type of Fuel

Quantity of Fuel MT/Day


Air Pollutan

ts


Measures (APCM)

1 Steam Boiler (10 TPH x 3 Nos.)

50 Coal

150 MT/day

SPM, SO2 , NOx

Electrostatic Precipitator

(ESP) 2 Thermopack

(25 Lac Kcal/hr x 2 nos.)

30

Coal

30 MT/day

Cyclone separator

followed by Bag filter

3 Hot Air generator (40 lac K.cal x 2 Nos.)

35 Coal

52 MT/day

Cyclone separator

followed by Bag filter

4 D.G. set (stand By) (1250 KVA)

11 HSD

0.3 KL/hr. --


Page 21 of 92


Page 21 of 92

Sr. no.

Specific Source of emission

(Name of the Product & Process)

Type of emission

Stack/Vent

Height (meter

)


1. Isolator /Sulphontor/ Nitrator (H-Acid)

SO2 15 Alkali Ventury + Alkali packed column /Water Ventury, water packed column, Alkali Ventury

Alkali, water packed column

2. Neutralizer (H Acid)

NOx

15 Glass Line Packed Column Acid Scrubber

3. Sulphonation Vessels (V.S) and its derivatives plants

HCl, SO2 15 Water Ventury, Water packed column, Alkali

Ventury, Water Packed Column

4. Amidation Reactors (Gama Acid and K Acid)

NH3 15 Acid Scrubber

5. Reaction Vessel (Dyes Plant)

HCl, SO2 15 Water Scrubber follows by Alkali Scrubber

6. Bromination Reactor of Bromamin Acid

HBr, Br2 15 Two stage Water Scrubber followed by Two stage

Alkali Scrubber

7. Reaction Vessels (Other Intermediate Plant)

HCl, SO2

15 Water Scrubber followed by Alkali Scrubber

8. Spray dryers (1500 lits/hr x 6 Nos.) for dyes plant

SPM 25 m each

Cyclone Separator followed by dual stage water

packed/demister 9. Spray dryers

(1500 lits/hr) for intermediates plant

SPM 25 Cyclone Separator followed by dual stage water

packed/demister

10. Spray dryers (9000 LPH 1 Nos.) for ZLD

SPM 25 Cyclone Separator followed by dual stage water

packed/demister


As below:

Fugitive emission: There will be chances of VOCs, Acid Mist generation from process

area & raw material storage area. There will be also chances of generation of PM from

packing/finishing area.

Mitigation measures:

• Close handling system provided for transfer of chemicals.

• Pneumatically transfer of liquid raw material in reactor.

• Raw material will be stored in the covered structure.

• Regular maintenance of valves, pipes etc.

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

• Greenbelt will be developed around the plant to arrest the fugitive emission.

Page 22 of 92


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F Hazardous wastes

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


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/Annu

m)

Management of HW

1 ETP sludge

ETP 35.3 400 MT/month

Collection Storage, Transportation and Disposal to TSDF.

2 Salt from Spray dryer

Spray dryer 35.3 150 MT/month


3 Gypsum from ETP

ETP 26.1 1710 MT/month

Collection Storage, Transportation and sold to Cement units or send to TSDF.

4 Gypsum from Process

Process of H-Acid

26.1 1270 MT/month


5 Iron Sludge Process of DASDA, MPDSA, H-Acid

26.1 690 MT/month


6 Process waste

Process of DMAVS,

OSB

26.1 10.2 MT/month


7 Used/Spent oil

Machinery, D.G. set

5.1 2 KL/year

Collection Storage, Transportation and disposal by sold out to registered recyclers or used for lubrication.

8 Discarded containers/ barrels/ liners

RM storage 33.1 4,000 Nos./month

Collection, Storage, Transportation and Disposal by sold out to decontamination facility or send back to suppliers.

9 Nitrosyl (NaNO2) (20-22%)

Process of H-Acid

-- 150 MT/month

Collection, storage, transportation and sold to actual end users under Haz Waste Rules.

10 Hydrochloric Acid (30%)

Process of PBVS, PCVS,

26.3 180 MT/month

Collection, storage and captive use in dyes plant

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DMAVS, OAVS, MUA,

Bromamine Acid, BCMB

11 Acetic Acid (93-95%)

Process of PBVS, PCVS,

DMAVS, OAVS

26.3 41 MT/month

Collection, storage and captive use in dyes plant and excess sold to actual end users under Haz Waste Rules

12 Glauber Salt MEE (from EO

condensate of PBVS, PCVS,

DMAVS, OAVS)

26.1 240 MT/month

Collection, storage, transportation and sold to actual end users under Haz Waste Rules

13 SBS (23%) Scrubber (of PBVS,

STA, Gamma

Acid, K Acid, H-Acid)

26.3 421 MT/month


14 Spent Acid (H2SO4) (30-45%)

Process (of PBVS,

PCVS, DMAVS, OAVS,

SOAVS, SVS)

26.3 1980 MT/month

Collection, storage, transportation and utilize in H-Acid plant.

15 Distillation Residue

Distillation process

20.3 17 MT/month

Collection, Storage, Transportation and disposed to CHWI facility

16 Ammonia Sulphate

Scrubber (of Gamma

Acid, K Acid)

-- 172 MT/month



(For HW management)

Membership of TSDF& CHWIF will be

taken after getting EC.



--


i Types of solvents, Details of Solvent recovery, % recovery, Reuse of recovered

Solvents

• Methanol, Toluene and PNT will be used as solvent. Solvent recovery will be

about 95-97%. Recovered solvent will be collected and reused again in next

Page 24 of 92


Page 24 of 92

batch.


• Closed handling & charging system will be provided.

• Mechanical seals to pumps will be provided to prevent leakages.

• Regular monitoring of VOCs will be done.


• During the meeting dated 23/01/2019, technical presentation made during the meeting by project

proponent.

• 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.


noise, water, biological and socioeconomic aspect. The baseline environmental study has been conducted

for the study area of 10 km radial distance from project site for the period March, 2018 to May, 2018.

Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, VOC, CO, HC, HBr, HCl, NH3 at

Eight 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 ISCST3. The

resultant concentrations are within the NAAQS. The ambient air quality around the proposed project site

will remain within the National Ambient Air Quality Standards (NAAQS).


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

Plan has been covered in the RA report.

• During SEAC meeting on 22/01/2019, committee noted that this proposal is for new project. Industrial

effluent from Dyes & OB and Dyes intermediate plant will be treated separately. Industrial effluent from

Dyes & OB plant along with domestic effluent will be treated in ETP-1 (P+S+T). After achieving prescribed

norms, it will be discharged to GIDC drainage for final disposal.

• Industrial effluent from Dyes intermediate plant will be divided into two streams - high COD/high TDS and

dilute stream. High COD/high TDS stream will be 396 KLD. Out of which, 48 KLD of EO condensate will be

subjected to MEE-1 for Glauber salt recovery. Condensate of MEE-1 will be taken into ETP-2 (P+S+T).

Recovered Glauber salt will be sold to actual users. Remaining and Condensate of MEE-1 will be treated in

“ETP-2” followed by “MEE-2”. Condensate of MEE-2 will be reused and rejected will be spray dried in in-

house spray dryer. Dilute stream of utility, washing and scrubber will be taken to ETP-1 of Dyes & OB plant

for final treatment and disposal.

• Coal and HSD will be used as fuel. Cyclone separator followed by bag filer will be provided as APCM with

TFH and HAG. Common ESP will be provided with 3 nos. 10 TPH steam boilers as APCM. Cyclone

Separator followed by dual stage water packed/demister will be provided with spray dryers.

• PP addressed Hazardous Waste as per HWR – 2016 including bleed liquors. PP addressed EMP, CER

with details of budgetary provisions was found satisfactory.

Page 25 of 92


Page 25 of 92



SEIAA.

1. Unit shall fed industrial effluent to MEE and spray dryer only after giving adequate treatment to ensure no adverse impacts on Environment and Human Health.

2. Necessary approvals from PESO and concerned Govt. Authorities shall be obtained. 3. Unit shall provide spare tank as a safety precaution for Oleum storage as per the prevailing

Rules/guidelines. 4. Emergency transfer facility for Oleum shall be provided. 5. Spare tank & Emergency facility for Oleum storage & handling shall be provided.

4. IA/GJ/IND2/66091/2017 M/s. Suleshvari Pharma

Plot No. 6012/1, GIDC Estate, Ankleshwar, Dist.: Bharuch – 393002.

Appraisal



• PP has submitted online application vide no. IA/GJ/IND2/66091/2017 dated 15/01/2019 for obtaining


• MoEF&CC issued TOR to PP vide their letter No.IA-J-11011/373/2017-IA-II (I) vide dated 24th August 2017.

• Project proponent has submitted EIA Report prepared by M/s. Aqua Air Environmental Engineering Pvt. Ltd.,

Surat based on the TOR issued by MoEF&CC.

• This is an existing unit and now proposes for expansion as tabulated below:

Sr. No.

Products Production Capacity (MT/Month)

CAS No. End use

Existing Additional Total

(A) Bulk drugs/Bulk Drugs Intermediates

1 Iso Amyl Acetate 1 -- 1 123-92-2 Pharma Intermediate 2 Iso Amyl Propionate 1 -- 1 105-68-0 Pharma Intermediate

3 Iso Amyl Butyrate 1 -- 1 106-27-4 Pharma Intermediate

4 Phenyl Ethyl Acetate 1 -- 1 103-45-7 Pharma Intermediate

5 Phenyl Ethyl Propionate 1 -- 1 122-70-3 Pharma Intermediate

6 Methyl -3- Amino Crotonate 1 4 5 14205-39-1 Pharma Intermediate 7 Phthalimido Amlodipine 1 4 5 88150-62-3 Pharma Intermediate

Or

& 8 Diaminomethyleneamino (1-

amino-1-iminomethylene) thio methyl thiozole dihydrochloride [ITU]-50

9 41 50

123-92-2 Pharma Intermediate

Or

&

9 N-Sulfomyl-3-chloropropionamide hydrochloride[IF]-50

9 41 50 106649-95-0 Pharma Intermediate

Or

&

10 Famotidine 4 6 10 76824-35-6 Anti Ulcer

Or

&

Page 26 of 92


Page 26 of 92

11 Poly Allaylamine Hydrochloride

9 191 200 71550-12-4 Pharma Intermediate

Or

&

12 Sevelamer Hydrochloride 9

20

20

152751-57-0 Hyper phosphataemia Or

13 Sevelamer Carbonate 9 845273-93-0 Hyper phosphataemia

Or

14 Fomepizole 0.6 7554-65-6 Hemodialysis

Or

15 Colsevelam hydrochloride 7.5 182815-44-7 Hyper phosphataemia

Or 16 Glimepiride 2.9 93479-97-1 Anti Diabetic

Or

17 Furosemide 9 54-31-9 Anti Diuretic

Or

18 Betahistine Dihydrochloride 3.2 106649-95-0 Pharma

Or

19 Adapalene 1.5 76824-35-6 Skin allergic

Or

20 Telmisartan 6.5 152751-57-0 Hypertension

Or

21 Tapentadol Hydrochloride 8 845273-93-0 Analgesic

Or 22 Colistimethate Sodium 3.5 71550-12-4 Pharma

Proposed

23 Rusvastatin Calcium - 7554-65-6 High cholesterol

24 1-3 dichloro Acetone - 182815-44-7 Pharma Intermediate

25 Gunylthiourea - 93479-97-1 Pharma Intermediate

26 Rabeprazole Sodium - 5579-84-0 Pharma

27 Carvediol - 106685-40-9 Hypertension 28 Celecoxib - 144701-48-4 Arthritis

29 Clopidogrel Bisulfate - 175591-09-0 Heart attacks

30 Atoravastatin Calcium - 8068-28-8 High cholesterol

31 Etoricoxib - 147098-20-2 Spondylitis

32 Valsartan - 534-07-6 Antihypertensive

33 Tranexamic Acid - 2114-02-5 Antifibrinolytic

34 Folic Acid - 117976-90-6 Folate deficiency 35 Zolpidic Acid - 72956-09-3 Bone diseases

36 Pregabaline - 169590-42-5 Anti diabetes

Total (A) 9 336 345

• The project falls under the Category B of project activity 5(f) as per the schedule of EIA Notification 2006.



Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: 0.94

Proposed: 5.00

Total: 5.94

Page 27 of 92


Page 27 of 92

B Total Plot area

( sq. meter)

Existing: 1567 Sq. m.

Proposed: 778 Sq. m.

Total: 2345Sq. m.

Green belt area

( sq. meter)

Existing: 390 Sq. m.

Proposed: 400 Sq. m.

Total: 790 Sq. m.

C Employment generation Existing: 45

Proposed: 20

Total: 65

D Water

i


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

GIDC


Unit has obtained permission from GIDC for

water supply vide letter no

NO/NA/DEE(W/S)/860 dated 25/05/2018.


Existing

KLD

Proposed

(Additional)

KLD

Total after Expansion

KLD

(G) Domestic 1 2 3

(H) Gardening -- 1 1

(I) Industrial

Process 1 26 27

Washing 0.4 1.6 2

Boiler 0.6 9.4 10

Cooling 0.5 9.5 10

Scrubber Nil 1 1

Industrial Total 2.5 47.5 50

Grand Total (A+B+C) 3.5 50.5 54

10) Total water requirement for the project: 54 KLD

11) Quantity to be recycled: 0 KLD

12) Total fresh water requirement: 54 KLD


Page 28 of 92


Page 28 of 92

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(E) Domestic 0.9 1.5 2.4

(F) Industrial

Process 0.5 21.5 22

Washing 0.4 1.6 2

Boiler 0.05 0.45 0.5

Cooling 0.05 0.45 0.5

Others Nil 1.16 1.16* Sold to end user under

Rule-9 permission

Total Industrial

waste water

1 24 25



In-house ETP consist of Primary Treatment: 20.55 KL/Day & 4.45 KL/Day


Domestic: 2.4 KL/Day domestic wastewater will be disposed through Septic Tank/Soak Pit.

Industrial:

1) Industrial waste water (4.45 KL/day out of 25 KL/Day) will be treated in ETP and treated waste water will be sent to CETP of M/s. Enviro Technology Ltd. (ETL), Ankleshwar for further treatment and disposal. 2) Remaining Industrial wastewater (20.55 KL/Day out of 25 KL/Day) will be treated in ETP and treated waste water will be sent to Common MEE of M/s. Ankleshwar Cleaner Process Technology Centre Pvt. Ltd. (ACPTCL), Ankleshwar for further treatment and disposal.

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


Common MEE membership of M/s. ACPTCL, Ankleshwar & CETP of M/s. ETL, Ankleshwar


Unit has obtained membership of Common MEE of M/s. ACPTCL, Ankleshwar vide letter no.

ACPTCPL/1300000137/2018-19/72 dated 15/10/2018.


Page 29 of 92


Page 29 of 92


[Source of reuse & application area]

Total reuse 0 KLD

Source of waste

water for reuse

with quantity in

KLD


quantity in KLD

Remarks

regarding

feasibility to

reuse i.e. w/w

characteristics

(COD, BOD,

TDS etc.)

No reuse or recycle details

-

E Air


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

Existing & Proposed

-

Page 30 of 92


Page 30 of 92

Sr. no.

Source of emission

With Capacity


Type of Fuel


Type of emissions i.e. Air Pollutants


Measures (APCM)

1. Boiler (Capacity: 0.6 TPH)

15 Natural

Gas 300

Sm3/Day

SPM SO2 NOx

Adequate Stack Height

2. Boiler (Proposed) (Capacity: 2.0 TPH)

30 Natural

Gas 1000

Sm3/Day

SPM SO2 NOx


3.

Thermic fluid heater (Proposed) (Capacity: 4 Lac KCal/Hr.)

30 Natural

Gas 1000

Sm3/Day

SPM SO2 NOx


4. D. G. Set (150 KVA)

11 HSD 20 Lit/ Hr.

SPM SO2 NOx


-


Existing & Proposed

-

Sr.

no.

Specific Source of

emission

(Name of the Product &

Process)

Type of

emission

Stack/Vent

Height

(meter)


Measures

(APCM)

1 Process Vent (Chlorination or Amination) (Product Name: Glimepride & IF) (Existing)

Cl2 HCl NH3

11 Two Stage Water & Caustic scrubber

2 Process Vent (Chlorination) (Product Name: Rosuvastatin Calcium) (Proposed)

Cl2 HCl

11 Two Stage Water + Alkali scrubber

3 Process Vent (Sulphonation) (Product Name: Cetrizine Dihydrochloride) (Proposed)

SO2 11 Two Stage Alkali scrubber

4 Process Vent (Amination) (Product Name: Glimepride) (Proposed)

NH3 11 Two Stage Acid scrubber

-


Following measures will be adopted to prevent and control fugitive emissionsC

13. Airborne dust at all transfers operations/ points will be controlled either by spraying water or

Page 31 of 92


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providing enclosures.

14. Raw materials loading and unloading will be done in covered area

15. Care will be taken to store construction material properly to prevent fugitive emissions, if any.

16. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent

leakages and thus minimizing the fugitive emissions of VOCs.

17. Entire process will be carried out in the closed reactors with proper maintenance of pressure and

temperature.

18. Periodic monitoring of work area will be carried out to check the fugitive emission.


20. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all

solvent pumps.

21. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be

connected to vent chillers.


23. Enclosures to chemical storage area, collection of emission from loading of raw materials in

particular solvents through hoods and ducts by induced draft, and control by scrubber / dust

collector to be ensured.

24. Adequate ventilation will be provided.

25. Periodic monitoring of work area will be carried out to check the fugitive emission as per the

norms of Gujarat Factory Rules.

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.)

Category

and

Schedule

as per

HW

Rules.

Quantity

(MT/Annum)

Management of

HW


1 Used Oil Equipment & Machinery

Sch-I/ 5.1

0.25 23.75 24 Collection, Storage, Transportation and reuse or sell to Registered recycler.

2 Organic Waste

Process (Rosuvastatin

Calcium)

Sch-I/ 28.1

0.72 179.28 180 Collection, Storage, Transportation

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and given to cement industries for co-processing or disposal at CHWIF of BEIL, Ankleshwar.

3 Discarded Bags & Liners

Raw Material & Storage

Sch-I/ 33.1

6.48 59.52 66 Collection, Storage, Transportation and sell to GPCB Registered Re-processors after Decontamination.

Discarded Containers

4 Inorganic Process Waste

Process (Rabeprazole

Sodium)

Sch-I/ 28.1

-- 60 60 Collection, Storage, Transportation and disposal at Common TSDF of BEIL, Ankleshwar

5 Spent Carbon

Process (Clopidogrel Bisulphate)

Sch-I/ 28.2

-- 24 24 Collection, Storage, Transportation and given to cement industries for co-processing or disposal at CHWIF of BEIL, Ankleshwar.

6 Hydrochloric Acid (30%)

Scrubber (10 MT/M) + Process

(IF)(20 MT/ M)

Sch-II/ B15

-- 360 360 Collection, Storage, Transportation and sell to end user having permission under Rule-9.

7 Ammonium Chloride (30%)

Scrubber Sch-II/ B15

-- 420

420

8 Di Potassium Phosphate

Process (Guanyl

Thiourea)

Sch-I/ 28.1

-- 420

420

9 Sodium Sulphite (25%)

Scrubber Sch-II/ B36

-- 420 420

10 Spent Solvent

Process Sch-I/ 28.6

-- 600 600 Collection, Storage, in-house distillation or sent to job work for distillation to end user registered under Rule-9 permission and Reuse within

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premises.

11 Sodium Chloride (30%)

Scrubber (10MT/M) +

Process (Colsevelam

Hydrochloride) (20 MT/M)

Sch-I/ 28.1

-- 360 360 Collection,

Storage, and

sent to ETP.

12 Spent Catalyst

Process (Atorvastatin

Calcium)

Sch-I/ 28.2


Storage,

Transportation

and sent to

registered

regenerator.


Distillation Sch-I/ 20.3


Storage,

Transportation

and sent for co-

processing in

cement

industries or sent

to common

incineration of

M/s. BEIL.

14 ETP Sludge ETP Sch-I/ 35.3

-- 120 120 Collection, Storage, Transportation and disposal at Common TSDF of BEIL, Ankleshwar

-


(For HW management)

Company has membership of M/s. BEIL, Ankleshwar

vide letter No. BEIL/ANK/2017 dated 18/03/2017.



No such waste will be generated.


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

SOLVENT Boiling Point (°C)

Vapor Pressure (kPA@ 20oC)

INPUT

(MT)

RECOVER (MT)

LOSSES (MT)

%RECOVER (MT)

%LOSSES (MT)

Acetone 56.2 24 600 580 20 96.67 3.33

Dichloromethane 39.75 46.5 580 570 10 98.27 1.73

Dimethylformamide 153 0.3 120 117.8 2.2 98.17 1.83

Ethanol 78.5 5.7 85 83 2 97.64 2.36

Page 34 of 92


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Hexane 68 17.3 72 70.2 1.8 97.5 2.5

Iso Propyl Alcohol 82.5 4.4 490 480.2 9.8 98.0 2

Methanol 64.5 12.3 550 536.2 13.8 97.5 2.5

Toluene 110.6 3.8 @ 25oC

180 175 5 97.22 2.78


During operation stage, leakage through valves/pumps, leakage and emission from open drum containing chemicals, open feeding, storage tanks, etc. will be major sources of fugitive emissions and VOCs. Excess use of solvent/s may also results fugitive emission from the process vessels.

• Solid raw material charging will be done through closed system.

• Entire process will be carried out in the closed reactors with proper maintenance of pressure and

temperature.

• Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be

connected to vent chillers.

• Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area, will be

collected through hoods and ducts by induced draft and controlled by scrubber/dust collector.

• Emphasis will be given to solvent management/solvent loss prevention.

• Control by having proper scrubbing system.

• Condenser to trap VOC.

• Enclosures to chemical storage area, collection of emission from loading of raw materials in particular

solvents through hoods and ducts by induced draft, and control by scrubber/dust collector to be

ensured.

• Proper maintenance schedule will be adhered to avoid emissions through flange joints, pump seals

etc.

• Minimum number of flanges, joints and valves in pipelines.

• Proper gland packing will be maintained for pumps and valves and to the extent possible pumps with

mechanical seal.

• All the raw materials will be pneumatically transfer to the reactor.

• All rotating equipments like pumps will be installed with mechanical seals to arrest any sort of

emissions.

• 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 place.

• Periodic monitoring of work area will be carried out to check the fugitive emission.

• Solvent tank vents will be connected to vent chillers.

• Adequate ventilation will be provided.

• Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing

Page 35 of 92


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enclosures.

• Breather valves will be provided on solvent tanks.







the study area of 10 km radial distance from project site for the period March to May 2017. Ambient Air Quality

monitoring was carried out for PM10, PM2.5, SO2, NO2, NH3, CO, HCl, HBr, C6H6, HC & 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 ISCST3. The resultant






• During SEAC meeting on 23/01/2019, committee noted that the proposal is for expansion project. This unit has

valid CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP ensured that there are no

court cases pending and no public complaints against the project. Industrial waste water will be treated in ETP

and treated wastewater will be partly sent to CETP of M/s. Enviro Technology Ltd. (ETL), Ankleshwar for

further treatment and partly treated wastewater will be sent to Common MEE of M/s. Ankleshwar Cleaner

Process Technology Centre Pvt. Ltd. (ACPTCL), Ankleshwar for further treatment.

• Natural gas and diesel will be used as fuel. Two stage acid scrubber will be provided with proposed Amination

reactor as APCM. Two Stage Water + Alkali scrubber will be provided with proposed chlorination reactor.

• PP addressed Hazardous Waste as per HWR – 2016 including bleed liquors. PP addressed EMP, CER with



After detail deliberation the committee unanimously decided to recommend the proposal for grant of EC –

Amendment to SEIAA.

1. Unit shall send wastewater to Common MEE only after achieving inlet norms to common MEE prescribed

by GPCB in order to achieve no adverse impacts on Environment and Human Health.

2. Unit shall comply all the conditions & recommendations mentioned in the guidelines for the management of

the spent solvents published by GPCB in letter and spirit.

3. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB

guidelines.

Page 36 of 92


Page 36 of 92

4. Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.

5. SIA/GJ/IND2/21107/2017 M/s. Advatech Formulations Pvt. Ltd.

Plot no. 830/5/3, GIDC Estate, Jhagadia,

Dist.: Bharuch.

Appraisal


Project status: New

• PP has submitted online application vide no. SIA/GJ/IND2/21107/2017 dated 25/12/2018 for obtaining



• Project proponent has submitted EIA Report prepared by Aqua-Air Environnemental Engineers Pvt. Ltd., Surat

based on the TOR issued by SEIAA.

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

Sr. No.

Name of Products CAS NO. Proposed Quantity

End Use

MT/Month

Group- 1

1 Atenolol 29122-68-7 20 blood pressure, heart attacks, chest pain (angina) heart

attack.

2 Metoprolol tartrate 56392-17-7 blood pressure, heart attacks, and kidney problems. Beta

blockers 3 Ofloxacin 82419-36-1 bacterial infections. quinolone

antibiotics. 4 Modafinil 68693-11-8 Obstructive

5 Cetirizine Di HCl 83881-52-1 allergy symptoms

6 Triclabendazole 68786-66-3 Fascioliasis ,liver fluke

7 Meprobamate 57-53-4 Anxiety disorders

8 Diclofenac sodium 15307-79-6 Arthritis& anti-inflammatory 9 Amlodipin besylate 111470-99-6 blood pressure

(hypertension).

10 Metoprolol succinate 98418-47-4 Blood pressure

11 Famotidine 76824-35-6 histamine-2 blockers. Zollinger-Ellison syndrome.

12 Pantaprazol Sodium 138786-67-1 Zollinger-Ellison syndrome.

13 Trimebutine maleate 34140-59-5 Spasmolytics

14 Cis-bromo benzoate 61397-56-6 Antifungal

15 Itraconazole 84625-61-6 fungal infections

16 Rabeprazole sodium 117976-90-6 Gastroesophageal

17 Levetiracetam 102767-28-2 Epilepsy & seizures

Group-2

18 Pregabalin 148553-50-8 10 Fibromy

19 Telmisartan 144701-48-4 blood pressure (hypertension)

Page 37 of 92


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20 Albendazole 54965-21-8 Anthelmintic

21 Ketoconazole 65277-42-1 Antifungal medication 22 Oxcarbazepine 28721-07-5 Anticonvulsant, or

antiepileptic 23 Fluconazole 86386-73-4 fungal infections

24 Quetiapine fumarate 111974-72-2 anti-psychotic

25 Valsartan 137862-53-4 blood pressure

Group-3

26 Venlafaxine Hydrochloride 99300-78-4 10 Antidepressant

27 Efavirenz 154598-52-4 human immunodeficiency virus (HIV) infection.

28 Phenylephrine HCl 61-76-7 breathing illnesses

29 Atorvastatin calcium 134523-03-8 Cholesterol and fats (such as LDL, triglycerides)

30 Mycophenolate mofetil 128794-94-5 immunosuppressant’s

31 Zonisamide 68291-97-4 anti-convulsant

Group-4

32 Olanzapine 132539-06-1 10 Antipsychotic

33 Emtricitabine 143491-57-0 human immunodeficiency virus (HIV)

34 Pranlukast 103177-37-3 chronic bronchial asthma

35 Rosuvastatine calcium 147098-20-2 cholesterol and fats (such as LDL, triglycerides)

36 Fluxetine hydrochloride 56296-78-7 major depressive disorder, bulimia nervosa

37 Ursodiol 128-13-2 primary biliary cirrhosis 38 Candesartan 129481-59-7 Blood pressure

(hypertension) 39 Montelukast sodium 151767-02-1 leukotriene receptor

antagonists Group-5

40 Iloperidone 133454-47-4 0.25 Schizophrenia 41 Tamsulosin Hydrochloride 106463-17-6 Alpha-adrenergic

42 Nebivolol Hydrochloride 152520-56-4 Blood pressure

43 Memantine hcl 41100-52-1 Alzheimer's disease 44 Silodosin 160970-54-7 Alpha-adrenergic

45 Zolmitriptan 139264-17-8 Headache, headache pain, nausea

TOTAL 50.25




Sr.

no.

Particulars Details


(Rs. in Crores):

5.6 Crores

B Total Plot area( sq. meter) 7049.94 Sq. m.

Green belt area ( sq. meter) 2326.48 Sq. m. (33 %)

C Employment generation 30 Nos.

Page 38 of 92


Page 38 of 92

D Water

i



GIDC Water Supply, Jhagadia

Status of permission from the concern authority. Yes, Granted

GIDC water supply letter No.:

No/GIDC/DEE/ING/341

Dated: 24/10/2018


Category

Quantity

KLD

Remarks

(J) Domestic 5.0

(K) Gardening 12.0

(L) Industrial

Process 21.0

Washing 6.0

Boiler 5.0

Cooling 15.0

Others (Scrubbing) 3.0


Total (A + B + C) 67.0


14) Quantity to be recycled: Nil

15) Total fresh water requirement:67 KLD


Category Waste water

KLD

Remarks

(G) Domestic 4.0 Domestic wastewater shall be

disposed in Septic tank / Sock pit

System.

(H) Industrial

Process 25.0

Washing 6.0

Boiler 1.0

Cooling 5.0

Others (Scrubbing) 1.0* Reuse in plant premises or send

to end users

Total Industrial

waste water

38.0 The Industrial effluent shall be

treated in ETP and treated effluent

shall be sent to common MEE

facility, M/s. ACPTCL,

Ankleshwar.

Total [A + B] 42.0

Note:

1. Worst Case Scenario For Water Consumption Is Based On Considering Rabeprazole Sodium, Pregabalin,

Efavirenz, Ursodiol, Tamsulosin HCl Product.

2. Worst Case Scenario For Waste Water Generation Is Based On Considering Rabeprazole Sodium, Fluconazole,

Page 39 of 92


Page 39 of 92

Zonisamide, Candesartan, Zolmitriptan Product.



In-House ETP (Primary & Advance treatment )-38 KLD


Domestic: Domestic wastewater (4 KL/Day) shall be disposed in Septic tank / Sock pit System.

Industrial: The Industrial effluent 38 KL/Day shall be treated in ETP and treated effluent shall be sent to

common MEE facility, M/s. ACPTCL, Ankleshwar.

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

Common MEE facility of M/s. ACPTCL (Ankleshwar Cleaner Process Technology Centre Limited,

Ankleshwar)



Yes

Common MEE facility of M/s. ACPTCL , Ankleshwar membership –

Ref No.: ACPTCL/1300000161/2018-19/38, Date of Issue: 11/07/2018



Water Consumption= 67

Domestic=5 Industrial=50 Gardening=12

Process=21 Boiler=5 Cooling=15 Washing=6

Process=26 Boiler=1 Cooling=5 Washing=6

ETP=38 KLD

4 KL/Day

Septic tank/

Soak Pit

System

Common MEE OF M/S. ACPTCL,

ANKLESHWAR-38 KLD

Scrubbing-3.0

Scrubbing

media will be

reused in

plant

premises and

sold to end

user who is

having Rule-9

Page 40 of 92


Page 40 of 92

Total reuse- Nil

Source of waste

water for reuse

with quantity in

KLD


quantity in KLD

Remarksregar

ding feasibility

to reuse i.e.

w/w

characteristics

(COD, BOD,

TDS etc.)

--

E Air



-

Sr. no.

Source of emission

With Capacity

Stack

Height

(meter)

Type of Fuel


Type of emissions i.e. Air

Pollutants


Measures (APCM)

1

Boiler

(Capacity-2 TPH)

(No. 1)

30 m Natural

Gas 193

m3/Hr

SPM < 150

mg/Nm3

SO2 < 100 ppm

NOx < 50 PPM


2

Boiler

(Capacity 1PH)

(No. 2)

30 m

Agro

waste/

Briquettes of

Biocoal

3 MT/Day Multicyclone

Separator & Bag Filter

3

Thermopack

(Capacity- 1 Lakh

Kcal/Hr)

15 m Natural

Gas 160

m3/Hr Adequate Stack

Height

4 D.G.Set -75 KVA

(Stand By) 11 m Diesel 7 Lit/Hr Adequate Stack

Height

-


-

Sr. no.

Specific Source of emission (Name of the

Product & Process)

Type of emission Stack/Vent

Height (meter)


1

Reaction Vessel

(Chlorination/

Sulfonation)

cl2 ≤ 09 mg/Nm3

HCl ≤ 20 mg/Nm3

SO2 ≤ 40 mg/Nm3

11 m Alkali Scrubber

2 Reaction Vessel

(Ammoniation) NH3 ≤ 175 mg/Nm3 11 m Water+ HCL Scrubber

3 Reaction Vessel 11 m Water + Alkali

Scrubber

Page 41 of 92


Page 41 of 92

(Bromination) br2 ≤ 2 mg/Nm3

hbr ≤ 30 mg/Nm3

-



26. Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures.

27. Adequate ventilation will be provided.

28. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus

minimizing the fugitive emissions.

29. Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.

30. Periodic monitoring of work area will be carried out to check the fugitive emission.


32. For dust emissions bag filter will be provided.

33. Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents

through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.


35. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent

pumps.

F Hazardous wastes

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

i

SR. NO.

TYPE/NAME OF HAZARDOUS WASTE

SOURCE OF GENERATION

CATEGORY AND SCHEDULE AS PER HW RULES.

QUANTITY (MT/ANNUM)

DISPOSAL METHOD

1 Discarded Drums/ Bags

Storage & Handling of Raw Material

Schedule- I (33.3)

151.6 MT/Annum

Collection, Storage and sent to authorized recycler after decontamination.

2 Oily/contaminated cotton waste

- Schedule- I (28.1)

0.72 MT/Annum

Collection, Storage, Transportation, Disposal at TSDF.

3 ETP Sludge ETP Schedule- I (35.3)

36.0 MT/Annum

Collection, Storage, Transportation and Disposal at TSDF of M/s. BEIL Ankleshwar.

4 Process waste (Spent Salt)/Residue

Manufacturing Process [Product- Certizine Di HCl, Telmisartan, Efavirenz, Rosuvastatine Calcium, Emtricitabine, Fluconazole]

Schedule- I (28.1)

36.0 MT/Annum

Collection, Storage, Transportation & sent for co-processing in cement industries or incineration at CHWIF.

5 Distillation Residue From Distillation Solvent/s

Schedule- I (20.3)

120.0 MT/Annum

Collection, Storage, Transportation and Disposal at TSDF of M/s. BEIL Ankleshwar.

Page 42 of 92


Page 42 of 92

6 Used Oil Equipment & Machineries

Schedule- I (5.1)

13.2 MT/Annum

Collection, Storage and reuse as lubricants in the machineries within the premises or sent to authorized re-processors.

7 Spent H2SO4 (70%)

Manufacturing process

[Product- Cetirizine Di Hydrochloride]

Schedule- I (26.3)

600 MT/Annum

Collection, Storage, Transportation and disposal by selling to authorized end user registered under Rule-9.

8 Spent Carbon Manufacturing process

[Product-Itraconazole, Pregabalin, Zonisamide,

Ursodiol]

Schedule- I (28.3)

2.4 MT/Annum

Collection, Storage, Transportation and sent for co-processing in cement industries or incineration at CHWIF.

9 HBr(35%) Manufacturing process + scrubbing

media [Product- Cis Bromo

Benzoate, Itraconazole, Albendazole,

Phenylephrine HCl ]

Schedule- I (28.1)

2760 MT/Annum

Collection, Storage, Transportation and disposal by selling to authorized end user registered under Rule-9

10. Sodium Sulfite (20%)

Scrubber Schedule- I (28.1)

230 MT/Annum

11 Liquor Ammonia (25%)

Manufacturing process + scrubbing

media [Product- Modafinil,

Albendazole, Zonisamide,

Montelukast Sodium ]

Schedule- I (28.1)

1560 MT/Annum

Collection, Storage, Transportation and reuse within premises-1068 MT/Annum Required MT/Annum Product no.3-108.0 MT/Annum Product no. 6-216.0 MT/Annum Product no. 14-120.0 MT/Annum Product no. 19-228.0 MT/Annum Product no. 23-396.0 MT/Annum OR 492 MT/Annum Collection, Storage, Transportation and disposal by selling to authorized end user registered under Rule-9

12 Dil HCL (30%) Manufacturing process + scrubber

[Product-Trimebutine

Schedule- I (26.3)

924 MT/Annum

Collection, Storage, Transportation and reuse within premises-

Page 43 of 92


Page 43 of 92

Maleate, Memantine HCl]

257 MT/Month Required MT/Annum Product no.33-84.0 MT/Annum Product no. 37-128.0 MT/Month Product no. 39-45.0 MT/month OR 667 MT/Annum Collection, Storage, Transportation and disposal by selling to authorized end user registered under Rule-9

13 Spent Catalyst Manufacturing process [Product-

Triclabendazole, Venafaxine

Hydrochloride]

Schedule- I (28.2)

2.4 MT/Annum

Collection, Storage, Transportation and give to manufacturer for regeneration for reuse.

14 Spent Solvent Manufacturing process

[Product No.-13,39,27,9, 15,23,16,33]

Schedule- I (28.6)

3000 MT/Annum

Collection, Storage & recovery within the premises .

15 Sodium Bromide (30%)

Scrubber Schedule- I (28.1)

210 MT/Annum

Collection, Storage, Transportation and disposal by selling to authorized end user registered under Rule-9

-


(For HW management)

Membership of TSDF/ Common

Hazardous Waste Incineration Facility

(CHWIF) that is M/s. BEIL, Ankleshwar,

vide letter no.:

BEIL/ANK/2018,Dated:04/09/2018

iii Details of Non-Hazardous waste & its disposal

(MSW and others)

No non Hazardous Waste will be

generated.



• The solvent distillation system shall be designed so as to achieve minimum 95.31 % recovery of solvent.

• Two condenser will install with cooling water and chilled brine to recover the solvent.

• Primary Condenser HE-01: Cooling Tower water or Chilled water (at 10 0C) will be used to condense the solvents depend

on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary

Condenser

• VOC Trap Condenser HE-02: Chilled Brine at -5 0C will be used to trap any traces of Solvent which is slipped from

Secondary condenser

Solvent Recovery Pattern

Name of Solvent Total Solvent Input Kg

Qty of Solvent

Recycled Kg

Qty of Losses

Kg

Recovery %

Loss %

Page 44 of 92


Page 44 of 92

Methanol 1057.12 1011.35 45.77 95.67 4.33

Toluene 1351 1289.73 61.27 95.46 4.54

Di Chloro Methane 475.95 455.38 20.57 95.68 4.32

Ethyl Acetate 1199.86 1150.55 49.31 95.89 4.11

Dimethyl formamide 570.83 545.94 24.89 95.64 4.36

Butanol 34.78 33.50 1.28 96.32 3.68

Acetone 276.95 263.97 12.98 95.31 4.69

Hexane 415.33 398.55 16.78 95.96 4.04

IPA 386.22 370.05 16.17 95.81 4.19


To prevent losses of these solvents in atmosphere, following infrastructure shall be used in addition to LDAR program

• Leak Free Pumps for transfer of solvents

• MSW Gaskets in solvent pipelines to prevent leakage from flanges

• Minimum number of flanges, joints and valves in pipelines.

• To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps.

• All the rotating equipments like pumps will be installed with Mechanical Seals to arrest any sort of emissions.

• Condenser and scrubber post Reactor with cooling arrangement

• Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through

hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.

• In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the

contaminated china clay (vermiculate) and send to ETP.

• If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark.

• Two condensers will install with cooling water and chilled brine to recover the solvent.

• Primary Condenser HE-01: Cooling Tower water or Chilled water (at 50C) will be used to condense the solvents depend

on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary

Condenser.

• VOC Trap Condenser HE-02: Chilled Brine at -15 0C will be used to trap any traces of

Solvent which is slipped from Secondary condenser.

Solvent Recovery Pattern After LDAR System is Installed

Name of Solvent Total Solvent Input Kg

Qty of Solvent Recycled Kg

Qty of Losses

Kg

% Recovery

% Loss

Methanol 1057.12 1029.35 27.77 97.37 2.63

Toluene 1351 1299.73 51.27 96.21 3.79

Di Chloro Methane 475.95 459.38 16.57 96.52 3.48 Ethyl Acetate 1199.86 1160.55 39.31 96.72 3.28

Dimethyl 570.83 550.94 19.89 96.52 3.48 Butanol 34.78 33.50 1.28 96.32 3.80 Acetone 276.95 269.97 6.98 97.48 2.52

Hexane 415.33 405.55 9.78 97.65 2.35

IPA 386.22 376.05 10.17 97.37 2.63


• Technical presentation was made by the project proponent dated 23/01/2019.





the study area of 10 km radial distance from project site for the period Oct., 2017 to Dec., 2017. Ambient Air

Page 45 of 92


Page 45 of 92

Quality monitoring was carried out for PM10, PM2.5, SO2, NO2, NH3, CO, O3, Pb, C6H6, BaP, As, Ni, HC &

VOC at ten 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 ISCST3. The resultant






• During SEAC meeting on 23/01/19, committee noted that this is new project. Industrial effluent after primary

treatment within premises will be sent to common MEE, M/s. ACPTCL, Ankleshwar for further treatment and

disposal.

• Natural gas, HSD and agro waste/briquettes of bio-coal will be used as fuel. Multi cyclone separator and bag

filter will be provided as APCM with solid fuel fired boiler. Water scrubber followed by acid scrubber will be

provided with amination reactor and alkali scrubber will be provided with chlorination/sulphonation reactor and

Water scrubber followed by alkali scrubber will be provided with bromination reactor as APCM.

• PP addressed Hazardous Waste as per HWR – 2016 including bleed liquors. PP addressed EMP, CER with



• After detail deliberation the committee unanimously decided to recommend the proposal for grant of

EC to SEIAA.

1. Unit shall send wastewater to Common MEE only after achieving inlet norms to common MEE prescribed

by GPCB in order to achieve no adverse impacts on Environment and Human Health.

2. Entire quantity of spent solvent shall be distillate in-house and recovered solvent shall be reused within

premises.

3. Unit shall comply all the conditions & recommendations mentioned in the guidelines for the management of

the spent solvents published by GPCB in letter and spirit.

4. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB

guidelines.

5. Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.

6. IA/GJ/ND2/64997/2017 M/s. Innovative Lifescience

Plot No. 9107/02, GIDC Estate,

Ankleshwar, Tal.: Ankleshwar, Dist.:

Bharuch.

Appraisal



Page 46 of 92


Page 46 of 92

• Project Proponent (PP) has submitted online application vide no. IA/GJ/ND2/64997/2017 dated 16/01/2019 for

obtaining Environmental Clearance.

• MoEFF&CC issued TOR to PP vide their letter dated J-11011/295/2017-IA-II(I),Vide 11/08/2017.

• Project proponent has submitted EIA Report prepared by M/s. Aqua Air Environmental Engineering Pvt Ltd.

based on the TOR issued by MoEF&CC.

• This is existing unit and now proposes for expansion as tabulated below:

Sr. No.

Name of Products CAS No. Existing Quantity

Additional Quantity

Total after Proposed expansion

End use

(MT/Month)

GROUP-1

1 Calcium Chloride 10043-52-4 50 - 50 Waste Water Treatment

2 EDTA [Ethylene diamine tetra acetic acid]

60-00-4 20 - 20 Control heavy metal

3 Di-Sodium Sulphate 7767-82-6 50 - 50 Fining Agent 4 Ammonium Nitrate 6484-52-2 50 - 50 Fertilizer

5 Sodium Acetate 127-09-3 50 - 50 Pickling Agent

6 Ammonium Chloride

12125-02-9 50 - 50 Acidifier

7 L2 [(4R-cis)-1,1-dimethylethyl-6-[2-[2-(4-fluorophenyl)-3-phenyl-4 [(phenylamino)carbonyl]-1H-pyrrol-1-yl]ethyl]-2,2-dimethyl-1,3-dioxane-4-acetate]

125971 -95-1 -

5

5

Anti-Lipemic

8 L3 /[(4R-cis)-1,1-dimethylethyl-6-[2-[2-(4-fluorophenyl)-3-phenyl-4 [(phenylamino)carbonyl]-1H-pyrrol-1-yl]ethyl]-2,2-dimethyl-1,3-dioxane-4-acetate]

125971 -95-1 Anti-Lipemic

9 Phenylbutazone 50 -33-9 Anti-Inflam matory,

Analgesic 10 Metoprolol base 37350 -58-6 Anti-

Hypertensive 11 Pregabalin 148553-50-8 Anti-Epileptic

12 Racemic [3-(Carbamoylmethyl)-5-methyl hexanoic acid]

181289 -15-6 Anti-Epileptic

Page 47 of 92


Page 47 of 92

13 RCMH [ R(-)-3-(Carbamoylmethyl)-5-methyl hexanoic acid]

181289-33-8 Anti-Epileptic

14 Phenylephrine HCl 61-76-7 Decongestant

15 Phenylephrine base 59-42-7 Decongestant

GROUP-2

16 Polyallylamine HCl 71550-12-4 - 20 20 Hyperphosphatemia

17 Polyallylamine 30551-89-4 - 20 20 Hyperphosphatemia

18 Allylamine HCl 10017-11-5 - 20 20 Hyperphosphatemia

19 2-(2-chloro ethoxy) acetic acid

14869-41-4 - 20 20 AntlAlergic

TOTAL 270 85 355




Sr. no.

Particulars Details

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

Existing:1.00 Crores Proposed:3.00 Crores Total: 4.00 Crores

B Total Plot area ( sq. meter)

Existing: 999.Sq. m. Proposed: --- Sq. m. Total: 999.Sq. m.

Green belt area ( sq. meter)

Existing: 100 Sq. m. Proposed: 230 Sq. m. Total: 330 Sq. m.

C Employment generation Existing: 5 Nos. Proposed: 25 Nos. Total:30 Nos.

D Water

i

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

GIDC Water Supply, Ankleshwar


Yes GIDC water supply letter No. NO/NA//DEE(W/S)/770 dated 18/04/2017


Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

(M) Domestic 0.5 2.0 2.5 (N) Gardening -- 1.0 1.0 (O) Industrial

Process Nil 12.0 12.0 Washing -- 0.5 0.5

Boiler Nil 5.0 5.0

Page 48 of 92


Page 48 of 92

Cooling Nil 5.0 5.0

Others (Scrubbing) -- 1.0 1.0

Industrial Total Nil 23.5 23.5

Grand Total (A+B+C) 0.5 26.5 27.0

16) Total water requirement for the project: 27.0 KLD 17) Quantity to be recycled: Nil 18) Total fresh water requirement: 27.0 KLD


Category Existing KLD

Proposed (Additional)

KLD

Total after

Expansion

KLD

Remarks

(I) Domestic 0.45 1.6 2.05 Domestic wastewater will be disposed of through septic tank/soak pit.

(J) Industrial

Process Nil 8.0 8.0

Washing -- 0.5 0.5

Boiler Nil 0.3 0.3

Cooling Nil 0.2 0.2

Others -- 1.0 1.0


Nil 10.0 10.0 Industrial wastewater (9.5 KL/Day) shall be treated in ETP within premises and treated waste water sent to common MEE of M/s. ACPTCL, Ankleshwar for further Treatment & final disposal. 0.5 KL/Day scrubbing media will be reused in plant premises.

TOTAL(Domestic +Industrial)

0.45 11.6 12.05

iv Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP –Primary Treatment

Page 49 of 92


Page 49 of 92

� ETP –Primary Treatment

M/s. Innovative Life Science shall have an Effluent treatment plant consisting of primary treatment units. The details of ETP are as follows. First all waste water streams shall be passed from O & G Trap (OGT-01) where floating O & G shall be removed from the effluent and collected in O & G Collection Tank (OGCT-01). Then, wastewater shall be collected in Equalization cum Neutralization tank (ENT-01) where the continuous addition and stirring of Caustic solution is done to maintain neutral pH of wastewater from Caustic Dosing Tank (CDT-01) as per requirement by gravity. Mixer is provided in the ENT-01 to keep all suspended solids in suspension and for proper mixing. Then, neutralized wastewater shall be pump to Primary Settling Tank (PST-01). Alum and Polyelectrolyte shall be dosed from Alum Dosing Tank (ADT-01) and Polyelectrolyte Dosing Tank (PEDT-01) respectively by gravity into PST-01 to carry out coagulation by using a Mixer. Then Mixer will be stopped, and effluent is allowed to settle in Primary Settling Tank (PST-01). After Primary treatment, Clear supernatant from PST-01 shall be collected in Treated Effluent Sump (TES-01) before sent to Common MEE of M/s Ankleshwar Cleaner Process Tech. Centre Ltd (ACPTCL) for further treatment and disposal. Sludge settled in PST-01 shall be collected in Sludge Drying Beds (SDBs-01-A/B) where, dewatering shall be carried out before storage in HWSA and ultimate disposal to TSDF. The Domestic wastewater is disposed of through septic tank & soak pit. SIZE OF TANKS :

S.N. Name of unit Size (m x m x m) No. MOC/ Remark

Flow 10.0 KLD

1 O & G Trap 2.0 x 0.8 x (0.8LD

+0.3FB) 1 RCC M30+ A/A Bk. Lining

2 O & G collection

Tank 100 Lit 1 HDPE/RCC M30

3 Equalization cum

Neutralization Tank (ENT-01)

2.0 x2.0 x (2.5 LD+0.5 FB)

1 RCC M30+A/A Bk. Lining

4

Primary Settling Tank

(PST-01)

1.5 x 1.5 x (2.0LD + 0.5 HB+0.5 FB)

1 RCC M30/MSFRP

5

Treated Effluent Sump

(TES-01)

2.0 x 2.0 x (2.5 LD+0.5 FB)

1 RCC M30

6

Sludge Drying Beds

(SDBs-01-A/B) 3.0 x 2.0 2 Bk. Maso. With RCC Bedding

7

Caustic Dosing Tank

(CDT-01) 250 Lit 1 HDPE

8

Alum Dosing Tank

(ADT-01) 250 Lit 1 HDPE

9

Poly Dosing Tank

(PEDT-01) 100 Lit 1 HDPE

EXPECTED CHARACTERISTICS OF EFFLUENT: Sr.

No. Parameter

Raw Effluent

(mg/L)

Primary

Treated

Effluent (mg/L)

1. pH 4.0 to 8.0 7-8

2. COD (mg/l) 40000 36750

3. BOD3(mg/l) 9000 6750

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4. TDS (mg/l) 50,000 50,000

FLOW DIAGRAM FOR PROPOSED ETP


Domestic: Domestic wastewater will be disposed of through septic tank/soak pit.

Industrial: Industrial wastewater (10 KL/Day) shall be treated in ETP within premises and treated waste water sent to common MEE of M/s. ACPTCL, Ankleshwar for further treatment & final disposal.

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

� Common MEE of M/s. Ankleshwar Cleaner Process Technology Centre Ltd. (ACPTCL), Ankleshwar


(For waste water treatment) Common MEE of M/s. ACPTCL, Ankleshwar Membership Certificate No :ACPTCL/1300000072/2017-18/96, Date of issue : 08/12/2017


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WATER BALANCE DIAGRAM : Total Proposed: Unit KL/Day

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

Total reuse: Nil (No Reuse/Recycle of water)

Source of waste water for reuse with quantity in KLD


Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.)

---

-

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. Existing & Proposed

-

Sr. no.

Source of emission

With Capacity


Type of Fuel

Quantity of Fuel

MT/Day

Type of emissions i.e. Air

Pollutants


Measures (APCM)

1 Boiler (Capacity- 800 Kg/Hr)

18 Briquette

of Biocoal

800 Kg/Day

SPM ≤ 150 mg/ Nm3

SO2 ≤ 100 ppm

Cyclone Separator +

Water

Scrubbing = 1.0

Scrubbing =

Fresh Water = 27 KL/Day

Domestic = 2.5 Gardening = Industrial =

2.05

KL/Day �

Specific

tank & soak

pit system

Process =

12.0 Washing =

0.5

Boiler = 5.0

Cooling =

5.0

Process Washing = Boiler = 0.3 Cooling =

0.2

ETP

CMEE (ACPTCL)

for disposal =

9.5

0.5 KL/Day

� reused

Page 52 of 92


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Existing NOx≤ 50 ppm Scrubber

2

D.G. Set (Capacity- 125 KVA) (Stand By) Existing

11 Diesel 10 Lit/Hr

SPM ≤ 150 mg/ Nm3

SO2 ≤ 100 ppm

NOx≤ 50 ppm


3

Boiler (Capacity- 1 TPH) Proposed

18

Briquette of

Biocoal

1.0 MT/Day

SPM ≤ 150 mg/Nm3

SO2 ≤ 100 ppm

NOx ≤ 50 ppm

Multi-cyclone separator with bag

filter

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

Existing & Proposed

-

Sr. no.

Specific Source of emission

(Name of the Product & Process)

Type of emission



Measures (APCM)

Existing : There shall be no process gas emission from the manufacturing process and any other ancillary industrial operation through various stacks vent of reactors, Process, vessel from plant premises.

1 Process Vent (Chlorination) –Proposed

HCl ≤ 20 mg/ Nm3

11 Two stage water scrubber

2 Process Vent (Ammoniation)-Proposed

NH3 ≤ 175 mg/ Nm3

11 Two stage Water +HCl Scrubber

-



36. Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures.

37. Adequate ventilation will be provided. 38. Regular maintenance of valves, pumps, flanges, joints and other equipment will be

done to prevent leakages and thus minimizing the fugitive emissions of VOCs. 39. Entire process will be carried out in the closed reactors with proper maintenance of

pressure and temperature. 40. Periodic monitoring of work area will be carried out to check the fugitive emission. 41. To eliminate chances of leakages from glands of pumps, mechanical seal will be

provided at all solvent pumps. 42. Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be

equipped with on-line pH meter with hooter system for better operational control. 43. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank

vents will be connected to vent chillers. 44. Minimum number of flanges, joints and valves in pipelines. 45. Regular inspection of floating roof seals and proper preventive maintenance of roofs

and seals for tanks. 46. Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer

area will be collected through hoods and ducts by induced draft and controlled by scrubber/

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dust collector. 47. Dedicated scrubber will be provided are used for fugitive emissions to control. 48. For dust emissions bag filter will be provided. 49. Enclosures to chemical storage area, collection of emission from loading of raw materials in

particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.

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

i

Sr.

No.

Hazardou

s/Solid

Waste

Source Category/

Schedule

Quantity

(MT/ Year)

Mode Of

Disposal


1 Discarded

Container

s /Bags

Raw

Material and

Storage

33.1

(Sch.-I)

6.0

MT/Year

15

MT/Year

21.0

MT/Yea

r

Collection,

Storage,

Transportat

ion, reuse

/sale to

authorized

recycler.

2 Used /

Spent Oil

Equipment

& Machinery

5.1

(Sch.-I)

500040

Gm/Year

1500

Gm/Year

501540

Gm/Yea

r

Collection,

Storage,

Transportat

ion &

reuse/ Sale

to

authorized

traders.

3 ETP

Sludge

ETP 35.3

(Sch.-I)

-- 20.00

MT/Year

20.00

MT/Yea

r

Collection,

Storage,

Transportat

ion & sent

to common

TSDF Site.

4 Spent

Solvent

Manufacturi

ng Process

[Product-

Pregabalin]

28.6

(Sch.-I)

-- 4500

MT/Year

4500

MT/Yea

r

Collection,

Storage,

recovered

through in

house

distillation

or sent for

distillation

job work to

authorized

recycler

then reuse

in process.

5 Distillatio

n Residue

Distillation 20.3

(Sch.-I)

-- 180

MT/Year

180

MT/YeaCollection,

Storage,

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r Transportat

ion & sent

to cement

industries

for co-

processing

or Sent for

incineratio

n at

common

incinerator

6 Spent

Carbon

Process

{Product-

RCMH[R (-)-

3-

(Carbamoyl

methyl)-5-

methyl

hexanoic

acid)}

28.3

(Sch-I)

-- 6.0

MT/Year

6.0

MT/Yea

r

Collection,

Storage,

Transportat

ion and

sent for co-

processing

in cement

industries

or sent to

CHWIF Site.

7 Ammoniu

m

Chloride

Scrubber 28.1

(Sch.-I)

-- 180

MT/Year

180

MT/Yea

r

Collection,

Storage &

send to ETP

for further

treatment.

8 HCl (30%) Scrubber 28.1

(Sch.-I)

-- 180

MT/Year

180

MT/Yea

r

Collection,

Storage &

reuse in

plant

premises

for

manufactur

ing of

calcium

chloride –

Require

quantity of

HCL (30%) -

708

MT/Year.

-

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

TSDF Site : BEIL –Ankleshwar, RSPL-Panoli, GSPL-Palsana Membership + : BEIL/ANK/288, Dated: 28/08/2012 RSPL & GSPL - Dated: 15/04/2017

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

No non Hazardous Waste will be generated.



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• The solvent distillation system shall be designed so as to achieve minimum 95.33 % recovery of solvent.

• Two condenser will install with cooling water and chilled brine to recover the solvent. • Primary Condenser HE-01: Cooling Tower water or Chilled water (at 100C) will be

used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser

• VOC Trap Condenser HE-02: Chilled Brine at -5 0C will be used to trap any traces of Solvent which is slipped from Secondary condenser.

Solvent Balance:

SOLVENT BOILING

POINT

(°C)

VAPOR

PRESSURE

(KPA@ 20OC)

INPUT

Kg

RECOVER

Kg

LOSSES

Kg

%RECOV

ER

%LOSS

ES

Methanol 64.5 °C 12.3

(@ 20°C)

4000 3820 180 95.5 4.5

Iso Propyl

alcohol

82.5 °C 4.4 (@ 20°C) 1000 960 40 96.0 4.0

Cyclone

Hexane

80.75 °C 12.9 kPa

(@ 20°C)

800 778 22 97.25 2.75

Acetone 56.2 °C 24 (@ 20°C) 950 910 40 95.79 4.21

Toluene 110.6 3.8 @ 25oC 1000 950 50 95.0 5.0

Chloroform 61°C 21.1 kPa (@

20°C)

10800 10300 500 95.37 4.63

Ethyl

Acetate

77°C 12.4 kPa (@

20°C) 300 285 15 95.0 5.0

ii VOC emission sources and its mitigation measures To prevent losses of these solvents in atmosphere, following infrastructure shall be used in

addition to LDAR program

• Leak Free Pumps for transfer of solvents • MSW Gaskets in solvent pipelines to prevent leakage from flanges • Minimum number of flanges, joints and valves in pipelines. • To eliminate chances of leakages from glands of pumps, mechanical seal will be

provided at all solvent pumps. • All the rotating equipments like pumps will be installed with Mechanical Seals to

arrest any sort of emissions. • Condenser and scrubber post Reactor with cooling arrangement • Enclosures to chemical storage area, collection of emission from loading of raw

materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.

• In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send to ETP.

• If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark.

• Two condensers will install with cooling water and chilled brine to recover the solvent.

• Primary Condenser HE-01: Cooling Tower water or Chilled water (at 50C) will be used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser.

• VOC Trap Condenser HE-02: Chilled Brine at -15 0C will be used to trap any traces

Page 56 of 92


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of • Solvent which is slipped from Secondary condenser.

SOLVENT BOILING

POINT

(°C)

VAPOR

PRESSURE

(KPA@ 20OC)

INPUT

Kg

RECOVER

Kg

LOSSES

Kg

%RECO

VER

%LOSSES

Methanol 64.5 °C 12.3

(@ 20°C)

3820 180 95.5 4.5 3820

Iso Propyl

alcohol

82.5 °C 4.4

(@ 20°C)

960 40 96.0 4.0 960

Cyclone

Hexane

80.75 °C 12.9 kPa (@

20°C) 778 22 97.25 2.75 778

Acetone 56.2 °C 24

(@ 20°C)

910 40 95.79 4.21 910

Toluene 110.6 3.8 @ 25oC 970 30 97.0 3.0 970

Chloroform 61°C 21.1 kPa (@ 20°C)

10300 500 96.37 3.63 10300

Ethyl

Acetate

77°C 12.4 kPa (@

20°C) 291 9 97.0 3.0 291







the study area of 10 km radial distance from project site for the period March 2017 to May 2017. Ambient Air

Quality monitoring was carried out for PM10, PM2.5, SO2, NO2, NH3, CO, O3, Pb, C6H6, BaP, As, Ni, HC &

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 ISCST3. The resultant






• During SEAC meeting on 23/01/19, committee noted that this proposal is for expansion. This unit has valid

CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP ensured that there are no court

cases pending and no public complaints against the project. Total plot area is 999 sq.m. There will be no

increase in plot area after proposed expansion. Upon asking, PP could not address area adequacy with

reference to expansion satisfactorily.

Page 57 of 92


Page 57 of 92

• Industrial effluent after primary treatment within premises will be sent to common MEE, M/s. ACPTCL,

Ankleshwar for further treatment and disposal.

• HSD and agro waste/briquettes of bio-coal will be used as fuel. Multi cyclone separator and bag filter will be

provided as APCM with solid fuel fired boiler. Two stage water scrubber will be provided with chlorination

vessel and two stage water scrubber followed by acid scrubber will be provided with amination vessel as

APCM.

• PP addressed Hazardous Waste as per HWR – 2016. Committee asked PP to address exhausted scrubbing

media (bleed liquors) management under the HWM Rules, 2016 to which PP could not explained. PP

addressed EMP, CER with details of budgetary provisions was found satisfactory.

• After deliberation, PP was asked to submit following details and it was unanimously decided to

consider the proposal in one of the upcoming SEAC meeting after submission of the following.

1. 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.

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

3. Project specific safety details considering PESO standards.

7. SIA/GJ/IND2/30545/2018

M/s. Jay Chemical Industries Limited, Unit-3

Plot no. - 109 and 220, Phase - II, GIDC,

Vatva, Dist.: Ahmedabad

Screening & Scoping



• This office has received an application vide their online proposal no. SIA/GJ/IND2/30545/2018 dated

27/12/2018 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for preparation of

EIA/EMP report.

• This is an existing unit and now proposes for expansion as tabulated below:

Sr. No

Name of Products

CAS Number

Type of Dye

Production capacity MT/Month

End Use of Products

Ex

isti

ng

Pro

po

sed

To

tal

1 Turquoise Blue

Reactive 40 0 40 Textile dye

Page 58 of 92


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2 Vinyl Sulphone Intermediate 160 0 160 Intermediate for dye manufacturing 3 Acetanilide Intermediate 60 0 60

4 Synthetic Organic Dyes

Reactive/ Disperse

Use in Textile industry

1 Acid Black 210 99576-15-5

REACTIVE 0 1000 1000

2 Acid Red 357 61951-36.8

3 Reactive Black 5 17095-24-8


5 Reactive Blue 220 128416-19-3

6 Reactive Blue 19 2580-78-1

7 Reactive Red 198 78952-61-1

8 Reactive Orange 107

94158-82-4


10 Reactive Orange 16 20262-58-2

11 Reactive Red 35 85940-67-6

12 Reactive Red 106 152066-97-2


14 Reactive Violet 5 12226-38-9

15 Reactive Yellow 37 20298-05-9



18 Reactive Blue 4 -



21 Reactive Blue 198 124448-55-1

22 Reactive Blue 160 93921-06-3

23 Reactive Blue 248 -

24 Reactive Green 19 61931-49-5


26 Reactive Violet 46 -



29 Reactive Red 74 12270-82-5

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31 Reactive Red 31 93919-17-6

32 Reactive Red 120 68214-04-0

33 Reactive Red 141 71002-20-5

34 Reactive Orange 14 -

35 Reactive Yellow 86 -




39 Reactive Yellow 145A

93050-80-7


41 Reactive Blue 172 85782-76-9

42 Reactive Blue 194 80156-94-1

43 Reactive Brown 9 70788-62-4

44 Reactive Red 198 A 111211-40-6

45 Reactive Red 195A 93050-79-4

46 Reactive Red 250 152187-49-0




50 Direct Orange 108 6358-79-8

51 Direct Blue 199 90295-11-7

52 Direct Blue 86 1330-38-7

53 BLACK BCH -

54 Yellow 22 12226-49-2

55 REACTIVE YELLOW C4G

-

56 Reactive Orange 122

12220-12-1

57 Reactive Brilliant Blue 221

93051-41-3

58 Brilliant Blue JRF 84057-71-6

59 BLUE 72 68967-01-1

60 BLUE P5G 12236-87-2

61 BLACK MIX -

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Page 60 of 92

62 YELLOW 160A 84000-63-5

63 YELLOW 95 84045-63-6

64 YELLOW 205 780759-89-9

65 RED 21 80419-51-8

66 YELLOW MIX -

67 RED MIX -

68 BLUE MIX -

69 ORANGE MIX -

70 Red 2BN / Red FB - CI Red 60

6408-72-6 Disperse Dye (Azo Cynation)

0 50 50

71 Reactive Violet-26 17418-58-5

72 Flourescent Yellow 10GF - CI Disperse 184

71838-87-4

Disperse Dye (Yellow Methine)

0 10 10

73 Flourescent Yellow 8GF - CI Disperse 82

12239-58-6

74 Flourescent Yellow 10GN - CI Disperse 232/184.1

35773-43-4

75 Brilliant Blue SR - CI Disperse Blue 354

104137-27-1

Disperse Dye (Blue Methine)

0 20 20

76 Cyanine Red - Disperse Dye (Cyanine Plant)

0 10 10

77 Cyanine Pink -

78 Cyanine Blue -

79 CI - Blue 56 12217-79-7

Disperse Dye (Multi P Plant)

0 10 10

80 CI - Yellow 64 10319-14-9

81 Blue BG - CI - Blue 60

12217-80-0

82 Orange RL - CI Orange 25

-

Disperse Dye (HCl- Nitrite Base Azo Dye)

0 400 400

83 Yellow SG - CI Yell 114

-

84 Yellow 4G – CI Yell 231

-

85 Scarlet BR - CI Red 74

-

86 Yellow C4G - C.I. Yellow 79

12220-70-1

87 Yellow SGL 70528-90-4

Page 61 of 92


Page 61 of 92

88 Yellow SG- C.I. Yellow 114

61968-66-9

89 Yellow 34 1344-37-2

90 Yellow 119 57308-41-5

91 Yellow 68 21811-64-3

92 Red 278 68248-10-2

93 Yellow M7G -

94 Yellow 247 -

95 Yellow 248 -

96 Yellow 249 -

97 Yellow 235 177570-98-8

98 Orange 25 31482-56-1

99 Red 74 61703-11-5

100 Yellow 56 -

101 Yellow 7GN -

102 Black 296 -

103 Black 1 6054-48-4

104 Orange 288 3769-57-1

105 Navy Blue 3G - CI Blue 79.1

3618-72-2

Disperse Dye (NSA Based Azo Dye)

0 500 500

106 Dark Red 2B - CI Red 167.1

-

107 Violet 3R - CI Violet 99

-

108 Blue 2R - CI Blue 183

-

109 Navy Blue 79.1 3618-72-2

110 Navy Blue 79.2 3618-72-3

111 Navy Blue 183 2309-94-6

112 Navy Blue 183.1 2537-62-4

113 Blue 291 56548-64-2

114 Blue 4R 66557-45-7

115 Blue 6GEF -

116 Blue 4RB -

117 Blue 4GEF -

118 Red BS 78564-86-0

119 Scarlet GS 86836-02-4

Page 62 of 92


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120 Red-XF2R -

121 Red 311 77907-28-9

122 Yellow Brown XF -

123 Brown XF -

124 Navy XF2R -

125 Navy XF2G -

126 Brown 378 -

127 Brown 165.1 -

128 Brown 165.1

129 Orange 61 12270-45-0

130 Orange 30 12223-23-3

131 Scarlet 3R C.I. Red 50

12223-35-7

132 Scarlet 3R C.I. Red 54

12217-86-6

133 Blue 373 51868-46-3

134 Red 202 61931-39-3

Total 260 2000 2260



• Water, Air and Hazardous waste management:

Sr. no.

Particulars Details

A Water

i

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

Water is sourced from GIDC water supply i.e. Vatva Industrial Estate Infrastructure Development Limited (SPV) of Vatva Industries Association.

Status of permission from the concern authority.Permission of Vatva Industrial Estate Infrastructure Development Limited (SPV) ofVatva Industrial Association is given.

ii Water consumption (KL/day)

- Existing

KL/day Proposed (Additional) KL/day

Total after Expansion KL/day

Remarks

UNIT - 3/1

UNIT - 3/2

(P) Domestic 2.67 5 30 37.67 GIDC fresh water

(Q) Gardening - - 5 5 (R) (S) Industrial

Process 10 15.7 1306 1331.7 GIDC fresh water

Page 63 of 92


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Washing 0.67 94.3 517 611.97 243.97 KLD GIDC fresh water, 190 KLD RO permeate and 178 KLD MEE condensate

Boiler 1.33 13 247 261.33

Cooling 1.66 2 45 48.66

Others - - -

Recycle 0 0 368 368 190 KLD RO permeate and 178 KLD MEE condensate

Total (A+B+C) 1928.33

-

iii

Waste water generation (KL/day)

-

Category Existing KL/Day

Proposed (Additional) KL/day

Total after Expansion KL/day

Remarks

UNIT - 3/1

UNIT - 3/2

(K) Domestic 2 5 26 33 Disposed to Soak Pit

(L) Industrial

To ETP followed by RO& MEE / CETP

Process 9 0 143 152

Washing 0.67 94.3 217 454.97

Boiler 0.33 0.7 20 21.03

Cooling - - -

Others - - -


10 95 380 485 After ETP treatment, 105 KLD going to CETP and 380 KLD will be sent to MEE followed by RO.

-

iv Treatment facility with capacity (ETP, CETP, MEE, STP etc).

The industrial effluent is treated in ETP of capacity 250 KLD &After ETP treatment, 105 KLD going to CETP and 380 KLD will be sent to MEE followed by RO.


Domestic: To Soak Pit

Industrial: The industrial effluent is treated in ETP of capacity 250 KLD &After ETP treatment, 105 KLD going to CETP and 380 KLD will be sent to MEE followed by RO.

vi Reuse/Recycle details (KL/day) -

vii B Air(Existing and Proposed)


Page 64 of 92


Page 64 of 92


-

SR. no.

Unit Source of emission

With Capacity

e.g. Boiler (8 TPH)


Name of the fuel

Quantity of Fuel MT/hr & MT/Day

Type of emissions

i.e. Air Pollutants

APCM

NAAQS (National Ambient

Air Quality Standards)

Existing

1 Unit - 3/1

Steam Boiler

12

Natural Gas

0.028 KL/Hr

Particulate Matter, SO2,

NOx N/A

PM- 150 ppm, SO2

– 100 µg/m3,

NOx - 50 µg/m3

2 HAG 20 0.07KL/Hr

3 Unit - 3/2

Thermic Fluid Heater

- 1 11

10 SCM/Hr

4 Thermic

Fluid Heater - 2

30

5 Steam Boiler

15 25 SCM/Hr

6 HAG (GS Recovery)

20 110 SCM/Hr

7 D.G.Set 12 Diesel 40 lit/hr.

Proposed

8 Unit - 3

HAG - 1 (Reactive

Plant) 20

Natural Gas

320 SCM/Hr

Particulate Matter, SO2,

NOx

N/A

PM- 150 ppm, SO2

– 100 µg/m3,

NOx - 50 µg/m3

9 HAG - 2

(Reactive Plant)

20 240 SCM/Hr

10 HAG - 3

(Reactive Plant)

20 240 SCM/Hr

11 Boiler

(Reactive Plant)

20 150 SCM/Hr

12 HAG - 1

(Disperse Plant)

20 120 SCM/Hr

13 HAG - 2

(Disperse Plant)

20 140 SCM/Hr

14 HAG - 3

(Disperse Plant)

20 240 SCM/Hr

15 HAG - 4

(Disperse Plant)

20 240 SCM/Hr

16 HAG - 5

(Disperse Plant)

20 240 SCM/Hr

17 Boiler 20 300 SCM/Hr

Page 65 of 92


Page 65 of 92

(Common) (Disperse

Plant)

(Common)

18 D.G.Set 12 Diesel 80 lit/hr.

-

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.) (Existing and Proposed)

-

Sr. no.

Unit Source of emission

Type of emission


APCM

Existing

1 Unit 3/1

Reaction Vessel (Sulphonation

Vessel)

SO2, HCl, Cl2

20 Water Ventury, Two Stage Water

Scubber followed by Alkali Ventury, Two Stage Alakali Scrubber

2 Spray Dryer (800 Lit/Hr) (Product)

PM 20 Cyclone Separator with Water

Scrubber

3

Unit - 3/2

Sulphonation Vessel - 1

SO2, HCl, Cl2

15 Water Ventury, Two Stage Water

Scubber followed by Alkali Ventury, Two Stage Alakali Scrubber

4 Sulphonation

Vessel - 2 SO2, HCl,

Cl2 15

Water Ventury, Two Stage Water Scubber followed by Alkali Ventury,

Two Stage Alakali Scrubber

5 Dumping Vessel SO2, HCl,

Cl2 15

Water Scubber followed by Alakali Scrubber

6 Spray Dryer (800

Lit/Hr)(GS - Recovery)

PM 20 Cyclone Separator + Water

Scrubber Primary + Water Scrubber Secondary Packed/Demister

Proposed

1

Unit - 3

HCl Scrubber-1 (Reactive Plant)

SO2, HCl, Cl2

25

Venturi Scrubber Water Scrubber-I + Alkali packed column-I + Alkali Venturi Scrubbing Alkali Packed

Column-II

2 HCl Scrubber-2 (Reactive Plant)

SO2, HCl, Cl2

25


Column-II

3

HCl Scrubber-3 (Blue Plant)

(Sulphonation Vessel-)

SO2, HCl, Cl2

25


Column-II

4 Ammonia Scrubber

NH4 15 Venturi Scrubber + Packed Column

Dip Tank

5 Spray Dryer - 1 (Reavtive Plant)

(2000 Lit/Hr) PM 40

Cyclone Separator + Water Scrubber Primary + Water Scrubber

Secondary Packed/Demister

6 Spray Dryer - 2 (Reactive Plant)

(1500 Lit/Hr) PM 40



7 Spray Dryer - 3 (Reactive Plant)

(1500 Lit/Hr) PM 40



Page 66 of 92


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8

HCl Scrubber-4 (HCl - Nitrite

Base Azo Disperse Plant)

SO2, HCl, Cl2

25


Column-II

9 Spray Dryer - 1 (Disperse Plant)

(750 Lit/Hr) PM 40




(750 Lit/Hr) PM 40




(1500 Lit/Hr) PM 40




(1500 Lit/Hr) PM 40




(1500 Lit/Hr) PM 40



-

v Fugitive emission details with its mitigation measures. (Existing and Proposed)

Parameter Frequency

TVOC Quarterly (Two Location : VS Plant & Turquoise Blue Plant)

PM Quarterly (Two Location : VS Plant & Turquoise Blue Plant)

Noise Quarterly 10 Location

Details will be covered in EIA report

C Hazardous waste (As per the Hazardous and Other Wastes (Management and Trans boundary Movement) Rules 2016. (Existing and Proposed)

i

Sr. no.

Type/Name of

Hazardous waste

Source of generation

Category and

Schedule as per HW

Rules.

Quantity (MT/Annum)

Disposal Method

Existing Propose

d Total UNIT

- 3/1 UNIT - 3/2

1 ETP Sludge ETP 35.3 480 3600 9600 13680

Packed in HDPE

Bags, and Dispose to TSDF

2 Gypsum Sludge

Pre- treatment

plant

26.1 - - 1000 1000

Packed in HDPE

Bags, and Dispose

to Cement Industry

3 Ammonium

Chloride 35.3 - - 256 256

Reused in plant


Evaporation 36.1 - - 256 256

Packed in HDPE


Page 67 of 92


Page 67 of 92

5 Spray Dry

Salt Evaporation 37.3 - - 3000 3000

Packed in HDPE


6 Used Oil Machinrary 5.1 0.33 1.1 1.8 3.23

Disposal by selling to register recycler

7 Discarded Container

Production 33.1 131.4 108 72 311.4


8 Discarded

Liners/Bags Production 33.1 - 9.6 8.4 18


9

Spent Acid (Spent

Sulphuric Acid)

Production 26.3 1800 7200 20400 29400

Disposal by selling

to NOVEL, Arvind

and Aarvee

denim and Actual

end user

10

Spent Acid (Spent

Hydrochloric Acid)

Production 26.3 - 7200 - 7200

- Quantity of discarded containers must be in MT/Annum.

ii Membership details of CETP, TSDF, CHWIF, Common MEE etc. CETP:Membership Certificate of M/s. The Green Environment Services Co-op. Society Ltd. For Effluent Treatment ICHWMF: Membership Certificate of M/s. SaurastraEnviro Projects Pvt. Ltd. and EcoCare Infrastructure Pvt. Ltd. For Hazardous Waste

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

Not Applicable

D i Spent Solvent management (If any)

Spent Sulphuric Acid and Spent Hydrochloric Acid are selling to NOVEL, Ecocare, Arvind and Aarvee denim.


Not Applicable


• During the meeting dated 23/01/2019, technical presentation made by project proponent.

• Committee noted that unit has valid CC&A for existing unit. Unit is complying conditions of CC&A. PP informed

that there are no court cases pending and no public complaints against the project.

Page 68 of 92


Page 68 of 92

• After proposed expansion, additional industrial effluent will be treated in ETP (P+S+T) followed by RO and

MEE. RO permeate and MEE condensate will be reused in washing within premises. PP ensured that there will

be no increase in organic and hydraulic load of effluent being discharged to CETP, Vatva after proposed

expansion. Natural gas and diesel will be used as fuel. Cyclone separator followed by two stage water

scrubber will be provided as APCM with proposed spray dryers. PP has addressed hazardous waste

management satisfactorily under the HWM Rules, 2016.

• 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. 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 therein. The details of

fund allocation and activities for CER shall be incorporated in EIA/EMP report.

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

project energy-efficient through 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.

3. 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.

4. 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 endeavor prevention

of losses of solvents to the best minimum extent.

5. PP shall furnish status of all the applicable rules, acts, regulation, clearances in a tabular form

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

unloading, storage, transportation, handling and processing of Solvents

7. 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.

8. Treatability & adequacy report for complete ZLD for additional waste water. Feasibility report for

complete reuse treated waste water for industrial purpose.

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

Page 69 of 92


Page 69 of 92

• 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/IND2/30082/2018 M/s. Liberty International ltd.

Plot No. C-19, G.I.D.C. Saykha, Ta-

Vagra, District: Bharuch, Gujarat

Screening & Scoping


Project status: New



EIA/EMP report.


SR. NO.

NAME OF PRODUCT CAS NO. PROPOSED CAPACITY MT/MONTH

END USE

A Beta Naphthol and its stream

1 G Salt 118-32-1 155.0 DYES & DYES INTERMEDIATES

-- --

2 Amido G Salt 86-65-7 127.0

3 K Acid 41016-61-9 50.0

4 Gamma Acid 90-51-7 50.0

5 R Salt ( 2 Naphthol 3:6 Di Sulphonic Acid )

135-51-3 10.0

6 Schaffers Acid 833-66-9 50.0

7 Beta naphthol 135-19-3 500.0

8 Broenner's Acid 93-00-5 25.0

9 J Acid 87-02-5 100.0

B Nitrobenzene Series

10 Metanilic Acid 121-47-1 100.0

11 Aniline 2:5 Di Sulpfonic Acid 98-44-2 50.0

12 Meta Amino Phenol 591-27-5 50.0

13 DE MAP 91-68-9 50.0

C Other Derivatives

14 Peri Acid 82-75-7 10.0

15 Phenyl Gamma Acid 5855-84-5 10.0

16 Sulpho J Acid ( 2,8 DiHydroxyNaphtahlene 6 Sulphonic Acid )

6535-70-2 10.0

17 F C Acid 74-79-3 30.0

18 Sulphanilic Acid 121-57-3 50.0 19 Aniline 2:4 Di Sulphonic Acid 137-51-9 15.0

20 Meta Uredio Aniline 59690-88-9 50.0

21 4 SulphoHydrazone 118969-29-2 10.0

22 5 SulphoHydrazone 10.0

23 4 Sulpho Anthranilic Acid 77734-52-2 20.0

24 5 Sulpho Anthranilic Acid 68645-45-4 20.0

25 PAABSA 104-23-4 20.0 26 Sulpho Tobias Acid 117-62-4 50.0

Page 70 of 92


Page 70 of 92

27 D Acid 94-75-7 20.0

28 Sulpho C Acid 132-87-6 10.0 29 Benzoyl J Acid 132-87-6 10.0

30 4,4 Di Amino Benzanilde 785-30-8 10.0

31 M Sulfo Phenyl Gamma J Acid 25251-42-7 10.0

32 MAMAS Acid 6300-07--08 10.0

33 1 Benzaidehyde Di Sulfonic Acid 88-39-1 10.0 34 1,8 Napthasaultan 470-82-6 10.0

35 2 pyridone 142-08-5 20.0

36 4 Carboxy Phenyl Gamma Acid 5855-84-5 10.0

37 Rhoduline Acid 87-3-6 10.0

38 4 NAP 99-57-0 20.0

39 N Methyl J Acid 22346-43-6 25.0

40 N Phenyl J Acid 119-40-4 25.0 41 H Acid 9067-32-7 100.0

42 VS 77-77-0 200.0

43 Acetanilide 103-84-4 133.0

44 MPDSA 88-63-1 25.0

45 Di Amino Benzoic Acid ( DABA ) 535-87-5 25.0

46 DASA 16803-97-7 50.0

47 PNA / ONA 100-01-06/88-74-4

50.0

48 OAVS 10079-20-6 15.0 49 Sulpho VS 42986-22-1 50.0

50 Sulpho OAVS 121-88-0 10.0

Total 2480.0




Sr.

no.

Particulars Details


(Rs. in Crores):

25.0 Crores

B Total Plot area( sq. meter) 33108.40 Sq. m.

Green belt area

( sq. meter)

10925.78 Sq. m.

C Employment generation

50

50

D Water

i



GIDC Water Supply


ii

Water consumption (KLD)

Category

Quantity

KLD

Remarks

(T) Domestic 26.0

(U) Gardening 26.0

Page 71 of 92


Page 71 of 92

(V) Industrial

Process 340.0

Washing 140.0

Boiler 96.0

Cooling 10.0

Others 7.0

Industrial Total

593.0

Total (A + B + C)

645.0

19) Total water requirement for the project: 645.0

20) Quantity to be recycled: 516.0


iii



KLD

Remarks

(M) Domestic 24.0

septic tank

(N) Industrial

Process 450.0

Washing 140.0

Boiler 10.0

Cooling 1.0

Others 7.0

reuse in

plant

premises or

send to end

users having

Rule-9

permission

Total Industrial 606.0 ETP, R.O,

Page 72 of 92


Page 72 of 92

waste water MEE plant

Total [A + B] 630.0

-



ETP : 66 KL/DAY

MEE : 560.0 KL/DAY with Spray dryer


Domestic: Septic Tank & Soak Pit system

Industrial:

In house ETP and MEE plant which is ultimately Zero Liquid

Discharge

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

, Name of CF

-

--




Page 73 of 92


Page 73 of 92


Total reuse 516.0

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.)

PH TDS COD BOD NH3-

N

MEE

Condensate

470.0 KLD 6.5-8.5 220.0 50.0 10.0 <50.0

R. O

Permeate

46.0

KL/Day

6.5-8.5 140.0 34.0 16.0 <50.0

E Air



KVA etc.

-

Sr. no.

Source of emission With Capacity


Type of Fuel




1 Steam Boiler (6 TPH* 2 nos)

30 coal 30 MT/day

PM<150 mg/Nm3

SO2<262mg/Nm3 NOx<92mg/Nm3

Multicyclone separator with Bag filter

2 Thermic Fluid Heater (TFH) 10,000 cal/hr)

30 coal

10 MT/day

PM<150 mg/Nm3

SO2<262 mg/Nm3 NOx<92 mg/Nm3

Multicyclone separator with Bag filter

3 D.G set1 (1250 KVA)

11 Diesel

0.2KL/Day

PM<150 mg/Nm3

SO2<262 mg/Nm3 NOx<92 mg/Nm3

Adequate Height will be provided

-


-

Page 74 of 92


Page 74 of 92

Sr. no.

Specific Source of emission (Name of

the Product & Process)

Type of emission



Measures (APCM)

1

Process vent-1

SO2<40.0 mg/Nm3

HCL<20.0 mg/Nm3

30 Alkali Scrubber

2

Process vent-2

NH3<175.0 mg/Nm3

30 Water Scrubber

3

Process vent-2

NOx<92 mg/Nm3

11 Alkali Scrubber

-


As below:

• Enclosed Processed

• Minimum joints/flanges

• Auto handling for charging Raw Materials

• Pumps with double mechanical seals

• Proper Ventilation

PPEs

F Hazardous wastes

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


i

SR. NO.

SOURCE TYPE OF HAZARDOUS WASTE

QUANTITY

HAZARDOUS WASTE CATEGORY

STORAGE, COLLECTION & DISPOSAL

1. From ETP ETP Sludge 28.0 MT/Month

Sch-I/35.3

Collection, Storage, Transportation & and Disposal to TSDF site

2. From Plant Machinery

Used Oil 0.05 MT/Month

Sch-I/5.1 Collection, Storage, Transportation &Sell to GPCB registered re-processor or used for low grade lubrication of

Page 75 of 92


Page 75 of 92

machinery.

3. From Raw material

Discarded Drum/Containers/Carboys Plastic bags/Liners

Bags: 40 MT./Month Drums: 15 MT/Month

Sch-I/33.3

Collection, Storage, Transportation, Decontamination & Sell to GPCB authorized Vendor.

4. From Mfg. process

Spent Solvent 420.0 MT/Month

Sch-I/26.4

Collection, Storage, and in-house solvent recovery plan.

5. From Solvent plan

Distillation residue 10 MT/Month

Sch-I/26.1

Collection, Storage, Transportation & co-processing in cement industries or sent to CHWIF site

6. From Mfg. process of Product no.10,14,17,41,44,46

Iron Sludge 821.0 MT/Month

Sch-I/26.1

Collection, Storage, Transportation & and Disposal to TSDF site

7. From Mfg.

process of

product

no.41,44

Process Sludge 126.0

MT/Mont

h

Sch-

I/26.1

Collection,

Storage,

Transportatio

n & and

Disposal to

TSDF site

8. From Mfg.

process of

product

no.1,2,4,42,45,4

8

Dil. Sulphuric acid 3676.0

MT/Mont

h

Sch-

I/26.3

Collection,

Storage,

Reuse in

Product no.

3,40,42

Required

192.0

MT/Month &

3484.0

MT/Month

Sell to End

users having

Page 76 of 92


Page 76 of 92

rule-9

permission

9. From Mfg.

process of

product no.

6,18,40,

Carbon Sludge 0.5

MT/Mont

h

Sch-

I/26.1

Collection,

Storage,

Transportatio

n & and

Disposal to

TSDF site

1

0

From Mfg.

process of

product no. 41

Gypsum Sludge 850.0

MT/Mont

h

Sch-

I/26.1

Collection,

Storage,

Transportatio

n & and

Disposal to

TSDF site

1

1

From Mfg.

process of

product no.14

Mgso4 80.0

MT/Mont

h

Sch-

I/26.1

Collection,

Storage,

Transportatio

n & Sell to

End users

having rule-9

permission.

1

2

From MEE plant MEE salt 100.0

MT/Mont

h

Sch-

I/35.3

Collection,

Storage,

Transportatio

n & and

Disposal to

TSDF site

1

3

From Scrubber Dil. HCL (30 %) 60.0

MT/Mont

h

SCH-II/

B15

Collection,

Storage,

Reuse in

Product no.

12,13,35,36

Required

223.5

MT/Month

1

4

From Scrubber Liq. Ammonia (25

%)

51.0

MT/Mont

h

Sch-

I/26.1

Collection,

Storage,

Reuse in

Product no.

08, Required

16.0

MT/Month &

35.0

MT/Month

Sell to End

users having

Page 77 of 92


Page 77 of 92

rule-9

permission

1

5

From Scrubber Sodium Sulphite

(20 %)

40.0

MT/Mont

h

SCH-II/

B15

Collection,

Storage,

Transportatio

n & Sell to

End users

having rule-9

permission.

1

6

From Scrubber Sodium Nitrite soln.

(15 %)

44.0

MT/Mont

h

SCH-II/

B15

Collection,

Storage,

Transportatio

n & Sell to

End users

having rule-9

permission.

-


(For HW management)

BEIL


(MSW and others)

NO



Solvents

Primary Condenser HE-01: Cooling Tower water or Chilled water will be used to

condense the solvents depend on the vapor pressure at its operating conditions and

the non condensed vapors will be condensed in a Secondary Condenser

Secondary Condenser HE-02: Chilled Brine at - 5 0C will be used to condense the

non condensed vapors in the Secondary Condenser

Final venting will be done after passing through carbon column.

• 96.7% of Spent solvent will be recovered


•

Vacuum Distillation

• Enclosed Processed


• Adequate Condenser

• Brine will be utilized as chilling agent



PPEs



• Committee noted that proposal is new in G.I.D.C. Saykha.Industrial effluent will be treated in ETP consists

of primary, secondary and tertiary treatment units followed by RO, MEE and spray dryer. RO permeate and

Page 78 of 92


Page 78 of 92

MEE condensate will be reused in process, washing and boiler feed. MEE concentrate will be fed to in

house spray dryer. Coal and diesel will be used as fuel. Muticyclone separator with bag filter will be

provided with TFH and boiler as APCM. Alkali scrubber and water scrubber will be provided as APCM with

process vents. PP has addressed hazardous waste management including bleed liquor.

• 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.








conservation.









7. Treatability & adequacy report for complete ZLD. Feasibility report for complete reuse of treated waste

water for industrial purpose.

8. Compliance of GPCB’s circular of dirty products.



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.



Page 79 of 92


Page 79 of 92

9 SIA/GJ/IND2/30596/2019 M/s. Shree Vardayini Chemical Industries Pvt. Ltd. Plot No. 3804 & 3803, G.I.D.C, Industrial Estate, Ankleshwar, Dist: Bharuch.

Screening & Scoping





EIA/EMP report.

• This is an exiting unit and now proposes for expansion as tabulated below:

Sr. No.

Name Of Products CAS No. Quantity (MT/Month)

End Use of the products Existing Proposed Total

1. PTS Chloride 98-59-9 9.3 93 102.3 Pharma Intermediate & Dye Intermediate

2. O/P Toluene Sulfonamine 88-19-7/ 70-55-3

1.8 18 19.8 Resin Raw material, Florescent Pigment

3. OTSA (Intermediate) 88-19-7 6.3 63 69.3 Pharma Intermediate & Saccharin Intermediate

4. Saccharin AND/OR 81-07-2 5

50 55

Pharma Intermediate

5. Sodium Saccharin (NaHCO3 Route)

128-44-9 --- Pharma Intermediate

6. Basic Chromium Sulfate 39380-78-4 75 375 450 Leather Tanning

7. Saccharin(Sodium Saccharin Route)

81-07-2 --- 50 50 Pharma Intermediate

8. Sodium Saccharin (KMnO4 Route)

128-44-9 --- 50 50 Pharma Intermediate

9. Methyl Paraben AND/OR 99-76-3 ---

25 25

Preservative

10. Propyl Paraben AND/OR 94-13-3 --- Preservative

11. Levosulpiride AND/OR 23672-07-3 --- Active Pharma Ingredient

12. Cilnidipine AND/OR 132203-70-4 --- Active Pharma Ingredient

13. Benfotiamine 22457-89-2 --- Active Pharma Ingredient

TOTAL 97.4 724 821.4 After Proposed expansion, Total Production capacity will be 821.4 MT/Month




Sr

.

n

o.

Particulars Details

Page 80 of 92


Page 80 of 92


(Rs. in Crores):

Existing: 4.00 Crores

Proposed: 1.75 Crores

Total: 5.75 Crores

B Total Plot area

( sq. meter)

Existing: 6055.56 Sq. m.

Proposed: 0 Sq. m.

Total: 6055.56 Sq. m.

Green belt area,/Tree Plantation area

( sq. meter)

Existing: 2039.05 Sq. m.

Proposed: 0 Sq. m.

Total: 2039.05 Sq. m.

C Employment generation Existing: 20 Nos.

Proposed: 40 Nos.

Total: 60 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.

ii Water consumption (KLD) (Pending)

Category Consumption, KL/day Remarks

Existing Proposed

(Additional)

Total after

Expansion

(A)Domestic 3.0 2.0 5.0

(B)Gardening 5.0 1.5 6.5

(C)Industrial

Process + Washing 6.5 82.0 88.5

Scrubber 0.5 6.0 6.5

Boiler 1.5 7.0 8.5

Cooling 2.0 5.0 7.0

Industrial Total 10.5 100.0 110.5

Total (A + B + C) 18.5 103.5 122 [Fresh 40 KLD+ Recycle 82 KLD]


23) Quantity to be recycle: 82 KLD

24) Total fresh water requirement: 40 KLD


Page 81 of 92


Page 81 of 92

Category Waste water Generation KL/day Remarks

Existing Proposed

(Additional)

Total after

Expansion

(A)Domestic 1.5 1.0 2.5

(B Industrial

Process +Washing 6.5 88.0 94.5

Scrubber 0.0 0.0 0.0

Boiler 0.0 2.0 2.0

Cooling 0.0 2.0 2.0

Other 0.0 0.0 0.0

Industrial Total 6.5 92.0 98.5

Total [A + B] 8.0 93.0 101.0

Note:

(1) Domestic: Domestic waste water will be disposed in to Septic tank/Soak pit. (2) Existing: Industrial effluent is being treated in to the primary treatment unit and after adequate

treatment of waste water is being sent to ETL-CETP for further treatment and disposal. (3) Proposed: 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.



� For Existing, Industrial effluent is being treated in to the primary treatment unit and after adequate treatment of waste water is being sent to ETL-CETP for further treatment and disposal.

� 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 and will be maintained ZLD.


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

Industrial: 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.

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


� We are existing member of ETL since long and membership certificate for the same is attached as

Annexure-II.

� ETL(Enviro Technology Limited)

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

� We are existing member of ETL since long and membership certificate for the same is attached as Annexure-II.


Page 82 of 92


Page 82 of 92


Total Reuse= 82 KLD

Source of waste water for reuse

with quantity in KLD


quantity in KLD

Remarks regarding feasibility to

reuse i.e. w/w characteristics

(COD, BOD, TDS etc.)

[1] MEE(Condensed Water)

[82 KL/Day]

In Process

[82 KL/Day]

pH 6-8

TDS (mg/lit) 300-500

TSS (mg/lit) 100-150

COD (mg/lit) 100-400

• Condensed water (82 KLD) will be recycle in process.

E Air



Existing & Proposed

Page 83 of 92


Page 83 of 92

Sr. no.

Source of emission With Capacity


Type of Fuel

Quantity of Fuel



Measures (APCM)

For Existing

1. Steamer Boiler [Cap. 600 Kg/hr]

11

Natural Gas

180 Nm3/ Day

PM < 150mg/Nm3 SO2< 100 ppm NOx< 50 ppm

Adequate Stack height

2. Tray Dryer [96 Tray] [Cap. 600 Kg/hr]

NG based direct fire

burner emissio

n via exhaust

20 Nm3/Day

3. FBD-1 [Cap. 120 Kg/hr]

20 Nm3/Day

4. FBD-2 [Cap. 120 Kg/hr]

20 Nm3/Day

5. Boiler [Cap. 1.5 TPH]

11 1300 Nm3/Day

6. Thermic Fluid Heater [Cap. 2 Lac Kcal]

11 100 Nm3/Day

7. D.G Set [320 KVA]

9 Diesel 150 lit/Day

For Proposed

1. Boiler [Cap. 1.5 TPH]

10 Natural

Gas 1300 m3/ day

PM < 150mg/Nm3 SO2< 100 ppm NOx< 50 ppm

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 Type of

emission



For Existing

1 Sulphonation /Amidation

Process (PTS Chloride/O/P Amide)

HCl≤20 mg/Nm3 15 Four stage Scrubber

For Proposed

1. Process Reactor HCl≤20 mg/Nm3 12 Water Scrubber


• Minimum Joints & flanges

• Pumps with mechanical seals

• Proper ventilation

• Adequate PPEs

Page 84 of 92


Page 84 of 92

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

Source of

Generation

Categor

y as per

HWM,

2016

Quantity MT/ Year Management of

HW Existing Propose

d

Total

1. Empty

barrels/contain

ers/liners

contaminated

with

hazardous

chemicals/was

tes

Raw Material

and Packaging

33.1 1200

Nos.

3000

Nos.

4200

Nos.

Collection,

Storage,

Decontamination,

transportation,

reuse or send

back to supplier,

and sold to

Authorized

Vendors.

2. Used Oil From Machinery 5.1 0.1 1.9 2.0 Collection, Storage, Transportation and sold to authorized Recyclers.

3. ETP Sludge

ETP 35.3 30 1770 1800 Collection,

Storage,

Transportation and

sent to TSDF site.

4. MEE Salt MEE 35.3 --- 1800 1800 Collection, Storage, Transportation and sent to TSDF site.

5. Process waste(Sludge)

Process (1)O/P Toluene Sulfonamine

26.1 10 101 111 Collection,

Storage,

Transportation and disposal at CHWIF-BEIL-Ankleshwar.

6. Spent Carbon

Process

(1)O/P Toluene

Sulfonamine

(2)Saccharin

(3)Sodium

Saccharin

(NaHCO3 Route)

36.2 2.5 25.5 28.0 Collection,

Storage,

Transportation and

disposal at

CHWIF-BEIL-

Ankleshwar.

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7. Dilute Sulfuric Acid

Process

(1)PTS Chloride

--- 525.6 5304 5829.6 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.

8. Hydrochloric Acid (Comm. Grade)

Process

(1)PTS Chloride

(2)O/P Toluene

Sulfonamine

--- 300 2995 3295 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.

9. Spent Chromic Acid

Process

(1)Saccharin

(2)Sodium

Saccharin

(NaHCO3 Route)

--- 1380 KL 6900 KL 8280 KL Collection, Storage, Captive consumption for the manufacturing of Basic Chromium Sulfate or sell to authorized end users registered under rule-9.

10. MnO2 Sludge Process

(1)Sodium

Saccharin

(KMnO4 Route)

--- --- 900 900 Collection, Storage, Transportation and and sell to authorized end users registered under rule-9.

ii Membership details of TSDF, CHWIF etc. We are existing member of ETL since long and membership certificate for the same is attached as Annexure-III.


(MSW and others)

Not Applicable



• Not Applicable



• Adequate Condenser

• Brine will be utilised as chilling agent



• PPEs



• Committee noted that unit has valid CC&A for existing unit. Unit is complying conditions of CC&A. PP informed

that there are no court cases pending and no public complaints against the project. After proposed expansion,

Page 86 of 92


Page 86 of 92

additional industrial effluent will be treated in ETP consists of primary treatment units followed by MEE. MEE

condensate will be reused for industrial purpose. PP ensured that there will be no increase in hydraulic and

organic load of effluent being discharged to CETP of ETL after propose expansion. Natural gas and diesel will

be used as fuel. Scrubber will be provided as APCM for process gas emission control. PP has addressed

hazardous waste management under the HWM Rules, 2016 including bleed liquor.












conservation.









7. 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.

8. Treatability & adequacy report for complete ZLD for additional waste water. Feasibility report for

complete reuse condensate waste water for industrial purpose.







10 SIA/GJ/IND2/29691/2018 M/s. Saprad Colourant Pvt Ltd

Plot No. C-298/2/2, Saykha GIDC,

Tal: Vagra; Dist: Bharuch.

Screening & Scoping


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10. SIA/GJ/IND2/29691/2018 M/s. Saprad Colourant Pvt Ltd

Plot No. C-298/2/2, Saykha GIDC,

Tal: Vagra; Dist: Bharuch.

Screening & Scoping


Project status: New



EIA/EMP report.


Sr. No.

Name of the Products CAS no. /CI no. Quantity MT/Month

End-use of products

1 Pigment Yellow 1 221491

35

Textile

Paints

Plastic

Inks

2 Pigment Yellow 3 6486-23-3




6 Pigment Red 8 6410-30-6

7 Pigment Red 12 6410-32-8

8 Pigment Red 23 6471-49-4

9 Pigment Red 31 6448-96-0

10 Pigment Red 48:2 7023-61-2

11 Pigment Red 210 61932-63-6

12 Pigment Orange 13 3520-72-7

13 Solvent Red 24 85-83-6

14 Solvent Yellow 2 60-11-7

15 Solvent Yellow 72 4645-07-2



• Salient features of the project are as under:

Sr.

no.

Particulars Details


(Rs. in Crores):

3.25

B Total Plot area ( sq. meter) 2441.12

Green belt area ( sq. meter) 813.50

C Employment generation 15

D Water

Page 88 of 92


Page 88 of 92

i



GIDC Water


Assurance letter is granted

for this project from GIDC.

ii

Water consumption (KLD)

Category

Quantity

KLD

Remarks

(Z) Domestic 1.50

(AA) Garden

ing

1.00

(BB) Industrial

Process 30.00

Washing 2.50

Boiler 1.60

Cooling --


Total (A + B + C) 36.60


29) Quantity to be recycled: --


iii



KLD

Remarks

(Q) Domestic 1.20 Septic tank / soak pit system.

(R) Industrial

Process 41.00 Wastewater is increase due

to ice consumption.

Washing 2.50

Boiler 0.20

Cooling --

Total Industrial

waste water

43.70 GIDC Drainage Line.

Total [A + B] 44.90

-



Sr.

No.

Particular Size (m) Volume

1 Collection cum

Neutralization Tank (2 Nos.)

4.0 x 4.0 x 3.5 56 m3

2 Filter Press 36” x 36” x 40 Nos. --

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Page 89 of 92

3 Aeration Tank 4.0 x 4.0 x 3.5 56 m3

4 Secondary Settling Tank 2.5 x 2.5 x 3.5 18.75 m3

5 Holding Tank 2.0 x 2.0 x 2.5 10 m3

6 Dual Media Filter 1.5 Ø x 1.5 ht --

7 Final Holding Tank 2.0 x 2.0 x 2.5 10 m3


Domestic: Septic Tank / Soak Pit system

Industrial: GIDC Drainage Line

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

, Name of CF

--



--


Nil

viii

Total reuse NIL KLD

Source of waste

water for reuse

with quantity in

KLD


quantity in KLD

Remarks

regarding

feasibility to

reuse i.e. w/w

characteristics

(COD, BOD,

TDS etc.)

-- -- --

E Air



KVA etc.

-

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

Industrial

Boiler

(0.8 TPH)

20 Agro

Waste

(Briquettes/

White coal)

70 kg/hr. PM

SO2

NOx

Bag Filter

2.

Hot Air

Generator

– 1

20 100

kg/hr Bag Filter

Page 90 of 92


Page 90 of 92

(1 U)

3.

Hot Air

Generator

– 2

(1 U)

100

kg/hr

4. D. G. Set

(20 kva) 8

High

Speed

Diesel

5 lit/hr --

-


-

Sr.

no.

Specific

Source of

emission

(Name of

the

Product &

Process)

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution

Control

Measures

(APCM)

None

-


As below:

None

F Hazardous wastes

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


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 Discarded

Drum/Containers

Raw

Material

Packaging

33.3

2.40

Reuse back

for refilling

finished

product or

Sold to

registered

recycler

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Page 91 of 92

Bags

1.20

Sold to

registered

recycler

2 ETP Sludge Effluent

Treatment

34.30 6.00 Collection.

Storage,

Transportatio

n, Disposal at

TSDF site.

3 Used Oil Machinerie

s

5.1 0.100 Collection.

Storage,

Transportatio

n, Disposal

by selling to

Registered

Recycler.

-


(For HW management)

None


(MSW and others)

Ash from White Coal

Sold to brick manufacturer

or disposal at TSDF site.



Solvents

Not Applicable


None



• Committee noted that this is new proposal in GIDC-Saykha. Industrial effluent will be treated in ETP consists of

primary and secondary treatment units. Treated effluent will be sent to CETP, Synkha for further treatment and

disposal. Agro waste/white coal and diesel will be used as fuel. Bag filter will be provided with Boiler and TFH.

There will be no process gas emission. PP has addressed hazardous waste management under the HWM

Rules, 2016.









Page 92 of 92


Page 92 of 92




conservation.













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


Meeting ended with thanks to the Chair.

Minutes approved by:

1. Dr. Dinesh Misra, Chairman, SEAC 2. Shri V. N. Patel, Member, SEAC

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

4 Shri A.K. Muley, Member, SEAC

5. Shri K. C. Mistry, Member Secretary, SEAC

Documents

Minutes of the 476 meeting of the State Level Expert ... Minutes of the 476th I.pdf · Page 2 of 92 476th meeting of SEAC-Gujarat, Dated 23.01.2019 Page 2 of 92 Sulpho Succinate (DOSS)