Minutes of the 387th 04/04/2018 at Committee … Minutes of the 387th.pdfPage 3 of 126 387 th meeting of SEAC-Gujarat, Dated 04.04.2018 Page 3 of 126 34 TariquidarAnalo g presently

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387thmeeting of SEAC-Gujarat, Dated 04.04.2018

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Minutes of the 387thmeeting of the StateLevelExpertAppraisalCommittee held on 04/04/2018 at Committee Room, GEER Foundation, Gandhinagar.

The 387thmeeting of the StateLevelExpertAppraisalCommittee (SEAC) was held on 04thApril 2018 at Committee Room, GEER foundation, Gandhinagar. Following members attended the meeting:

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

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

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

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

5. Dr. Mayuri Pandya, Member, SEAC

6. Shri Rajesh I Shah, Member, SEAC

The agenda of TOR/Scopingcases and Appraisal were 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/IND2/20669/2017 M/s. Mangalam Drugs & Organics Limited (Unit-II) Plot No. 1203, Phase-III, G.I.D.C Estate, Vapi-396 195, District: Valsad, Gujarat

Screening & Scoping

Project / Activity No.: 5(f)

Project status: Expansion

• This office has received an application vide their online proposal no. SIA/GJ/IND2/20669/2017

dated 12/10/2017regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP

report.

• This is an existing unit engaged in Synthetic Organic Chemicals and now proposes for

expansion as tabulated below:

Sr. no.

Name of the Products

CAS no.

Quantity MT/Month End-use of product

Existing Proposed Total

(A) BULK DRUGS

Group 1

1 Nimesulide 51803-78-2 31.0 49.0

80.0

Anti Inflammatory

2 Lumefantrine 82186-77-4 7.0 73.0 Antimalarial

3 Sulfadoxine 2447-57-6 - 80.0 Antimalarial

Group 2

4 Furosemide 54-31-9 5.0 25.0

30.0

Anti Inflammatory

5 HydroxyChloroquine Sulphate (HCQS)

747-36-4 3.0 27.0 Rheumatic arthritis

6 Allopurinol 315-30-0 5.0 25.0 Diuretic

7 Colesevelam Hydrochloride

182815-44-7 - 30.0 Diabetes

Group 3

8 AmodiaquineHy 6398-98-7 5.0 25.0 30.0 Antimalarial

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drochloride (AMQ HCl)

9 Piperaquine Phosphate

4085-31-8 5.0 25.0 Antimalarial

Group 4

10 TenofovirDisoproxilFumarate

202138-50-9 7.0 23.0 30.0

Antiretroviral

11 Efavirenz 154598-52-4 - 30.0 Antiretroviral

Group 5

12 Artemether 71963-77-4 2.0 18.0 20.0

Antimalarial

13 Artesunate 182824-33-5 2.0 18.0 Antimalarial

Group 6

14 Emtricitabine 143491-57-0 1.0 9.0

10.0

Antiretroviral

15 Pyrimethamine 58-14-0 - 10.0 Antiretroviral

16 Dihydroartemisinin

81496-81-3 - 10.0

Antimalarial

17 Bisoprolol Fumarate

104344-23-2 - 10.0

Heart Disease

Group 7

18 Pyronaridine 76748-86-2 0.5 4.5

5.0

Antimalarial

19 AtazanavirSulfate

229975-97-7 - 5.0

Antiretroviral

20 Primaquine Phosphate

63-45-6 - 5.0

Antimalarial

21 Chloroquine Phosphate (CQP)

50-63-5 2.0 3.0

Antimalarial

Group 8

22 TenofovirAlafenamideFumarate

1392275-56-7 - 10.0

10.0

Antiretroviral

23 TenofovirDisoproxilOrotate

202138-50-9 - 10.0

Antiretroviral

24 Sofosbuvir 1190307-88-0 - 10.0 Antiretroviral

Group 9

25 Dolutegravir Sodium

1051375-19-9 - 5.0

5.0

Antiretroviral

26 Velpatasvir 1377049-84-7 - 5.0 Antiretroviral

27 AdefovirDipivoxilFumarate

presently N/A - 5.0

Antiretroviral

28 Ledipasvir 1256388-51-8 - 5.0 Antiretroviral

29 DaclatasvirDihydrochloride

1009119-65-6 - 5.0

Antiretroviral

30 Tafenoquine Succinate

106635-81-8

- 5.0 Antimalarial

Group 10

31 Ursodiol 128-13-2 - 5.0

5.0

To treat a certain type of liver disease

32 Terizidone 25683-71-0 - 5.0 -

33 Delamanid presently N/A

- 5.0 Used to improve urination in men with benign prostatic hyperplasia.

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34 TariquidarAnalog

presently N/A - 5.0

-

35 Solifenacin Succinate

242478-38-2

- 5.0 To treat the symptoms of overactive bladder such as incontinence, urinary frequency

36 Montelukast Sodium

151767-02-1 - 5.0

-

37 Silodosin 160970-54-7

- 5.0 Used to improve urination in men with benign prostatic hyperplasia.

38 Cinacalcet Hydrochloride

364782-34-3

- 5.0 To treat increased amounts of a certain hormone in people with long-term kidney disease who are on dialysis

39 Maraviroc 376348-65-1 - 5.0 Anti retroviral activity

40 Vilazodone Hydrochloride

163521-08-2 - 5.0

To treat depression

41 Metoprolol succinate

98418-47-4

- 5.0 To treat angina (chest pain) and hypertension. To treat or prevent heart attack.

(B) BULK DRUGS INTERMEDIATES

1. Meta Chloro Aniline (MCA)

108-42-9 - 6.0 6.0

Intermediates for the manufacturing of different bulk drugs

2. 2,7-Dichloro-9H-fluorene (DCF)

7012-16-0 30.0 -15.0 15.0

3. 2-(2,7-dichloro-9H-fluoren-4-yl)oxirane

53221-14-0

- 15.0 15.0

4.

[2-Dibutylamino-1-(2-7-dichloro-9H-florine-4-yl)] ethanol(DBA)

69759-61-1 30.0 -10.0 20.0

5. Dihydroartemisinin (DHA)

71939-50-9 2.0 13.0 15.0

6. 4-cyanoethyl-2-methyl-phenol (MHPN)

presently N/A 5.0 - 5.0

7.

(R)-9-(2-phosphonylmethoxypropyl)-adenine (PMPA)

147127-20-6 10.0 15.0 25.0

8. 4,7-Di ChloroQuinoline (4,7-DCQ)

86-98-6 12.0 8.0 20.0

9. N-(2-phenoxyphenyl)

51765-51-6 46.0 4.0 50.0

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-methanesuphonamide (OPMSA)

10. Meta Amino Acetanilide (MAA)

102-28-3 4.0 1.0 5.0

11.

N-{3-[(diethylamino)methyl]-4-hydroxyphenyl}acetamide(Mannich Base)

121-78-8 - 20.0 20.0

12. 4,6-dichloro-5-methoxypyrimidine

5018-38-2 - 25.0 25.0

13.

L-Menthyl-5-(2R,5S)-[4-amino-5-fluoro-2-oxopyrimidin-1(2H)-yl]-1,3-oxathiolane-2-carboxylate (FCME)

764659-72-5 - 40.0 40.0

14.

(S)-2-(2-amino-5-chlorophenyl)-4-cyclopropyl-1,1,1-trifluorobut-3-yn-2-ol (E-6)

209414-27-7 - 24.0 24.0

15. TenofovirDisoproxil Free Base (TD Base)

202138-50-9 - 10.0 10.0

Products to be discontinued

1 Meta Nitro Aniline

99-09-2 4 -4 0


2 Meta Amino Propionilide

22987-10-6 4 -4 0

3 2,4,5, Trichloro Aniline

636-30-6 4 -4 0

4 LF-2 ASCF - 30 -30 0

5 Ortho Phenoxy Aniline OPA

2688-84-8 25 -25 0

6 Arteether 75887-54-6 0.5 -0.5 0 Anti-malarial

7 Losartan Potassium

124750-99-8 7 -7 0

Use for Hart dieses

8 Acetazolamide 59-66-5

2 -2 0

Anti-sickness

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

2006.

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• PP was called for presentation in the SEAC meeting dated 04/04/2018.

• During the meeting dated 04/04/2018, technical presentation made during the meeting by

project proponent.

• Salient features of the project are as under:

Sr. No.

Particulars Details

A Total cost of Proposed Project

(Rs. In Crores):

Existing: 47 Proposed: 1 Total: 48

B Total Plot area ( sq. meter)

Existing: 10,000 Sq. m. Proposed: 0 Sq. m. Total: 10,000 Sq. m.

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

Existing: 900 Sq. m. Proposed: 2,500 Sq. m. (outside unit) Total:3,400 Sq. m.

C Employment generation Existing: 350 Proposed: 22 Total: 372

D Water

i

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

Vapi, G.I.D.C

Status of permission from the concern authority.

Unit has water permission letter for existing unit. Permission for additional water requirement is under process.

Ii Water consumption (KLD)

-

Category Existing KLD

Proposed (Additional)

KLD

Total after Expansion

KLD Remarks

(A) Domestic 25 0 25 -

(B) Gardening 20 0 20 -

(C) Industrial

Process 37 59 96 -

Washing 24 0 24 -

Boiler 10 0 10

Earlier very less condensate quantity was utilized now we are going to collect maximum condensate and access available steam will be utilised.

Cooling 20 0 20 -

Others (R&D and Pilot)

15 -10 5 -

(C) Industrial Total 106 49 155 -

Grand Total (A+B+C)

151 49 200 -

1) Total water requirement for the project:200 KLD

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2) Quantity to be recycle:30 KLD

3) Total fresh water requirement: 170 KLD

iii Waste water generation (KLD)

-

Category Existing KLD Proposed

(Additional) KLD

Total after Expansion KLD

Remarks


(C) Industrial

Process 38.5 42 80.5 -

Washing 15 0 15 -

Boiler 2 0 2 -

Cooling 4 0 4 -

Others (R&D and Pilot + Unit-I))

16.5 -14.5 2 Effluent will not be received from unit-I.

(C) Total Industrial waste water

76 27.5 103.5 -

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

ETP: 125 KLD consisting Primary, Secondary and Tertiary treatment, MEE and RO

V Mode of Disposal & Final meeting point

Domestic: To ETP for treatment

Industrial: Existing load to CETP after treatment in ETP and additional load will be Reused/Recycled

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

CETP: Vapi Green Enviro Limited CHWIF: BEIL

Membership of CF Unit has obtained CETP membership for existing load Membership of BEIL is also obtained.

Vii Reuse/Recycle details (KLD) 30 KLD

E Air[Existing & Proposed]

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 Pollutants

Air Pollution Control

Measures (APCM)

1 IBR

Boiler (2 TPH x 1 No.) 30

Natural Gas

2580m3/Day

PM SO2 NO2

adequate stack height is provided

2 Non IBR Boiler

&Thermopack no. 1 (4 Lac kcal)*

15

3 Thermo pack no. 2

(2 Lac Kcal) 15

4 DG Set (320 kVA x 1

No.) 11 Diesel 60 Lit/hr

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5 DG Set (75 kVA x 1

No.)* 11 Diesel 20 Lit/hr

Proposed

1 Gas Generator

(1.0 MW) 15

Natural Gas

5000 m3/Day

PM SO2 NO2

adequate stack height will be provided

* Existing Non IBR Boiler,Thermopack no. 1 and D.G.Set (75 KVA) will be removed

-

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

Stack/Vent

Height (meter)

Air Pollution Control Measures

(APCM)

Existing

1 Reaction vessel

Cl2 HCl

11 water scrubber and

Alkali Scrubber

2 Incinerator PM SO2 NO2

30 Venturay Scrubber

Proposed

No process gas generation form proposed expansion

-

iii Fugitive emission details with its mitigation measures. [Existing & Proposed]KAs below:

The fugitive emissions of organic chemicals and VOCs mainly occur due to tank breathing losses, Leaking pipe fitting and valves, during maintenance operations. Though these are not expected to be significant, the following measures are being followed to ensure compliance and further reductions wherever possible, the same will be continued after expansion.

• The fugitive emissions in terms of handling losses are reduced by proper storage and handling.

• Hazardous chemicals are stored as per standard criteria.

• Proper ventilation in storage & production area is provided and all materials are being stored in suitable packing to prevent contamination of air due to particulates & volatile emissions from storage container & area.

• Enclosed system & efficient procedures for materials charging is provided.

• SOP’s for start-up, shut down, operation & maintenance are established & maintained in all relevant area of works.

• The coverage of greenbelt around the plant consisting of noise and air pollution capturing species also acts as natural barrier to stop carrying of dust along with the wind current.

• Good housekeeping is maintained in the plant.

• Work area monitoring is carried out twice in a year as per GFR.

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

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i

Sr. No.

Type/Name of Hazardous waste

Source of generation

Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Disposal Method

Existing

Proposed

Total

1 ETP Waste Effluent

Treatment Plant

34.2 27.6 322.4 350 Collection, storage, Transportation, disposal at TSDF – VWEMCL

2 Distillation Residue

Solvent Recovery

Plant 20.3 112.49 1088 1200

Collection, storage and disposed in Captive incinerator (capacity 200 kg/hr)/Sent to RSPL / cement industry for co-processing

3 Process Residue

Process 28.1 146 354 500

4 Used Oil Plant

machinery 5.1 0.0925 0.0276 0.12

Collection, storage and reuse as lubricants in the machineries within the premises only or send to authorized reprocessors.

5 Discarded Container/

Bags

Raw Material storage

33.1 21 26.2 47.2 Collection, storage and send to authorized recycler after decontamination.

6 Iron

Sludge

From manu. of

Ortho Phenoxy Aniline

28.1 840 -840 0 --

7 Used/ Waste filter clothes

- 35.1 0.06 0.09 0.15 Collection, storage, Transportation, disposal at TSDF

8 Sludge from wet Scrubber

APCM Device

35.1 0.024 0.096 0.12 Collection, storage, Transportation, disposal at TSDF

9 Spent

Carbon Process 28.3 78 222 300

Collection, storage and disposed in captive incinerator (capacity 200 kg/hr)/ CHWIF/sent to cement industries for co-processing

10 Salt from Evaporator

MEE 37.3 672 228 900 Collection, storage, Transportation, disposal at TSDF

11 Tri SodiumPhosphate

From manu. of

4,7-Di ChloroQui

noline

28.1 180 120 300 Collection, storage, Transportation, disposal at TSDF

12 Incineration Ash

Incinerator 37.2 30 30 60 Collection, storage, Transportation, disposal at TSDF

13 Spent solvent

From process

28.6 7000 15000 22000

Inhouse Distillation and

recovered solvents will be

reused

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12. Eutectic Oil From Manu. Of

Meta Chloro Aniline (MCA)

- 0 6.0 6.0

Sell to end user 13.

Sodium Thio Sulphate

- 0 6.0 6.0

14. Hydrochloric Acid

- 0 10.0 10.0

Waste received from M/s. Mangalam Drugs & Organics Limited [Unit-I]

15. Distillation Residue

Solvent Recovery

Plant 20.3 43.2 1156.8 1200 Reception from [Unit-I]

through manifest system, storage, Incineration at captive Incinerator(capacity 200 kg/hr) within premises/ sent to cement industries for co-processing

16. Process residue

Process 28.1 6 494 500

17. Spent carbon

Process 28.3 78 222 300

18. Used oil Plant

machinery 5.1 0.06 0.06 0.12

ii Membership details of TSDF, CHWIF etc. • Membership Certificate No. of CETP & TSDF of Vapi Green Enviro Limited is 245 dated 3rd May, 2016.

• BEIL Membership obtained for incineration

• Membership Certificate of RSPL is obtained

• MOU with Cement Industry (Ambuja cement)

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

N.A.

G Solvent management, VOC emissions etc.

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

Plant onsite solvent recovery system with 97% recovery and distillation residues are sent to Captive incinerator /Sent to RSPL / cement industry for co-processing.

ii VOC emission sources and its mitigation measures

VOC emissions results from uses of solvents. This emission takes place only at storage and handling of solvent.

• Technical presentation was made by the project proponent. Committee deliberated on compliance

of the existing project. Earlier PP has obtained EC from MoEF&CC. Committee asked PP to submit

Certified Compliance Report [CCR] with EIA report. While discussing about the waste water

management, Committee observed that entire quantity of effluent will be discharged to CETP, Vapi.

Looking to the direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution)

act, 1974 issued by CPCB regarding compliance of CETP, Committee asked to go for ZLD for

additional waste water generation. PP agreed upon and informed that they will achieve ZLD for

additional waste water by means of in-house MEE.Committee also deliberated on Hazardous waste

management and asked PP to explore the possibilities to send incinerable waste for co-processing

instead of sending to CHWIF.

• 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

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covering 10 Km radial distance from the project boundary.

1. Treatment and disposal of additional waste water in line with prevailing direction of CPCB

under section 18(1) (b) of the Water Act 1974.

2. Adequacy of ZLD for additional waste water generation.

3. Certified Compliance Report (CCR) from the concern authority as per the MoEFCC’s

Circular no. J-11011/618/2010- IA (II) (I) dated 30/05/2012 and Circular no. J-11013/6/2010-

IA-II (Part) vide dated 07/09/2017.

• 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.

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

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

2. SIA/GJ/IND2/20660/2017 M/s. Mangalam Drugs & Organics Ltd. (Unit-I) Plot No. 187, Phase-II, G.I.D.C Estate, Vapi-396 195, District: Valsad, Gujarat

Screening & Scoping





report.



Sr. no.


CAS no. Quantity

MT/Month End-use of product


(A) AROMATIC CHEMICALS

1. Phenyl Ethyl Methyl Ether

3558-60-9 9.0 - 9.0

Perfumery

2. Phenyl Ethyl Chloride

622-24-2 3.0 - 3.0

Perfumery

(B) BULK DRUGS

Group 1

1 Nimesulide 51803-78-2 17.0 63

80

Anti Inflammatory

2 Lumefantrine 82186-77-4 18.0 62 Antimalarial

3 Sulfadoxine 2447-57-6 - 80 Antimalarial

Group 2

4 Furosemide 54-31-9 5.0 25

30

Anti Inflammatory

5 HydroxyChloroquine Sulphate (HCQS)

747-36-4 3.0 27 Rheumatic arthritis

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6 Allopurinol 315-30-0 5.0 25 Diuretic

7 Colesevelam Hydrochloride

182815-44-7 - 30 Diabetes

Group 3

8 Amodiaquine Hydrochloride (AMQ HCl)

6398-98-7 9.0 21 30

Antimalarial

9 Piperaquine Phosphate

4085-31-8 5.0 25

Antimalarial

Group 4

10 TenofovirDisoproxilFumarate

202138-50-9 7.0 23 30

Antiretroviral

11 Efavirenz 154598-52-4 - 30 Antiretroviral

Group 5

12 Artemether 71963-77-4 2.0 18 20

Antimalarial

13 Artesunate 182824-33-5 2.0 18 Antimalarial

Group 6

14 Emtricitabine 143491-57-0 1.0 9

10

Antiretroviral

15 Pyrimethamine 58-14-0 - 10 Antiretroviral

16 Dihydroartemisinin

81496-81-3 - 10

Antimalarial

17 Bisoprolol Fumarate

104344-23-2 - 10

Heart Disease

Group 7

18 Pyronaridine 76748-86-2 0.5 4.5

5

Antimalarial

19 Atazanavir Sulfate

229975-97-7 - 5

Antiretroviral

20 Primaquine Phosphate

63-45-6 - 5

Antimalarial

21 Chloroquine Phosphate (CQP)

50-63-5 2.0 3

Antimalarial

Group 8

22 TenofovirAlafenamideFumarate

1392275-56-7 - 10

10

Antiretroviral

23 TenofovirDisoproxilOrotate

202138-50-9 - 10

Antiretroviral

24 Sofosbuvir 1190307-88-0 - 10 Antiretroviral

Group 9

25 Dolutegravir Sodium

1051375-19-9 - 5

5

Antiretroviral

26 Velpatasvir 1377049-84-7 - 5 Antiretroviral

27 AdefovirDipivoxilFumarate

presently N/A - 5

Antiretroviral

28 Ledipasvir 1256388-51-8 - 5 Antiretroviral

29 DaclatasvirDihydrochloride

1009119-65-6 - 5

Antiretroviral

30 TafenoquineSuccinate

106635-81-8

- 5

Antimalarial

Group 10

31 Ursodiol 128-13-2 - 5

5 To treat a certain type of liver disease

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32 Terizidone 25683-71-0 - 5 -

33 Delamanid presently N/A

- 5 Used to improve urination in men with benign prostatic hyperplasia.

34 Tariquidar Analog

presently N/A - 5

-

35 Solifenacin Succinate

242478-38-2

- 5 To treat the symptoms of overactive bladder such as incontinence, urinary frequency

36 Montelukast Sodium

151767-02-1 - 5

-

37 Silodosin 160970-54-7

- 5 Used to improve urination in men with benign prostatic hyperplasia.

38 Cinacalcet Hydrochloride

364782-34-3

- 5 To treat increased amounts of a certain hormone in people with long-term kidney disease who are on dialysis

39 Maraviroc 376348-65-1 - 5 Anti retroviral activity

40 Vilazodone Hydrochloride

163521-08-2 - 5

To treat depression

41 Metoprolol succinate

98418-47-4

- 5 To treat angina (chest pain) and hypertension. To treat or prevent heart attack.

(C) BULK DRUGS INTERMEDIATES

1. Meta Chloro Aniline (MCA)

108-42-9 6.0 - 6.0


2. 2,7-Dichloro-9H-fluorene (DCF)

7012-16-0 8.0 7.0 15.0

3. 2-(2,7-dichloro-9H-fluoren-4-yl)oxirane

53221-14-0

- 15.0 15.0

4.

[2-Dibutylamino-1-(2-7-dichloro-9H-florine-4-yl)] ethanol(DBA)

69759-61-1 8.0 12.0 20.0

5. Dihydroartemisinin (DHA)

71939-50-9 5.0 10.0 15.0

6. 4-cyanoethyl-2-methyl-phenol (MHPN)

presently N/A - 5.0 5.0

7.

(R)-9-(2-phosphonylmethoxypropyl)-adenine (PMPA)

147127-20-6 - 25.0 25.0

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8. 4,7-Di ChloroQuinoline (4,7-DCQ)

86-98-6 - 20.0 20

9.

N-(2-phenoxyphenyl)-methanesuphonamide (OPMSA)

51765-51-6 - 50.0 50

10. Meta Amino Acetanilide (MAA)

102-28-3 - 5.0 5

11.

N-{3-[(diethylamino)methyl]-4-hydroxyphenyl}acetamide (Mannich Base)

121-78-8 - 20.0 20.0

12. 4,6-dichloro-5-methoxypyrimidine

5018-38-2 - 25.0 25.0

13.

L-Menthyl-5-(2R,5S)-[4-amino-5-fluoro-2-oxopyrimidin-1(2H)-yl]-1,3-oxathiolane-2-carboxylate (FCME)

764659-72-5 - 40.0 40.0

14.

(S)-2-(2-amino-5-chlorophenyl)-4-cyclopropyl-1,1,1-trifluorobut-3-yn-2-ol (E-6)

209414-27-7 - 24.0 24.0

15. TenofovirDisoproxil Free Base (TD Base)

202138-50-9 - 10.0 10.0

Products to be discontinued

1. Lopinavire 192725-17-0

1 -1 0 Anti-HIV

2. Praziquintal 55268-74-1

2 -2 0 Anti-worm

3. Ritonavir 155213-67-5

1 -1 0 Anti HIV

4. CiprotloxacinHydrochloride

93107-08-5 5 -5 0 Antibiotics

5.

M-1 &/Or M-2 &/Or M-3 &/Or M-4 &/Or M-5 &/Or M-6 &/Or M-7 &/Or M-13

- 50 -50 0 Intermediates for the manufacturing of different bulk drugs

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&/Or M-15 M-21 &/Or M-23 &/Or M-25

6.

2(2-chloro-1-(2,7-dichloro-9H Fluorene-4-yl)ethanol (LF2)

131023-37-5 8 -8 0 Intermediates for the manufacturing of different bulk drugs

• The project falls under Category B of project activity 1(d) as per the schedule of EIA Notification

2006.



project proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 57 Proposed: 1 Total: 58


Existing:8737.82Sq. m. Proposed:0 Sq. m. Total:8737.82Sq. m.


Existing: 1050 sq.m. Proposed: -2500sq.m. (outside unit) Total: 1050 sq.m.


D Water

i


Vapi, G.I.D.C


Unit has water permission letter for existing unit. Permission for additional water requirement is under process.

ii

Water consumption (KLD)

Existing Proposed Total after Remarks

Page 15 of 126


Page 15 of 126

KLD (Additional) KLD

Expansion KLD


(B) Gardening 20 0 20 -

Industrial

Process 18 78 96 -

Washing 13 16 29 -

Boiler

10 0 10

Earlier very less condensate quantity was utilized now we are going to collect maximum condensate and access available steam will be utilised.

Cooling 20 0 20 -

Others 3 -3 0 -

Industrial Total 64 91 155 -

Grand Total (A+B+C)

101 99 200 -

4) Total water requirement for the project:200 KLD

5) Quantity to be recycle:70 KLD

6) Total fresh water requirement: 130KLD

iii

Waste water generation (KLD)

Category Existing KLD Proposed

(Additional) KLD


KLD

Remarks


(C) Industrial

Process 18 62.5 80.5 -

Washing 13 12 25 -

Boiler 4 0 4 -

Cooling 7 0 7 -

Others 3 -3 0 -

(C) Total Industrial

waste water 45 71.5 116.5 -

-

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

ETP: 135 KL/d having primary, secondary and tertiary treatment, MEE and RO.

v Mode of Disposal & Final meeting point

Domestic: To ETP for treatment

Industrial: Existing load to CETP after treatment in ETP and additional load will be

Page 16 of 126


Page 16 of 126

Reused/Recycled.


CETP: Vapi Green Enviro Limited

Membership of CF

Unit has obtained CETP membership for existing load

vii Reuse/Recycle details (KLD)

70 KLD


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


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 IBR

Boiler (2 TPH x 1 No.)

30 Natural

Gas 193 m3/hr

PM SO2 NO2

adequate stack

height is provided

2 Non IBR Boiler standby facility*

15

3 DG Set

(320 kVA x 1 No.) 11 Diesel 70 Lit/hr

4 Thermic Fluid

Heater* (4 Lac K cal)

15 Diesel 600

Lit/day

Proposed

1 Gas Generator

(1.2 MW) 15

Natural Gas

5200 m3/Day

PM SO2 NO2

adequate stack

height will be provided

* Existing Non IBR Boiler and TFH will be removed

-


-

Sr. no.

Source of emission

Type of emission

Stack/Vent Height (meter)

Air Pollution Control Measures (APCM)

Existing

1 Chlorinator in Meta Chloro Aniline Plant

Cl2

HCl

11 A glass line water

scrubber followed by ventury caustic scrubber

Proposed

No process gas generation form proposed expansion

-

iii Fugitive emission details with its mitigation measures.

Page 17 of 126


Page 17 of 126

[Existing & Proposed]KAs below:

The fugitive emissions of organic chemicals and VOCs mainly occur due to tank breathing losses, Leaking pipe fitting and valves, during maintenance operations. Though these are not expected to be significant, the following measures are being followed to ensure compliance and further reductions wherever possible, the same will be continued after expansion.

• The fugitive emissions in terms of handling losses are reduced by proper storage and handling.

• Hazardous chemicals are stored as per standard criteria.

• Proper ventilation in storage & production area is provided and all materials are being stored in suitable packing to prevent contamination of air due to particulates & volatile emissions from storage container & area.

• Enclosed system & efficient procedures for materials charging is provided.

• SOP’s for start-up, shut down, operation & maintenance are established & maintained in all relevant area of works.

• The coverage of greenbelt around the plant consisting of noise and air pollution capturing species also acts as natural barrier to stop carrying of dust along with the wind current.

• Good housekeeping is maintained in the plant.

• Work area monitoring is carried out twice in a year as per GFR.


i -

Sr. no.




Quantity (MT/Annum)

Disposal Method


1 ETP Waste Effluent

Treatment Plant

34.2 72 228 350

Collection, storage, Transportation, disposal at TSDF -VWEMCL

2 Distillation Residue

Solvent Recovery

Plant 20.3 43.2 1156.8 1200

Collection, storage and disposed in incinerator (200 kg/hr) at Unit-II/Sent to RSPL / cement industry for co-processing

3 Process Residue

Process 28.1 6 494 500

4 Used Oil Plant

machinery 5.1 0.06 0.06 0.12

Collection, storage and reuse as lubricants in the machineries within the premises only or send to authorized re-processors.

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Page 18 of 126

5 Discarded Container/

Bags

Raw Material storage

33.1 21 26.2 47.2

Collection, storage

and send to

authorized recycler

after

decontamination

6 Iron Sludge Process 28.1 1800 -1800 0 -

7 Used/ Waste filter clothes

- 35.1 0.05 0.10 0.15

Collection, storage,

Transportation,

disposal at TSDF

8 Sludge from wet Scrubber

APCM Device

35.1 0.024 0.096 0.12


Transportation,

disposal at TSDF

9 Spent Carbon

Process 28.3 78 222 300

Collection, storage and disposed in incinerator (200 kg/hr) at Unit-II or for co- processing at cement industry

10 Salt from Evaporator

MEE 37.3 0 650 650


Transportation,

disposal at TSDF

11 Spent Solvent

Process 28.6 6,000 18,000 22,000

Inhouse Distillation

and recovered

solvents will be

reused

12. Eutectic Oil From Manu. Of

Meta Chloro Aniline (MCA)

- 6.0 - 6.0

Sell to end users 13.

Sodium Thio Sulphate

- 6.0 - 6.0

14. Hydrochloric Acid

- 10.0 - 10.0

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

ii Membership details of TSDF, CHWIF etc.

• Membership Certificate No. of CETP & TSDF of Vapi Green Enviro Limited is 244 dated 3rd May, 2016.

• Membership Certificate of RSPL is obtained

• MOU with Cement Industry (Ambuja cement)


N.A.



Plant onsite solvent recovery system with 97% recovery and

Page 19 of 126


Page 19 of 126

distillation residues are sent to Captive incinerator /Sent to RSPL / cement industry for co-processing.

ii VOC emission sources and its mitigation measures VOC emissions results from uses of solvents. This emission takes place only at storage and handling of solvent.

• Technical presentation was made by the project proponent. Committee deliberated on compliance

of the existing project. Earlier PP has obtained EC from MoEF&CC. Committee asked PP to submit

Certified Compliance Report [CCR] with EIA report. While discussing about the waste water

management, Committee observed that entire quantity of effluent will be discharged to CETP, Vapi.

Looking to the direction under section 18 (1) (b) of the Water (Prevention and Control of Pollution)

act, 1974 issued by CPCB regarding compliance of CETP, Committee asked to go for ZLD for

additional waste water generation. PP agreed upon and informed that they will achieve ZLD for

additional waste water by means of in-house MEE. Committee also deliberated on Hazardous

waste management and asked PP to explore the possibilities to send incinerable waste for co-

processing instead of sending to CHWIF.






1. Treatment and disposal of additional waste water in line with prevailing direction of

CPCB under section 18(1) (b) of the Water Act 1974.

2. Adequacy of ZLD for additional waste water generation.

3. Certified Compliance Report (CCR) from the concern authority as per the MoEFCC’s

Circular no. J-11011/618/2010- IA (II) (I) dated 30/05/2012 and Circular no. J-

11013/6/2010-IA-II (Part) vide dated 07/09/2017.





2006.



3. SIA/GJ/IND2/21605/2018

M/s. Subhasri Pigments Pvt Ltd PLOT NO:-J/1207, GIDC ESTATE, ANKLESHWAR, DIST:-BHARUCH

Screening & Scoping

Page 20 of 126


Page 20 of 126


Project status: Existing unit



report.



Sr. no.


CAS no. / CI no.

Quantity (MT/Month) End-use of the products


1 CPC Green-7

1328-53-6 0 100 100 Ink, Coatings, Plastics & Paints, Cosmetic, Printing ink and Packaging Industry.

2 Sodium Nitrite

-- 15 -15 0 --

3 Sodium Nitrate

-- 5 -5 0 --

4 Molybidate -- 3 -3 0 --

5 Tungustate Salt

-- 2 -2 0 --

6 Sodium acetate

-- 10 -10 0 --

7 Sodium format

-- 10 -10 0 --

Note: Existing products will be removed.


2006.



project proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

Existing:0.375 Proposed:13.45 Total:13.825


Existing: - 605.13 Sq. m. Proposed: ----Sq. m. Total: 605.13 Sq. m.


Existing: ----Sq. m. Proposed: 100.Sq. m.

Page 21 of 126


Page 21 of 126

Total: 100 Sq. m.

C Employment generation Existing:00 Proposed:20 Total:20

D Water i


GIDC Water


GIDC has given permission for it.

ii


Existing KLD

Proposed (Additional) KLD


Remarks

(C) Domestic 1 9 10 GIDC Water is a source of water.

(D) Gardening

-- 5 5 GIDC Water is a source of water.

Industrial

Process -- 74.5 74.5 Total 159 KLD water will be required.56.5 KLD will be a GIDC fresh water,18 KLD from steam to parent industry M/s. Subhasri Pigments Pvt Ltdat Plot No:- J-1201+1202+1211+1213+1208+1209+1209/A, GIDC Industrial Estate, Ankleshwar,73.5 KLD internal recycle and 11KLD from RO Permeate.

Washing -- -- -- --

Boiler -- -- -- Unit will take required 18 KLD stream from parent industry industry M/s. Subhasri Pigments Pvt Ltdat Plot No:- J-1201+1202+1211+1213+1208+1209+1209/A, GIDC Industrial Estate, Ankleshwar

Cooling -- -- -- 25 KLD RO permeate water will be used for this purpose.

Others ---- ---- ---- ----

Industrial Total 1 74.5 74.5

Grand Total (A+B+C)

1 88.5 89.5

Page 22 of 126


Page 22 of 126

1) Total water requirement for the project: 199KLD

2) Quantity to be recycle: 109.5KLD

3) Total fresh water requirement: 89.5 KLD

• Note :- Total water consumption will be 199 KLD. Fresh water requirement will be 71.5 KLD. GIDC water will be a source of fresh water. 73.5 KLD will be a internal recycle water. Unit will use 36 KLD RO-Permeate water. Total 18 KLD steam will be required for distillation purpose. Unit will take this steam from parent industry M/s. SUBHASRI PIGMENTS PVT LTD located at Plot No:- J-1201+1202+1211+1213+1208+1209+1209/A, GIDC Industrial Estate, Ankleshwar-in the vicinity of the unit.

iii





Remarks

(A) Domestic 0.8 9.2 10 10 KLD effluent will be subjected to RO after primary & tertiary treatment.

Industrial

Process - 117.5 117.5 73.5 KLD water will be internally reused by the unit. Remaining 44 KLD effluent will be subjected to RO after primary& tertiary treatment.

Washing - -- --

Boiler - -- --

Cooling - 5 5 5 KLD effluent will be subjected to RO after primary & tertiary treatment.

Others - - - ----

Total Industrial waste water

- 122.5 122.5 Total 122.5 KLD effluent will be generated from process & cooling tower. 73.5 KLD effluent (effluent which property like water) will be internally recycled. Remaining 49 KLD

Page 23 of 126


Page 23 of 126

water along with 10 KLD domestic water will be subjected to RO after primary & tertiary treatment. Unit will get 36 KLD water as RO-Permeate. Remaining 23 KLD Ro-rejected water will be sent to M/s. ACPTCL.

-


Unit will be having primary and Tertiary treatment facility. Total capacity of effluent treatment will be 75 KLD. Unit has also proposed to install RO. RO capacity will be 60 KLD.


Domestic:10

Industrial:122.5

Total 122.5 KLD effluent will be generated from process & cooling tower. 73.5 KLD effluent (effluent which property like water) will be internally recycled. Remaining 49 KLD water along with 10 KLD domestic water will be subjected to RO after primary & tertiary treatment. Unit will get 36 KLD water as RO-Permeate. Remaining 23 KLD Ro-rejected water will be sent to M/s. ACPTCL.


M/s. ACPTCL

Membership of CF

Unit is having membership certificate of M/s. ACPTCL.


109.5 KL/Day

E Air [Existing & Proposed]

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


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 TFH 11

Agro waste/Briquet

te

3 MT/Day

Particulate Matter

Sox Nox

Bag Filter

2. D. G. Set (100 KVA)

10 Diesel 300 lit/Day

Particulate Matter

Sox Nox

----

• For proposed expansion 18KLD stream will be required. To cope up the

Page 24 of 126


Page 24 of 126

demand of steam, unit will not install boiler in this premises. Unit will take 18KLD stream from the parent industry M/s.:Subhasri Pigments Pvt Ltd.located at Plot No:- J-1201+1202+1211+1213+1208+1209+1209/A, GIDC Industrial Estate, Ankleshwar, in the vicinity of this plot.


-

Sr. no.

Source of emission

Type of emission



Measures (APCM)

1 Chlorination

Reactor

HCl Cl2

15

Water Scrubber followed by

Alkali Scrubber

2 Drowning

vessel

HCl

15

Water Scrubber

-


- Unit has proposed to install water scrubber and alkali scrubber to curb the

process and fugitive emission.


i

Sr. no.




Quantity (MT/Annum)

Disposal Method

1 ETP sludge From process

35.3 1440 Collection, Storage, Transportation, Disposal at TSDF site authorized by the GPCB.

2 Used Oil From lubrication of machineries

5.1 6 Collection, Storage, Transportation, Reused, Disposal at by Selling registered refiners.

3 Discarded From raw 33.1 12 Collection,

Page 25 of 126


Page 25 of 126

containers/ Empty barrels

material Storage, Decontamination, Reuse/ Transportation, Disposal at by Selling to recycler.

4 Empty bags / Liner

From raw material

33.1 24 Collection, Storage, Decontamination, Reuse/ Transportation, Disposal by Selling to recycler or disposal through TSDF Site

5 Aluminum chloride Solution (acidity:-11% to 12%) (Al2O3:- 3 to 3.5%)

From process

26.3 12000 Unit will send this filtrate in parent industry M/s. Subhasri Unit for the manufacturing of PAC under rule 9..

6 Sodium Hypo Chloride Solution (10% to 10.5%)

From process

-- 2640 Sell to end user having permission under rule-9.

7 Spent Carbon

From ETP 36.2 0.6 Disposal by incineration in common incineration of BEIL

8 Hydrochloric Acid (26% to 28%)

From process

-- 3564 Internal recycle in process-drowning vessel if applicable rule 9 permission will be taken.


Unit is having a membership in TSDF site M/s.BEIL.


Unit will follow MSW rules.



Unit will recover more than 95% solvent.

ii VOC emission sources and its mitigation measures There will be no such raw

Page 26 of 126


Page 26 of 126

material which is led to generate VOC emission.

• Technical presentation was made by the project proponent.

• Committee noted that existing products will be removed and CC&A will be surrendered after getting

EC. Committee felt that the proposed project shall be considered as new project as there will be no

existing activities after getting EC and there will be no impact on environment from the existing

activities.

• Steam requirement for the proposed project shall be obtained from their sister concern unit namely

M/s.:Subhasri Pigments Pvt Ltd.which is located at adjacent plot. Unit will also obtain Cl2 gas as

raw material from their sister concern unit through pipeline. Committee deliberated on safety issues

for Cl2 handling and asked to follow PESO norms for storage and handling of Cl2 gas.

• Waste water generated from the proposed project will be subjected to RO after primary & tertiary

treatment. Unit will get 36 KLD water as RO-Permeate. Remaining 23 KLD Ro-rejected water will

be sent to Common MEE of M/s. ACPTCL, Ankleshwar which is common facility with ZLD.






1. Adequacy of proposed area with respect to plant machineries , EMS, green belt , safety aspect,

raw material & product storage considering worst case scenario. Submit proper lay out plan

clearly demarcating all activities with scale.

2. Qualitative and quantitative analysis of hazardous waste streams Spent HCl, Spent Aluminum

Chloride etc. generation from the manufacturing process/scrubbing system and its feasibility

report for reuse within premises. Worst case scenario shall be considered for generation of

wastes streams. Explore the possibilities to complete reuse of above mentioned hazardous

wastes streams within premises.

3. Details regarding availability of extra steam from the sister concern unit. Agreement with sister

concern unit for supply of steam.

4. Permission from the concern authority for pipeline of Steam and Chlorine gas from the sister

concern unit.





2006.



4. SIA/GJ/MIS/22097/2018 M/s. Vihaan Clean & Green Tech Private Screening &

Page 27 of 126


Page 27 of 126

Limited Survey No : 166, Village: Dholasan, Taluka: Jotana, District: Mehsana, Gujarat

Scoping

Project / Activity No.: 7(h)

Project status: New

• This office has received an application vide their online proposal no.

SIA/GJ/MIS/22097/2018dated 07/03/2018regarding grant of Terms of Reference [ToR] for

preparation of EIA/EMP report.

• This is a new unit proposes manufacturing for CETPs as tabulated below:

Sr. no.

Treatment Facility Capacity Proposed MLD

1 Common Effluent Treatment Plant (CETP) for food processing industries

10 MLD

• The project falls under Category B of project activity 7(h) as per the schedule of EIA Notification

2006.



project proponent.


Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 90.00 Crores

1. Capital cost for EMS (Environmental Management System):. 90.00 Crores

2. Recurring cost towards the environmental protection measures:.0.2 Crores per

Annum.

B Total Plot area ( sq. meter) 14,769 Sq. m.

Green belt area,/Tree Plantation area ( sq. meter) 5000 Sq. m.

C Employment generation

1. Direct 40

2. Indirect 25

Total 65

D Water

i


Local gram panchayat

Status of permission from the concern authority. Permission has been obtained from local authority.

ii Water consumption (KLD)

Category

Water Consumption KLD

Remarks

(A) Domestic 3.0 Fresh Water from local gram panchayat

(B) Gardening 15.0 Treated water will be reuse in gardening.No fresh

Page 28 of 126


Page 28 of 126

water requirement.

(C) Industrial

Process 1.0 No fresh water requirement.Treated water will be reuse for preparation of nutrient solution for aerobic secondary treatment.

Washing 0.0

Boiler 0.0

Cooling 0.0

Others 0.0

Industrial Total 16.0

Total (A + B + C) 19.0

1) Total water requirement for the project: 3.0 KLD

2) Quantity to be recycle: Wastewater being received & treated will be 10 MLD & it will not be a part of the water requirement & wastewater generation of the project.Out of this 10 MLD, at least 5 MLD will be given back to the contributing member on commercial basis.In addition to this,@ 0.5 MLD will be given to the food park management for development of internal road plantation & green belt development within the parks being developed.The remaining will be @ 4.5 MLD will be further treated to ensure for the use of industrial purpose & will be given to the nearby farmers as well as industries on commercial basis.Total details for potential users in addition to the food industries will be incorporated in REIA report. 3) Total fresh water requirement: 3.0 KLD


-

Category KLD Remarks

(A) Domestic 2.4 Being a negligible quantity of sewage,it will be treated along with the aerobic treatment of the CETP.

(B) Industrial

Process 0.0

Washing 0.0

Boiler 0.0

Cooling 0.0

Others 0.0


0.0

-

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

6 MLD

v Mode of Disposal & Final meeting point Domestic: Will be treated in CETP Industrial:


--

Membership of Common facility (CF) --

vii Reuse/Recycle details (KLD) Wastewater being received & treated will be 10 MLD & it will not be a part of

Page 29 of 126


Page 29 of 126

the water requirement & wastewater generation of the project.Out of this 10 MLD, at least 5 MLD will be given back to the contributing member on commercial basis.In addition to this,@ 0.5 MLD will be given to the food park management for development of internal road plantation & green belt development within the parks being developed.The remaining will be @ 4.5 MLD will be further treated to ensure for the use of industrial purpose & will be given to the nearby farmers as well as industries on commercial basis.Total details for potential users in addition to the food industries will be incorporated in REIA report.

E Air


-

SR. no.

Source of emission With Capacity


Type of Fuel

Quantity of Fuel M3/Day

Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 Biogas Electrification Plant (Max.3 MW)

10 Biogas 32,000-35,000

-- ---

2. D.G Set (375 KVA)

7 LDO 40 L/hr -- --

CNG/LPG will be used as alternative fuel in biogas electrification plant.

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

-

Sr. no.

Source of emission

Type of emission



1 -- -- -- --

-

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

Being a CETP project involving handling of ETP chemicals & effluent from the food industries minor odor nuisance is envisaged

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

i

Sr. no.

Type of Hazardous waste



Quantity (MT/Annum)

Disposal Method

1 Used Oil From Plant & Machinery

5.1 7 KL Collection, storage, transportation, disposal to GPCB registered recyclers

2 Discarded From Raw 33.3 30 MT Collection, storage,

Page 30 of 126


Page 30 of 126

Containers/liner/bags

Material Storage

transportation, disposal to GPCB registered recyclers

Quantity of discarded containers must be in MT/Annum.

DETAILS ON NON-HAZARDOUS WASTE

Sr.No

Description of Waste

Quantity(MT/Month) Disposal

1

Sludge from the secondary treatment consisting of aerobic & anaerobic

45

It will be used as manure within premises as well as by the potential users utilizing treated water.

ii Membership details of TSDF, CHWIF etc. Membership of registered recyclers will be obtained prior to commencement of the project.

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

Sludge from the secondary treatment & it will be used as manure within premises as well as by the farmers utilizing treated water.

Technical presentation was made by the project proponent. Project proponent has submitted revised

Form-1 and PFR for revised capacity of proposed CETP. Upon asking, PP informed that earlier they

have proposed 4 MLD capacity considering the 10 % additional capacity for future expansion. After

submission of ToR application, they received request letters from already existing/functional units

considering their expansion in near future and considering such requests, PP has revised their CETP

capacity from 4 MLD to 10 MLD. PP has also submitted a letter regarding justification for modification of

capacity and relevant details. The proposed CETP is exclusively for food & agro processing industries

of nearby area. Effluent from various food processing industries will be accepted either through pipeline

or GPS mounted dedicated tankers. Required treated water will be re-used/recycled to maximum extent

within CETP premises for gardening purpose, chemical preparation & toilet flushing. The balance will

be given to contributing member units to the extent of 45% to 50% on commercial basis and the

remaining to the potential farmers of nearby area for irrigation purpose.Online monitoring system will be

installed as per CPCB guideline at requisite locations in CETP as well as magnetic flow meter, online

pH & TDS meter will be installed at all contributing member units. The common effluent treatment plant

will be designed based on direct degradation of raw effluent with anaerobic process followed by aerobic

treatment to achieve desired norms. It is proposed to establish a biogas electrification plant for captive

use & supply of balanced biogas to nearby contributing member units based on feasibility of distribution

network. While discussing about the reuse of treated waste water, PP informed that entire quantity of

treated waste water will be recycled and the details for potential users in addition to the food industries

will be incorporated in REIA report. Committee asked them to submit action plan for monsoon when

treated waste water cannot be utilized for gardening and plantation purpose.

After deliberation on various aspects, the terms of reference proposed by the project proponent were

accepted and the project proponent was asked to include following additional TOR for the EIA study to

be done covering 5 Km radius surrounding the periphery of the project :

Page 31 of 126


Page 31 of 126

1. A tabular chart with index for point-wise compliance of below mentioned TORs.

2. Land Possession Documents of the proposed site.

3. NA permission letter for proposed site.

4. Project sitespecific details such asdistance of the project site from the nearest (1) Village (2)

Water Body: Creek / Nallah / Lake / Pond / Reservoir / Canal (3) NationalHighway (4) State

Highway (5) Railwayline(6) Heritage site (7) NationalPark / Wild LifeSanctuary / Reserve Forest

shall beincluded. Give satellite image of 10 KM radius from the boundary of project premises.

5. Present land use pattern of the study area as well as the project area shall be given based on

satellite imagery.

6. Provision of separate entry, exit and continuous unobstructed open path within the

projectareafor unobstructed easy movement of the emergencyvehicle / firetenders without

reversing back. Mark the same in the layout.

7. Exact scope of the project should be given in detail. Need for the proposed CETP shall be

justified in detail.

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

requirementsfor the proposed project. Permission from the concern authority for requirement of

the fresh water. Details of proposed ground water recharge scheme should also be submitted.

9. Characteristics of untreated and treated wastewater. A detailedeffluenttreat ability study vis-à-

vis the adequacy and efficacyof the treatment facilities proposedfor the wastewater tobe

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

based shall also be stated.

10. Explore use of Best Available Technology (BAT) incorporating latest features for the proposed

CETP instead of providing conventional treatment units.

11. Details of the CETP units including its capacity, size of each unit, retentiontime and other

technical parameters.

12. Techno-feasibility & adequacy for reuse / recycle of treated effluent by member units.

Justifications of the economic viability of the treated effluent reuse / recycle. Details of the

scheme fortotal recycle-reuse of the treated effluent. Details regarding the percentage of waste

water to be reused / recycled by each member units.

13. Application wise break-up of treated effluentquantitytobe recycled / reused in various

applications and green beltdevelopmentetc. Details about availability of sufficient open land and

suitability for utilizing treated effluent for plantation / gardening. How it will be ensured that

treated effluent won't flow outside the premises linked with storm water during high rainy days.

14. Action plan for monsoon when treated waste water cannot be utilized for gardening and

plantation purpose.

15. Detailed layout of effluentconveyancepipelinewith distances and all technical specifications, line

diagram and totalcapacity of the pipeline to convey effluent. Details of pumping stations,

pumping capacity in each pumping station etc. (if any) shall also be furnished.

16. List of the CETP members, their productioncapacity, effluent reuse / recycle capacity,

effluentgeneration capacity, effluent characteristics and effluent quantity. Whether any future

projections are envisagedfor finalization of the CETP capacity and conveyance pipeline.

17. Undertaking that only Food Industries & Agro Processing industries shall be permitted as a

member of the proposed CETP and there shall be no any other Chemical Industrial units as a

member.

Page 32 of 126


Page 32 of 126

18. Explore the possibilities of ‘Zero’ discharge of effluent (ZLD).

19. Explore the possibilities to give treated waste water to industrial units instead of sending to

Farmers.

20. Details about the proposedinlet norms of the CETP. Give details of the mandatorytreatment, if

any required by the member units to achieve the inlet norms by the each unit.

21. Specific monitoring plan to ascertain that all the CETP member units send their effluent

[contracted quantity] to the CETP and the effluent does not in any way find its way to other

sources i.e. measures to eliminate by passing of the effluent.

22. Details of the pipeline maintenance program to avoid choking / overflow / leakage of the effluent

conveyance pipeline and means to avoid the same.

23. Provision of flow meter at the outlet of the CETP; checks & balances to ensure that discharge

quality and quantity never exceeds the prescribed limit.

24. Details of the monitoring plan of the member units to ensure compliance with the inlet norms of

the CETP as well as to avoid shock loading in the system.

25. Justification / capacity of the project keeping in view the future effluent load from the additional

member units.

26. Details of CETP management and maintenance of the CETP during operation phase including

infrastructure, model of management, role of each stake holder, CETP effluent quality

monitoring scheme etc.

27. Impact of the CETP installation and treated effluent conveyance & disposal system on the

environment including the local hydrology, soil condition, floral and faunal bio-diversity of the

region and the mitigation measures proposed.

28. Surface water quality and ground water quality in the study area.

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

30. Details of emergency storage of effluent in the CETP for the monsoon season.

31. Details of R&D to be initiated by the CETP management for effective and viable treatment of the

effluent received.

32. Details of total power load required for the CETP as well as details of dedicated power back up /

D.G.Sets to be provided to take care of power requirements during power supply failure, to

ensure that treatment units operate uninterrupted.

33. CETP managementmanualcoveringvarious management aspects during the effluent collection,

transportation, treatment and disposal aspects forbest management practices. The member

units shall abide by various clauses in this regard tocheck problems during the collection,

transportation, treatment and reuse / recycle / disposal of the effluent.

34. One season Site-specific micro-meteorological data using temperature, relative humidity, hourly

wind speed and directionand rainfall should be incorporated.

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

significance and based on corresponding likely impacts VECs (Valued Environmental

Components) may be identified. Baseline studies may be conducted within the study area of 5

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

magnitude in order to identify mitigation measures.

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

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

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

Page 33 of 126


Page 33 of 126

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

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

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

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

concentration is likely to occur.

37. Modelling indicating the likely impact on ambient air quality due to proposed activities. The

details of model used and input parameters used for modelling should be provided. The air

quality contours may be shown on location map clearly indicating the location of sensitive

receptors, if any, and the habitation. The wind rose showing pre-dominant wind direction should

also be indicated on the map. Impact due to vehicular movement shall also be included into the

prediction using suitable model. Results of Air dispersion modelling should be superimposed on

satellite image/ geographical area map.

38. Quantity of fuel required, its source and transportation.

39. Specific details of (i) Details of the utilities required (ii) Flue gas emission ratefrom each utility

(iii) Air PollutionControl Measures proposedto each of the utility along with its adequacy.

40. Impact of the project on local infrastructure of the area such as on road network due to

transportation of effluent, fuel, ash etc. Whether any additional infrastructure would need to be

constructed and the agency responsible for the same with time frame.

41. Details of flora and fauna duly authenticated should be provided. In case of any scheduled

fauna, conservation plan should be provided.

42. Details of management of the hazardous wastes tobe generated from the project stating detail

of storageareafor each type of waste, its handling, its utilization and disposal etc. How the

manual handling of the hazardous wastes will be minimized.

43. Characteristics of manure to be generated from CETP operations and its sound management.

44. Copy of membershipcertificate of Common Environmental Infrastructure like TSDF, (if required)

should be incorporated.

45. Details of measures proposedfor the noise pollutionabatement and its monitoring. Provisions to

provide ear plugs / ear muffs to workers and to ensure its usage in high noise areas. Measures

to ensure that the noise from the looms remains less than 80 dB(A). Undertaking to carry out

Audiography of workers working near the looms, at least once in a year.

46. A detailed EMP including the protection and mitigation measures forimpact on human health

and environment as well as detailed monitoringplan and environmental

managementcellproposed for implementation and monitoring of EMP. The EMP should also

include the concept of waste-minimization, recycle/reuse/recover techniques, energy

conservation, and naturalresource conservation. Totalcapitalcost and recurring cost/annum

earmarkedforenvironmentpollutioncontrol measures.

47. Occupationalhealth impacts on the workers and mitigation measures proposedto avoid the

human health hazards along with the personalprotectiveequipment to be provided to the

workers. Provision of industrial hygienist and monitoring of the occupationalinjury to workers

aswell as impact on the workers. Plan forperiodicmedicalcheck up of the workers exposed.

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

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

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

carried out. The worst-case scenario should take into account the maximum inventory of

Page 34 of 126


Page 34 of 126

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

clearly showing which of the activities would be affected in case of an accident taking place.

Based on the same, proposed safeguard measures including On-Site / Off-Site emergency plan

should be provided.

49. Measures to guard against fire hazards including details of automaticfiredetection and

controlsystem&detailed fire controlplan showing hydrantpipeline network, provision of DG Sets,

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

50. Provision to ensure sufficient water storage all the time for use during emergency situation.

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

manufacturing utility staff for safety related measures.

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

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

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

at appropriate places in the nearby areas and elsewhere.

53. Proposal for socio-economic development activities including communitywelfare program most

useful in the projectareafor the overallimprovement of the environment. Submit a detailed plan

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

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

54. A tabular chartfor the issues raised and addressed during public hearing/consultation

and commitment of the project proponent on the same should be provided. An action

plan to address the issues raised during public hearing and the necessary allocation of

funds for the same should be provided.

55. Plan forcompliance of CETP guidelinesissued by the CPCB.

56. Whether any litigationpending and / or any direction/ order passed by any Court of Law against

the company, if so, details thereof.

57. Details of schemefor surface aswell as roof top rain water harvesting and ground water recharge

with proper scientific calculations considering rainfall in the region, catchment area, land / soil

characteristics, ground water recharge rate, duration of rain water harvesting etc. Details of

provisions of pre-treatment of the rainwater in the case of surface run off are to be harvested.

Location of recharge percolation wells on the layout plan.

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

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

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

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

59. Disciplinary policy of CETP for member units.

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

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

system may be given.

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

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

This reporting mechanism should be detailed in the EIA Report.

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

incorporated in the EIA Report.

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

Page 35 of 126


Page 35 of 126

MoEF’s sector specific EIA Manual for CETP shall be considered as generic TORs for preparation of

the EIA report in addition to all the relevant information as per the generic structure of EIA given in

Appendix III in the EIA Notification, 2006. The draft EIA report shall be submitted to the Gujarat

PollutionControlBoardfor conducting the publicconsultationprocessasper the provisions of the

EIA Notification, 2006.

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


Validity of ToR:

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

& EMP report accordingly, ToR will lapse after 3 years from the date of issue.

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

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

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

recommendation of the SEAC

5. SIA/GJ/MIS/22240/2018 M/s. Narol Textile Infrastructure &Enviro Management Survey no. 34/Paiki, Gyaspur, Pirana Sewage Farm area, Near Animal Health Foundation, Gyaspur, Ahmedabad.

Screening & Scoping

Project / Activity No.: 7(h)



SIA/GJ/MIS/22240/2018dated 01/02/2018 regarding grant of Terms of Reference [ToR] for


• This is an existing Common Effluent Treatment Plant [CETP] and now proposes for expansion

as tabulated below:

Sr

No

Activity Existing

Capacity

Additional

Capacity

Ultimate

Capacity

1. Collection, Treatment and Disposal of partially

treated effluent generated from member textile units

of Narol Textile Infrastructure & Enviro

Management, Narol

100 MLD 30 MLD 130 MLD

• The project falls under Category B of project activity 7(h) as per the schedule of EIA Notification

2006.



project proponent.


Sr. no.

Particulars Details

Page 36 of 126


Page 36 of 126


(Rs. in Crores):

Existing: 19656 Proposed: Total: 19656


Existing: 113700 Sq. m. Proposed: KK.Sq. m. Total: 113700 Sq. m.


Existing: 10000 Sq. m. Proposed: Sq. m. Total: 10000 Sq. m.


D Water

i


Ahmedabad Municipal Corporation.


Not applicable

ii


Existing KLD



Remarks

(E) Domestic 20.00 NIL 20.00

(F) Gardening 10.00 NIL 10.00

Industrial

Process NA NA NA

Washing NA NA NA

Boiler NA NA NA

Cooling NA NA NA

Others NA NA NA

Industrial Total NIL NIL NIL

Grand Total (A+B+C)

30.00 NIL 30.00


2) Quantity to be recycle: NIL


iii


Page 37 of 126


Page 37 of 126




Remarks

(B) Domestic 20.00 NIL 20.00

Industrial

Process --- --- ---

Washing --- --- ---

Boiler ---- --- ---

Cooling --- --- ---

Others --- --- ---


--- --- --

-


We have operating CETP having permission of 100 MLD and we are going for an expansion for additional 30 MLD


Domestic: 20 KLD

Industrial: 130 MLD


---

Membership of CF

---


---



-

SR. no.

Source of

emission With

Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

Not Applicable

-


-

Sr. no.

Source of emission

Type of emission



Measures (APCM)

Page 38 of 126


Page 38 of 126

Not Applicable

-



i

Sr. no.




Quantity (MT/Annum)

Disposal Method

1 ETP Sludge CETP 35.3 118625 Collection, storage, Transportation and Dispose to Active TSDF Site

2 Used Oil CETP 5.1 23.72 Collection, storage, Reuse within premises.

3 Discarded Container/ Bags

Raw material Storage

33.1 21900 Collection, storage, Transportation and Dispose to Registered Recycler.


We have obtained membership of Authorized TSDF site


Technical presentation was made by the project proponent. This is a Common Effluent Treatment

Plant(CETP) having permission of 100 MLDoperated by Narol Textile Infrastructure & Enviro Management

[NTIEM] is in operation and collecting partially treated effluent of 100 MLD generated from member textile units of

NTIEM through conveyance line laid down by NTIEM in Narol, Shahwadi and piplaj area. CETP of NTIEM treating

this wastewater into Common facility and disposed the treated waste water into River Sabarmati after achieving

GPCB Norms.

While discussing about the justification for proposed expansion, PP informed that Capacity of CETP has been

Page 39 of 126


Page 39 of 126

proposed by estimating wastewater from member industries and for that they were conducted primary inventory at

that time.

They have designed this CETP having latest technology which is capable to handle textile effluent up to 200 MLD.

Due to market demand member units are expanding their processing units. They have designed this CETP by

keeping future expansion of our member industries. Looking to the scenario, Narol Textile Infrastructure & Enviro

Management wants to utilized this additional capacity of Common Effluent Treatment Plant and expand their

Collection, Treatment and Disposal of partially treated effluent generated from member textile units from 100 MLD

to 130 MLD at present.Further PP informed that they are introducing latest treatment Technology and for proposed

expansion the retention time in key treatment units namely CONTINUOUS FLOW INTEGRATED CLARIFIER

ACTIVATED SLUDGE SYSTEM (CFICASS TANK) will be reduced by only 04 Hours and it will be 24 Hours instead

of 28 hours. This unit is designed to take hydraulic load of 200 MLD looking to textile effluent.

Committee noted the following salient features of the proposed expansion.

� Proposed expansion will be within same premises and there will be no additional land required for this

proposed expansion.

� The existing infrastructure is capable to handle proposed load and there will be no additional infrastructure

is required for this proposed expansion.

� The conveyance line to receive the partially treated effluent from member industries is callable enough to

convey 225 MLD wastewater hence there will be no additional conveyance line required for this proposed

expansion.

� There is no fuel required for existing facilities as well as proposed expansion

� They have adopted latest technology for sludge drying which is dry up to 80 % of total waste generation

hence the sludge generation is also lesser than the conventional technology

� They installed SCADA system to control the flow from member industries.

After deliberation on various aspects, the terms of reference proposed by the project proponent were

accepted and the project proponent was asked to include following additional TOR for the EIA study to

be done covering 5 Km radius surrounding the periphery of the project :

1. A tabular chart with index for point-wise compliance of below mentioned TORs.

2. Land Possession Documents of the proposed site.

3. Project sitespecific details such asdistance of the project site from the nearest (1) Village (2)

Water Body: Creek / Nallah / Lake / Pond / Reservoir / Canal (3) NationalHighway (4) State

Highway (5) Railwayline(6) Heritage site (7) NationalPark / Wild LifeSanctuary / Reserve Forest

shall beincluded. Give satellite image of 10 KM radius from the boundary of project premises.

4. Need for the proposed expansion should be justified in detail.

5. Adequacy of existing EMS (Environmental Management System).

6. Explore the possibility to reuse treated waste water for existing as well as proposed activity.

7. Permission from the concern authority for treated effluent discharge in to mixing chamber of final

disposal point at Pirana STP of Ahmedabad Municipal Corporation through NTIEM pipe line.

8. Records of any legalbreach of Environmental laws i.e. details of show- cause notices, closure

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

after for prevention of pollution.

9. Copies of Environmental Clearances obtained for the existing plant, its point wise compliance

report.

Page 40 of 126


Page 40 of 126

10. Environmental audit reports for last 3 years and compliance of its

recommendations/Suggestions. (Include latest audit report and its compliance.)

11. Copy of Consent to Operate (CC&A) obtained along with point wise compliance status of all the

conditions stipulated therein.

12. Copies of XGN generated Inspection reports with analysis reports of the water/Air/Hazardous

samples collected by GPCB (Last 2 year). Copies of instructions issued by GPCB in last 2 year

and point wise compliance thereof.

13. Certified Compliance Report (CCR) from the Member Secretary, GPCB as per the MoEFCC’s

Circular no. J-11011/618/2010- IA (II) (I) dated 30/05/2012 and Circular no. J-11013/6/2010-IA-II

(Part) vide dated 07/09/2017.

14. Present land use pattern of the study area as well as the project area shall be given based on

satellite imagery.

15. Provision of separate entry, exit and continuous unobstructed open path within the

projectareafor unobstructed easy movement of the emergencyvehicle / firetenders without

reversing back. Mark the same in the layout.

16. Exact scope of the project should be given in detail. Need for the proposed expansion of CETP

shall be justified in detail.

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

requirementsfor the proposed project. Permission from the concern authority for requirement of

the fresh water. Details of proposed ground water recharge scheme should also be submitted.

18. Characteristics of untreated and treated wastewater. A detailedeffluenttreat ability study vis-à-

vis the adequacy and efficacyof the treatment facilities proposedfor the wastewater tobe

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

based shall also be stated.

19. Explore use of Best Available Technology (BAT) incorporating latest features for the proposed

CETP instead of providing conventional treatment units.

20. Details of the CETP units including its capacity, size of each unit, retentiontime and other

technical parameters.

21. Techno-feasibility & adequacy for reuse / recycle of treated effluent by member units.

Justifications of the economic viability of the treated effluent reuse / recycle. Details of the

scheme fortotal recycle-reuse of the treated effluent. Details regarding the percentage of waste

water to be reused / recycled by each member units.

22. Application wise break-up of treated effluentquantitytobe recycled / reused in

variousapplications and green beltdevelopmentetc. Details about availability of sufficient open

land and suitability for utilizing treated effluent for plantation / gardening. How it will be ensured

that treated effluent won't flow outside the premises linked with storm water during high rainy

days.

23. Detailed layout of effluentconveyancepipelinealong with distances and all technical

specifications, line diagram and totalcapacity of the pipeline to convey effluent. Details of

pumping stations, pumping capacity in each pumping station etc. if any shall also be furnished.

24. List of the CETP members, their productioncapacity, effluent reuse / recycle capacity,

effluentgeneration capacity, effluent characteristics and effluent quantity. Whether any future

projections are envisagedfor finalization of the CETP capacity and conveyance pipeline.

25. Undertaking that no industrial units except Textile industries shall be permitted as a member of

Page 41 of 126


Page 41 of 126

the proposed CETP.

26. Details about the proposedinlet norms of the CETP. Give details of the mandatorytreatment, if

any required by the member units to achieve the inlet norms by the each unit.

27. Specific monitoring plan to ascertain that all the CETP member units send their effluent

[contracted quantity] to the CETP and the effluent does not in any way find its way to other

sources i.e. measures to eliminate by passing of the effluent.

28. Details of the pipeline maintenance program to avoid choking / overflow / leakage of the effluent

conveyance pipeline and means to avoid the same.

29. Provision of flow meter at the outlet of the CETP; checks & balances to ensure that discharge

quality and quantity never exceeds the prescribed limit.

30. Details of the monitoring plan of the member units to ensure compliance with the inlet norms of

the CETP as well as to avoid shock loading in the system.

31. Justification / capacity of the project keeping in view the future effluent load from the additional

member units.

32. Details of CETP management and maintenance of the CETP during operation phase including

infrastructure, model of management, role of each stake holder, CETP effluent quality

monitoring scheme etc.

33. Impact of the CETP installation and treated effluent conveyance & disposal system on the

environment including the local hydrology, soil condition, floral and faunal bio-diversity of the

region and the mitigation measures proposed.

34. Surface water quality and ground water quality in the study area.

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

36. Details of emergency storage of effluent in the CETP for the monsoon season.

37. Details of R&D to be initiated by the CETP management for effective and viable treatment of the

effluent received.

38. Details of total power load required for the CETP as well as details of dedicated power back up /

D.G.Sets to be provided to take care of power requirements during power supply failure, to

ensure that treatment units operate uninterrupted.

39. CETP managementmanualcoveringvarious management aspects during the effluent collection,

transportation, treatment and disposal aspects forbest management practices. The member

units shall abide by various clauses in this regard tocheck problems during the collection,

transportation, treatment and reuse / recycle / disposal of the effluent.

40. One season Site-specific micro-meteorological data using temperature, relative humidity, hourly

wind speed and directionand rainfall should be incorporated.

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

significance and based on corresponding likely impacts VECs (Valued Environmental

Components) may be identified. Baseline studies may be conducted within the study area of 5

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

magnitude in order to identify mitigation measures.

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

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

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

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

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

Page 42 of 126


Page 42 of 126

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

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

concentration is likely to occur.

43. Modeling indicating the likely impact on ambient air quality due to proposed activities. The

details of model used and input parameters used for modeling should be provided. The air

quality contours may be shown on location map clearly indicating the location of sensitive

receptors, if any, and the habitation. The wind rose showing pre-dominant wind direction should

also be indicated on the map. Impact due to vehicular movement shall also be included into the

prediction using suitable model. Results of Air dispersion modeling should be superimposed on

satellite image/ geographical area map.

44. Impact on Environment due to additional discharge of waste water to River Sabarmati.

45. Quantity of fuel required, its source and transportation.

46. Specific details of (i) Details of the utilities required (ii) Flue gas emission ratefrom each utility

(iii) Air PollutionControl Measures proposedto each of the utility along with its adequacy.

47. Impact of the project on local infrastructure of the area such as on road network due to

transportation of effluent, fuel, ash etc. Whether any additional infrastructure would need to be

constructed and the agency responsible for the same with time frame.

48. Details of flora and fauna duly authenticated should be provided. In case of any scheduled

fauna, conservation plan should be provided.

49. Details of management of the hazardous wastes tobe generated from the project stating detail

of storageareafor each type of waste, its handling, its utilization and disposal etc. How the

manual handling of the hazardous wastes will be minimized.

50. Copy of membershipcertificate of Common Environmental Infrastructure like TSDF, if any taken,

should be incorporated.

51. Details of measures proposedfor the noise pollutionabatement and its monitoring. Provisions to

provide ear plugs / ear muffs to workers and to ensure its usage in high noise areas. Measures

to ensure that the noise from the looms remains less than 80 dB(A). Undertaking to carry out

Autography of workers working near the looms, at least once in a year.

52. A detailed EMP including the protection and mitigation measures forimpact on human health

and environment as well as detailed monitoringplan and environmental

managementcellproposed for implementation and monitoring of EMP. The EMP should also

include the concept of waste-minimization, recycle/reuse/recover techniques, energy

conservation, and naturalresource conservation. Totalcapitalcost and recurring cost/annum

earmarkedforenvironmentpollutioncontrol measures.

53. Occupationalhealth impacts on the workers and mitigation measures proposedto avoid the

human health hazards along with the personalprotectiveequipment to be provided to the

workers. Provision of industrial hygienist and monitoring of the occupationalinjury to workers

aswell as impact on the workers. Plan forperiodicmedicalcheck-up of the workers exposed.

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

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

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

carried out. The worst-case scenario should take into account the maximum inventory of

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

clearly showing which of the activities would be affected in case of an accident taking place.

Page 43 of 126


Page 43 of 126

Based on the same, proposed safeguard measures including On-Site / Off-Site emergency plan

should be provided.

55. Measures to guard against fire hazards including details of automaticfiredetection and

controlsystem&detailed fire controlplan showing hydrantpipeline network, provision of DG Sets,

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

56. Provision to ensure sufficient water storage all the time for use during emergency situation.

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

manufacturing utility staff for safety related measures.

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

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

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

at appropriate places in the nearby areas and elsewhere.

59. Proposal for socio-economic development activities including communitywelfare program most

useful in the projectareafor the overallimprovement of the environment. Submit a detailed plan

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

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

60. A tabular chartfor the issues raised and addressed during public hearing/consultation and

commitment of the project proponent on the same should be provided. An action plan to

address the issues raised during public hearing and the necessary allocation of funds for the

same should be provided.

61. Plan forcompliance of CETP guidelinesissued by the CPCB.

62. Whether any litigationpending and / or any direction/ order passed by any Court of Law against

the company, if so, details thereof.

63. Details of schemefor surface aswell as roof top rain water harvesting and ground water recharge

with proper scientific calculations considering rainfall in the region, catchment area, land / soil

characteristics, ground water recharge rate, duration of rain water harvesting etc. Details of

provisions of pre-treatment of the rainwater in the case of surface run off are to be harvested.

Location of recharge percolation wells on the layout plan.

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

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

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

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

65. Disciplinary policy of CETP for member units.

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

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

system may be given.

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

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

This reporting mechanism should be detailed in the EIA Report.

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

incorporated in the EIA Report.

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

MoEFCC’s sector specific EIA Manual for CETP 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

Page 44 of 126


Page 44 of 126

Appendix III in the EIA Notification, 2006. The draft EIA report shall be submitted to the Gujarat

PollutionControlBoardfor conducting the publicconsultationprocessasper the provisions of the EIA

Notification, 2006.

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


Validity of ToR:

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

submission of EIA & EMP report accordingly, ToR will lapse after 3 years from the date

of issue.

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

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

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

justification and also recommendation of the SEAC

6. SIA/GJ/IND2/22381/2018 M/s. Perstorp Industries India Private Limited Plot no. T – 49 to T – 54, Saykha Industrial Estate, Vagra Taluka, Dist.: Bharuch.

Screening & Scoping


Project status: New


SIA/GJ/IND2/22381/2018dated 16/03/2018regarding grant of Terms of Reference [ToR] for


• This is a new unit proposes manufacturing for Synthetic organic chemicals as tabulated below:

Sr. No.


CAS no. /CI no. Quantity MT/Month

End-use of products

1

Pentaerythritols

3333.33 MT/Month

or

(40000 MT/Annum)

Coatings, Resin and synthetic lubricants, polymer additives etc

Pentaerythritol 115-77-5

Dipentaerythritol 126-58-9

Mix Penta

Mixture of 40% Penta 40% Di Penta, 20% moisture

2 Calcium Formate 544-17-2

2166.66 MT/Month

or

(26000 MT/Annum)

Construction industry as additives with cement and additives for food and animal feed.

Total 66000

Page 45 of 126


Page 45 of 126

Production


2006.



project proponent.

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

Sr. no.

Particulars Details


(Rs. in Crores):

480 Crores


114852.23 Sq. m.


22571.00 Sq. m.


Direct: 120 Indirect: 300

D Water i


GIDC


Permission is taken from GIDC for water supply.

ii


Category

KLD

(G) Domestic 7

(H) Gardening 55

(I) Industrial

Process 0

Washing 58

Boiler 234

Cooling 810

Others 36

Industrial Total 1138

Total (A + B + C)

1200

4) Total water requirement for the project: 1200 KLD

5) Quantity to be recycle: 0 KLD


Page 46 of 126


Page 46 of 126

iii


Category Waste water KLD

Remarks

(C) Domestic 6

(D) Industrial

Process 309 266 KLD from Raw material + 43 KLD from Water with ejector

Washing 58

Boiler 191

Cooling 143

Others 36 From Water treatment plant

Total Industrial waste water 744

-


ETP: 1000 KLD having primary and secondary treatment


Domestic: To ETP for treatment and then to CETP for further treatment and disposal

Industrial: To ETP for treatment and then to CETP for further treatment and disposal


CETP of Saykha GIDC

Membership of Common facility (CF)

Membership of CETP is taken


-

E Air

i Flue gas emission details


-

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 – 1 (20 MTPH)

30 NG/FO 1500 Nm

3 /

1250Kg

SO2

NOx PM

Adequate Stack Height

2 Boiler – 2 (20 MTPH)

30 NG/FO 1500 Nm

3 /

1250Kg

3

Boiler – 3 (20 MTPH) (stand by)

30 NG/FO 1500 Nm

3 /

1250Kg

Page 47 of 126


Page 47 of 126

4

Waste Heat Recovery Boilercum Incinerator – 1 (5 MTPH)

30 NG/FO 375 Nm

3 / 300

Kg

5

Waste Heat Recovery Boiler cumIncinerator – 2 (5 MTPH)

30 NG/FO 375 Nm

3 / 300

Kg

6 D. G. Set (700 KW)

11 HSD 280 kg/hr

7 D. G. Set (700 KW)

11 HSD 280 kg/hr

-


-

Sr. no.

Source of emission

Type of emission Stack/Vent

Height (meter)


1 Process and storage area

Formaldehyde

HC 30

Central Absorption water Scrubbing System

2 Recovered methanol buffer

HC 10 Water Scrubber

3 Calcium Hydroxide Vessel

PM 10 Water Scrubber

4 HCl storage tank HCl 10 Water Scrubber

-

iii Fugitive emission details with its mitigation measures. As below: Fugitive emission details will be provided in EIA report.


i

Sr. no.




Quantity (MT/Annum)

Disposal Method

1 Process Sludge

Process 20.4 1626 MT TSDF

2 Ash from

waste heat recovery boiler

cum incineration

Waste heat Recovery Boiler cum Incinerator

37.2 792 MT

To Brick Manufacturing and Cement

Manufacturing Unit

3 Spent active carbon

ETP 36.2 400 MT TSDF/CHWIF

Page 48 of 126


Page 48 of 126

4 Spent ion

exchange resin

Water treatment

plant 35.2 50 MT

TSDF/CHWIF

5 Sludge from ETP

ETP 35.3 1000 MT TSDF

6

Broken packaging

Storage 33.1 396 MT

To registere

d recycler

7 Mother Liquor Process 20.3 8000 MT

Incinerated at site

8 Recovered Methanol

Process 20.2 3600 MT Incinerated at site

9

Used oil Maintenan

ce 5.1 5 MT

To registere

d recycler


Membership of CETP and TSDF will be taken.


Non-Hazardous waste will be generated in the facility on a yearly basis which are listed below:

1. Wooden scrap/ broken

pallet

2. Metal scrap

3. Paper waste

4. Poly bag/plastic waste

5. Powder bag/ gunny bag

6. Miscellaneous garbage

7. Canteen waste



Solvent recovery is a part of process. No separate solvent recovery is required.

ii VOC emission sources and its mitigation measures VOC emission and mitigation measures will be identified in EIA report

• The project proponent along with their environmental consultant attended the meeting.

Technical presentation was made by the project proponent.

• M/s: Perstorp Industries India Private Limited, intend to set up Pentaerythritols manufacturing

facility in Saykha industrial Estate having production capacity of 66000 MT/Annum.

• Committee observed that PP has proposed to discharge treated waste water to Common

Effluent Treatment Plant (CETP) of GIDC- Saykha after in-house treatment. Committee noted

that there is no existence of CETP-Syakha at present. In absence of CETP in Saykha GIDC,

Page 49 of 126


Page 49 of 126

Committee asked PP to opt for Zero Liquid Discharge (ZLD). PP informed that SEIAA, Gujarat

has granted ToR to GIDC for proposed CETP in Saykha and GIDC has committed to

commence CETP by December 2019. GIDC has also committed for alternative disposal system

meeting outlet norms till such time CETP is not available. A letter received from GIDC vide

dated 27/11/2017 in this regard is submitted by PP.Further, PP also informed that their

proposed project will be commenced in year 2020 after getting Environmental Clearance from

SEIAA, Gujarat.

• In view of the above, Committee agreed to allow them to discharge their waste water into

proposed CETP of GIDC-Saykha as proposed.

• Committee observed that Gujarat Industrial Development Corporation (GIDC), GoG has

obtained Environmental clearance for Petroleum, Chemical and Petrochemical Investment

Region (PCPIR), Bharuch and the instant proposal falls within the region of PCPIR. Hence,

public hearing is exempted for this proposal as per para 7(i) (III) (i) (b) of the EIA Notification,

2006 since the project site is located within the PCPIR.

• 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. Current Status of CETP Saykha. Submit a letter from authority of CETP-Saykha in this

regard.

2. In case of CETP-Saykha is not commenced, alternative disposal system available from

the GIDC authority considering disposal norms prescribed by regulatory authority.

3. Design details of In-house Incinerator as per the CPCB Guidelines.

4. Explore the possibilities for maximum reuse of treated waste water and minimum

discharge of waste water into CETP.



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.



7. SIA/GJ/IND2/21602/2018 M/s. P. K. Intermediates Pvt. Ltd. Plot no. C1B, 1906, 1907, GIDC Panoli, Taluka Ankleshwar, District Bharuch, Gujarat.

Screening & Scoping



Page 50 of 126


Page 50 of 126




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

as tabulated below:

Sr. no.

Name of the Products CAS no. Quantity MT/Month End-use of product Existing Proposed Total

1 Piperazine Anhydrous Recovered

110-85-0 20 0 20 Pharmaceutical Intermediate

and Fine Chemicals

2 2-Hydroxy-4-methyl quinolone

607-66-9 0 0.45 0.45

3 2-Chloro-4-methyl quinoline

- 0 0.47 0.47

4 4-methyl quinoline. (Lepidine)

- 0 0.34 0.34

5 Dibenzothiophene 132-65-0 0 0.39 0.39

6 1, 2, 4-triacetoxy benzene

- 0 0.48 0.48

7 Cinnamyl chloride 102-92-1 0 1.00 1.00

8 Cinnamyl Bromide 4392-24-9 0 0.45 0.45

9 4-Phenyl-3-thiosemicarbazide

5351-69-9 0 0.24 0.24

10 Benzhydrylpiprazine - 0 1.05 1.05

11 4-Chlorobenzhydrol piperazine

- 0 1.66 1.66

12 N-Benzyl piperazine 2759-28-6 0 0.71 0.71

13 Acetyl piperazine - 0 0.59 0.59

14 4-methoxy benzoic acid (P-Anisic acid)

- 0 2.18 2.18

15 2, 4, 6-trimethyl Acetophenone

- 0 0.30 0.30

16 N-Acetyl urea - 0 0.47 0.47

17 2-hydroxy -5-fluoroacetophenone

- 0 0.42 0.42

18 4-Acetyl Biphenyl 92-91-1 0 0.53 0.53

19 Diacetyl Hydrazine 3148-73-0 0 0.17 0.17

20 4-Biphenyl carboxylic acid

92-92-2 0 0.36 0.36

21 Phenyl thoiurea 103-85-5 0 0.42 0.42

22 2-Aminobenzthioazole 136-95-8 0 0.40 0.40

23 Benzalacetone 122-57-6 0.80 0.80

24 Ethyl benzoyl acetate 94-02-0 0 0.89 0.89

25 4-Chloro Resorcinol 95-88-5 0 0.40 0.40

26 9, 9’-Bis (Hydroxymethyl) fluorine

- 0 0.42 0.42

27 9, 9’-Bis methoxyFluorene

- 0 0.46 0.46

28 Hydroquinone diacetate 1205-91-0 0 0.35 0.35

29 2, 5-Dihydroxy acetophenone

490-78-8 0 0.40 0.40

30 2-Acetylcyclopentanone 1670-46-8 0 0.35 0.35

31 Disodium phenyl 3279-54-7 0 0.10 0.10

Page 51 of 126


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phosphate

32 4-Nitrophenyl phosphate Disodium salt

4264-83-9 0 0.09 0.09

33 1-Ethyl-2-methyl indole 40876-94-6 0 0.59 0.59

34 2, 3, 3-trimethyl indolinine

1640-39-7 0 0.73 0.73

35 2, 6-Dinito Mesitylene - 0 0.57 0.57

36 2, 6-Diamino Mesitylene - 0 0.44 0.44

37 N-(3-Amino-2, 4, 6—trimethyl phenyl)-2-methyl propanamide.

- 0 0.82 0.82

38 2-Chloroisovaniline 37687-57-3 0 0.33 0.33

39 2-Chloro-3, 5-Dimethoxy Benzaldehyde

112641-63-1 0 0.36 0.36

40 Dimethyl sulfamoyl chloride

13360-57-1 0 0.57 0.57

41 2-Chloro-4-Nitro Anisole 4920-79-0 0 0.35 0.35

42 3-Chloro-4-Methoxy aniline

5345-54-0 0 0.31 0.31

43 2-Chloro-3, 4-Methoxy phenyl hydrazine hydrochloride

- 0 0.32 0.32

44 4-Methoxy acetanilide 51-66-1 0 0.71 0.71

45 5-Acetamido-2-methoxy benzene sulfonyl chloride

- 0 1.07 1.07

46 DiphenylIodinium Bromide

1483-73-4 0 0.19 0.19

47 DiphenylIodinium Chloride

4673-26-1 0 0.15 0.15

48 DiphenylIodinium Nitrate 722-56-5 0 0.15 0.15

49 DiphenylIodiniumTosylate

6293-66-9 0 0.25 0.25

50 2-Chloro-5-phropyl methyl ester

- 0 1.32 1.32

51 2-Phenyl thio-5-proionyl phenyl acetic acid

92321-29-4 0 1.62 1.62

52 2-Methyl-5-hexadecanyl Hydroquinone

- 0 0.38 0.38

53 4-Hydroxy-2-Methyl-5-hexadecanyl phenyl allylether

- 0 0.44 0.44

54 2-Methyl-6-allyl-5-hexadecanyl hydroquinone

- 0 0.22 0.22

55 2-Methyl-6-Propyl-5-hexadecanyl hydroquinone

- 0 0.20 0.20

56 8-Chloroazatidine 38092-89-6 0 2.00 2.00

Total ?? ?? ??


2006.

Page 52 of 126


Page 52 of 126


• During the meeting dated 04/04/2018, technical presentation made by project proponent.


Sr. no.

Particulars Details

A Water i

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

GIDC Panoli


ii Water consumption (KL/day)

-

Existing KL/day

Proposed (Additional) KL/day

Total after Expansion KL/day

(A) Domestic 1 1.1 2.1

(B) Gardening 0 2 2

(C) Industrial

Process 0 3.1 3.1

Washing 0 0.775 0.775

Boiler 1 1 2

Cooling 0.5 1.5 2

Scrubbing 0 1 1

Total (A+B+C) 12.975

-

iii Waste water generation (KL/day)

-

Category Existing KL/Day

Proposed (Additional) KL/day

Total after Expansion KL/day

Remarks

(A) Domestic 0.8 0.88 1.68 Disposed off through soak pit

(B) Industrial

Process 0 7.40 7.40

Washing 0 0.8 0.8

Boiler 0.2 0.2 0.4

Cooling 0 0.2 0.2

Others 0 1 1


0.2 9.60 9.80

-

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

After neutralization, all industrial effluent will be sent to PETL and ACPTL dilute and concentrated separately.


Domestic: Domestic waste water 1.68 KLD will be disposed off through soak pit.

Industrial: Industrial effluent will be segregated into two streams; dilute and concentrated. Dilute will be sent to PETL and concentrated will be sent to PETL (spray dryer) and ACPTL (MEE).

vi Reuse/Recycle details (KL/day) -

B Air(Existing and Proposed)

Page 53 of 126


Page 53 of 126


-

SR. no.

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

Emission Standard

1

Non IBR Boiler

(400 kg/hr)

9 m HSD 70

Lit/Day

PM SO₂ NOX

Adequate stack height

150 mg/Nm³ 100 ppm 50 ppm

Proposed Stacks

Non IBR Boiler

(400 kg/hr)

9 m HSD 70

Lit/Day

PM SO₂ NOX


150 mg/Nm³ 100 ppm 50 ppm

Thermopack (1 L Kcal)

12 m

HSD

100 Lit/Day

PM SO₂ NOX


150 mg/Nm³ 100 ppm

50 ppm

D.G.SET

(65 KVA) 7 m

HSD

25 lits/Day

PM SO₂ NOX


150 mg/Nm³ 100 ppm

50 ppm

-

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

-

Sr. no.

Source of emission

Type of emission


A CM

1 Vent Attached to Reactor

SO2 HCl HBr

10 Alkali Scrubber

-

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

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

i

Sr. no.



Category and Schedule as per HW Rules

Quantity (MT/ Annum)

Disposal Method

1 ETP Sludge ETP 35.3 10.2 TPA Collection, storage, transportation and send to TSDF site

2 Process waste (wet cake)

Process 28.1 5.9 TPA Collection, storage, transportation and send to TSDF site

3 Used oil

Plant machineries

5.1

27 lit/yr Collection storage, transportation and sell to GPCB authorized recyclers/ reused in

Page 54 of 126


Page 54 of 126

machineries as lubricants. 4 Discarder

Containers/ Barrels

Storage area

33.1 12000 Nos./yr

Collection, storage, transportation and sell to GPCB authorized vendors.

5 Caustic Lye Dilute

Process -

1200 TPA

Collection, storage, transportation and sell to GPCB authorized end users.

6 Spent Solvent

Process 28.6 304 TPA Collection, storage, transportation and send for recovery

7 Spent Carbon

Process 28.3 0.072 TPA

Collection, storage, transportation and send to GPCB authorized recovery or TSDF.

8 Process waste

(Nickel, Piperazine, N-Hexane, HBr)

Process 28.1 249.7 TPA

Collection, storage, transportation and send to GPCB authorized recovery.


ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.

CETP: PETL CETP: PETL (Spray dryer) Common MEE: ACPTL TSDF: SEPPL


None

D

i Spent Solvent management (If any) Spent solvent will be sent to GPCB authorized re-processors.

ii VOC emission sources and its mitigation measures Scrubbing stem is proposed.

• Technical presentation was made by the project proponent. PP has proposed to send entire

quantity of waste water to Common MEE of M/s: ACPTCL, Ankleshwar.Committee discussed about

LDAR and hazardous waste management.






1. Adequacy of proposed area with respect to plant machineries , EMS, green belt , safety

aspect, raw material & product storage considering worst case scenario. Submit proper lay

out plan clearly demarcating all activities with scale.

2. PP shall prepare detailed Leak Detection and Repairing Programme (LDAR) for all the

volatile organic solvent proposed for use in-house with detailed chemical properties

including vapour pressure. LDAR shall endeavour prevention of losses of solvents to the

Page 55 of 126


Page 55 of 126

best minimum extent.





2006.



8. SIA/GJ/IND2/21559/2018 M/s. Kohinoor Colours Pvt Ltd Plot No. 7204 &7205, GIDC, Ankleshwar, Dist.: Bharuch.

Screening & Scoping







as tabulated below:

Sr. no.


CAS no. / CI no.

Quantity (MT/Month) End-use of the products Existing Proposed Total

1. Diethyl Meta Amino Phenol

91-68-9 8.0 50 58 Use as Dyes intermediate

2. N,N, Diethyl Metanilic Acid

97-20-1 0.0 20 20 Use as Dyes intermediate

3. Meta Amino Phenol 594-27-5 0.0 20 20 Use as Dyes intermediate

4. Rhodamine Liquid (Minimum 10% To 40% Maximum) and/or

64-19-7 0.0 50.0 50.0 Use as Dyes in Paper, ink etc.

5 Auramine O Liquid (Minimum 20% To 50% Maximum)

2465-27-2 0.0 50.0 50.0 Use as Dyes in Paper, ink etc.


2006



project proponent.

• Salient features of the project are as under::

Sr. no

Particulars Details

A Total cost of Proposed Project Existing: 157 Lacs. Proposed: 300 Lacs.

Page 56 of 126


Page 56 of 126

(Rs. in Crores): Total: 457 Lacs.


Existing: 2000 Sq. m. Proposed: Nil Total: 2000 Sq. m.


Existing: 35 Sq. m. Proposed: 570 Sq. m. Total: 605 Sq. m.

C Employment generation 1. Direct Existing: 15

Proposed: 35

Total: 50

2. Indirect Existing: 3

Proposed: 6

Total: 9

D Water i


GIDC

Status of permission from the concern authority. GIDC permission letter obtained.


Existing KLD



Remarks

(A) Domestic 1.0 3.0 4.0

(B) Gardening 0.0 2.0 2.0

Industrial

Process 1.0 7.0 8.0

Washing 4.0 24.0 28.0

Boiler 1.0 5.0 6.0

Cooling 0.0 1.0 1.0

Others 0.0 0.0 0.0

Industrial Total 6.0 37.0 43.0

Grand Total (A+B+C)

7.0 42.0 49.0








Remarks

(A) Domestic 0.8 3.0 3.8

Industrial

Process 0.5 4.0 4.5

Washing 4.0 23.0 27.0

Boiler 0.0 0.5 0.5

Cooling 0.0 0.1 0.1

Others 0.0 0.0 0.0


4.5 27.6 32.1

-

Page 57 of 126


Page 57 of 126


ETP and MEE (Multi Effect Evaporator) Capacitate:- 30 KL/Day Existing ETP:- Primary + Secondary +Tertiary Proposed ETP:- Existing + MEE


Domestic:Disposal through septic/soak pit system

Industrial: -[Existing]

For the existing production capacity, the

generated waste water is collected, treated into

ETP, and then discharge to G.I.D.C. underground

drainage system and conveyed to FETP which

ultimately leads to deep sea for final disposal

through BEAIL pipeline.

[Proposed]

For proposed expansion, there will be

increase in the waste water generation from the

process and utility, washing sections and this

generated waste water will be treated into ETP and

then sent to Multi Effect Evaporator, condensate

water will be reuse within the plant premises.

Hence, for the proposed expansion, generated

additional waste water will have zero discharge

and there will not be any increase in the

consented discharge quantity.


Not Applicable

Membership of CF Member of NCTL-ETL Ankleshwar Certificate obtained.

vii Reuse/Recycle details (KLD) 23 KL/Day


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


Type of emissions i.e. Air

Pollutants


Measures (APCM)

Existing

1. Boiler 10 m Natural Gas

[90m3/day

]

PM SO2 NO2

--

Proposed

Page 58 of 126


Page 58 of 126

1. Boiler [600 Kg/ Hr.] [2 Nos.]

10 m each

Natural Gas

and/or Bio-coal

[400 m3/Day.] and/or

[1.4 MT/Day]

PM SO2 NO2

Cyclone Separator

+ Water

Scrubber

2. G.G. Set (63KVA) (Stand By)

2 m Natural Gas

[80 m3/Day]

PM SO2 NO2

------

-

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) [Existing & Proposed] – There is no any process gas emission from existing products as well as Process gas emission.

iii Fugitive emission details with its mitigation measures. [Existing & Proposed]KAs below: Not Applicable


i

Sr. no.




Quantity (MT/Annum)

Disposal Method

1. Used Oil Machinery Section

5.1 0.0241 MT Collection, Storage, Transportation and sold to authorized Recyclers.

2. Discarded containers

Packing Section

33.1 3.2 MT Collection, Storage, Decontamination or sold to authorized recycler.

3. ETP Waste/MEE solid waste (Potassium Sulphate & Sodium Sulphate)

ETP/MEE 26.2 1204.8 MT

Collection, Storage, Transportation and sent TSDF site.


ii Membership details of TSDF, CHWIF etc. Member of BEIL-TSDF-Ankleshwar. Certificate attached as Annexure-C.


Not Applicable




• Technical presentation was made by the project proponent.Committee observed that existing

quantity of effluent will be discharged to FETP after treatment and additional effluent will be

subjected to ETP followed by MEE system. Hence, there will be no qualitative or quantitative

Page 59 of 126


Page 59 of 126

increase in waste water discharge to FETP. PP has proposed drying of Wet Cake of Dyes, Liquid

Dyes from wet Cake of Dyes & repacking of Dyes and Pigments which are not falling in schedule to

the EIA Notification 2006. Upon asking, PP agreed to remove these products and submitted details

with relevant changes. Committee asked PP to obtain CTE-CCA from GPCB.






1. 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.

2. Adequacy of MEE system considering worst case scenario.





2006.



9. SIA/GJ/IND2/19090/2017 M/s. Spectrum Dyes & Chemicals Pvt. Ltd.

Plot No. DP/3 to DP/7, DP/75 to DP/78, DP/90, Sayakha GIDC,Village: Sayakha, Ta: Vagra, Dist.: Bharuch

Screening & Scoping


Project status: New



report.

• This is anew unit proposes for Synthetic Organic manufacturing as tabulated below:

No. Name of the product CAS no./

CI no* Quantity in MT/Month

End-use of product

A Dyes * Dyeing

1 SYNTHETIC ORGANIC DYES-1 3400

AZO Disperse Dyes (T-1)

Disperses Dyes (T-2)


AZO Disperse Dyes (T-3)


Dyes

1 DisperseYellow4 6407-80-3

Page 60 of 126


Page 60 of 126



















































Page 61 of 126


Page 61 of 126















66 DisperseYellow184.1 164578-37-4






























96 DisperseGreen9 58979-46-7

97 DisperseGreen7 71819-65-3

98 DisperseOrange5 6232-56-0




Page 62 of 126


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110 DisperseOrange25.1 31464-38-7










































Page 63 of 126


Page 63 of 126


153 DisperseOrange128 NA











164 DisperseRed2 76927-82-7












176 DisperseRed20 NA

177 DisperseRed21 37220-20-5


179 DisperseRed25 1228753-15-8





184 DisperseRed33 1228753-16-9

185 DisperseRed35 61951-62-0



188 DisperseRed43 12217-85-5


190 DisperseRed50 40880-51-1


192 DisperseRed52 104491-85-2

193 DisperseRed53 59787-78-9


195 DisperseRed55 17869-07-7

196 DisperseRed56 12637-13-7



199 DisperseRed59 17869-10-2

200 DisperseRed60 17418-58-5

201 DisperseRed61 71807-43-7

Page 64 of 126


Page 64 of 126


203 DisperseRed63 164578-06-7


205 DisperseRed65 16586-43-9


207 Disperse Red67 NA

208 Disperse Red68 61356-32-9


210 Disperse Red70 1262788-93-1

211 Disperse Red71 17418-58-5

212 Disperse Red72 12223-39-1

213 Disperse Red73 16889-10-4

214 Disperse Red74 61703-11-5

215 Disperse Red75 61725-14-2

216 Disperse Red76 12236-07-6




220 Disperse Red80 12236-08-7

221 Disperse Red 81 12223-41-5

222 Disperse Red82 30124-94-8

223 Disperse Red83 17418-58-5

224 Disperse Red84 12217-88-8

225 Disperse Red85 12217-89-9

226 Disperse Red86 81-68-5

227 Disperse Red87 12223-44-8

228 Disperse Red88 12217-04-8

229 Disperse Red89 12223-45-9

230 Disperse Red90 27767-98-2

231 Disperse Red91 34231-26-0

232 Disperse Red92 72363-26-9

233 Disperse Red93 12236-12-3

234 Disperse Red96 12223-47-1

235 Disperse Red98 61994-66-9


237 Disperse Red107 12236-16-7

238 Disperse Red109 84560-05-4

239 Disperse Red113 12223-59-5

240 Disperse Red117 12223-59-5

241 Disperse Red118 61480-15-7

242 Disperse Red120 12236-19-0

243 Disperse Red121 12223-62-0

244 Disperse Red122 12223-63-1

245 Disperse Red125 12236-20-3

246 Disperse Red127 66795-75-3

247 Disperse Red128 12236-22-5

248 Disperse Red129 12236-23-6

249 Disperse Red131 12236-24-7

250 Disperse Red132 12223-67-5

251 Disperse Red134 12223-69-7

Page 65 of 126


Page 65 of 126

252 Disperse Red135 29765-00-2

253 Disperse Red136 12223-70-0

254 Disperse Red137 73384-74-4

255 Disperse Red139 71832-05-8

256 Disperse Red140 58051-97-1

257 Disperse Red141 61968-45-4

258 Disperse Red143 20339-55-3

259 Disperse Red145 25510-81-0

260 Disperse Red146 59763-30-3

261 Disperse Red152 78564-86-0

262 Disperse Red153 78564-87-1

263 Disperse Red154 73384-65-3

264 Disperse Red155 71819-69-7

265 Disperse Red156 25473-34-1

266 Disperse Red157 118548-22-4

267 Disperse Red158 61968-48-7

268 Disperse Red159 61968-49-8

269 Disperse Red160 61968-50-1

270 Disperse Red163 71819-70-0

271 Disperse Red164 80892-58-6

272 Disperse Red165 1914998-77-8

273 Disperse Red167 26850-12-4

274 Disperse Red167.1 1533-78-4


276 Disperse Red177 68133-69-7

277 Disperse Red178 61951-63-1

278 Disperse Red179 16586-42-8

279 Disperse Red180 61951-65-3

280 Disperse Red181 86438-38-2

281 Disperse Red183 83764-36-7

282 Disperse Red184 61968-54-5

283 Disperse Red185 61901-71-1



286 Disperse Red189 934539-45-4

287 Disperse Red190 82230-10-2

288 Disperse Red191 103657-51-8

289 Disperse Red192 89072-61-7

290 Disperse Red193 26692-47-7

291 Disperse Red194 78564-87-1


293 Disperse BRILL BLUE ECB EX. CONC NA

294 Disperse Red196 82944-36-3


296 Disperse Red198 61968-55-6

297 Disperse Red199 6371-23-9

298 Disperse Red200 332137-64-1

299 Disperse Red201 61931-38-2

300 Disperse Red202 28462-17-1

301 Disperse Red203 61968-56-7

Page 66 of 126


Page 66 of 126


303 Disperse Red207 159131-66-5

304 Disperse Red210 13301-60-5

305 Disperse Red211 12236-22-5


307 Disperse Red214 90585-55-0


309 Disperse Red220 65907-69-9

310 Disperse Red221 64426-35-3

311 Disperse Red224 63641-91-8

312 Disperse Red225 103938-55-2

313 Disperse Red227 224966-20-5


315 Disperse Red258 73384-67-5

316 Disperse Red271 71832-08-1

317 Disperse Red272 80206-94-6


319 Disperse Red274 83929-87-7


321 Disperse Red276 71832-09-2

322 Disperse Red277 70294-19-8

323 Disperse Red278 61355-92-8

324 Disperse Red279 72827-94-2



327 Disperse Red282 155522-12-6

328 Disperse Red283 120797-62-8


330 Disperse Red288 77907-27-8

331 Disperse Red302 40530-60-7

332 Disperse Yellow UNXF NA

333 Disperse Red303 71872-53-2

334 Disperse Red305 89106-92-3

335 Disperse Red311 77907-28-9

336 Disperse LUMINOUS RED J NA


338 Disperse Red313 72827-95-3



341 Disperse Red316 83929-88-8

342 Disperse Red319 25510-81-0

343 Disperse Red323 73384-66-4

344 Disperse Red324 71617-28-2

345 Disperse Red329 87714-24-7


347 Disperse Red333 110342-28-4

348 Disperse Rubine UNXF NA

349 Disperse Red334 59970-81-9



Page 67 of 126


Page 67 of 126

352 Disperse Red338 63134-15-6


354 Disperse Red340 88264-87-3




358 Disperse Red353 94945-22-9

359 Disperse Red354 79300-13-3

360 Disperse Red356 159968-00-0

361 Disperse Red359 92818-48-9

362 Disperse Red361 16294-75-0

363 Disperse Red364 522-75-8


365 Disperse Red371 881997-87-1


367 Disperse Red376 524711-99-7

368 Disperse Red377 460987-35-3

369 Disperse Red378 947172-35-2

370 Disperse Red382 946850-26-6

371 Disperse Red383 22145-67-1

372 Disperse RED 4B NA

373 Disperse BLUE MD NA

374 Disperse Blue4 225918-97-8





379 Disperse Blue10 885474-83-9


381 Disperse Blue13 NA




385 Disperse NAVY BLUE 2GS EX-CONC. NA











396 Disperse GOLDEN YELLOW 2GNN NA





401 Disperse Red UNXF NA

Page 68 of 126


Page 68 of 126








409 Disperse Blue79.1 3618-72-2









418 Disperse Blue118 20241-77-4

419 Disperse Blue120 20241-76-3

420 Disperse Blue122 12270-38-1

421 Disperse Blue125 66693-26-3

422 Disperse Blue127 68310-48-5

423 Disperse Blue128 12270-41-6

424 Disperse Blue130 61968-27-2

425 Disperse Blue132 61902-08-7

426 Disperse Blue134 14233-37-5

427 Disperse Blue135 1228754-32-2

428 Disperse Blue139 50922-60-6


430 Disperse Blue141 1262789-72-9



433 Disperse Blue144 64553-76-0

434 Disperse Blue146 26931-40-8

435 Disperse Blue148 52239-04-0

436 Disperse Blue149.1 NA

437 Disperse Blue150 61951-53-9

438 Disperse Blue152 71819-61-9

439 Disperse Blue153 61815-13-2


441 Disperse Blue158 16618-09-0

442 Disperse Blue165 41642-51-7

443 Disperse Blue165.1 24170-60-3

444 Disperse Blue171 73299-32-8

445 Disperse Blue173 61867-90-1

446 Disperse Blue174 58694-33-0


448 Disperse Blue176 61968-33-0

449 Disperse Blue180 69912-84-1

450 Disperse Blue181 71872-42-9


Page 69 of 126


Page 69 of 126

452 Disperse Blue185 61968-36-3

453 Disperse Blue186 66795-74-2

454 Disperse Blue187 104491-83-0

455 Disperse Blue197 82230-08-8

456 Disperse Blue198 82230-09-9

457 Disperse Blue200 69070-68-4

458 Disperse Blue201 163751-71-1

459 Disperse Blue207 885470-94-0

460 Disperse Blue211 885473-15-4

461 Disperse Blue214 104491-84-1

462 Disperse Blue224 95078-18-5

463 Disperse Blue225 145537-86-6

464 Disperse Blue257 84931-03-3

465 Disperse Blue259 82457-20-3

466 Disperse Blue264 885473-58-5

467 Disperse Blue266 58204-91-4

468 Disperse Blue268 58049-96-0

469 Disperse Blue270 88650-95-7

470 Disperse Blue280 71902-09-5

471 Disperse Blue281 137573-90-1

472 Disperse Blue283 71819-63-1

473 Disperse Blue284 71872-43-0

474 Disperse Blue291 56548-64-2

475 Disperse Blue291.1 51868-46-3

476 Disperse Blue295 71872-47-4

477 Disperse Blue297 100358-00-7

478 Disperse Blue301 105635-65-2

479 Disperse Blue305 885473-80-3

480 Disperse Blue319 69828-87-1

481 Disperse Blue320 83929-85-5

482 Disperse Blue327 83929-86-6

483 Disperse NAVY HW-EFR NA

484 Disperse Blue328 885474-00-0

485 Disperse Blue330 87658-81-9

486 Disperse Blue331 99148-93-3

487 Disperse Blue333 88385-23-3

488 Disperse Scarlet UNXF NA


490 Disperse Blue335 63134-10-1

491 Disperse Blue336 885474-01-1

492 Disperse Blue UNXF NA

493 Disperse Blue337 65916-12-3

494 Disperse Blue338 68900-95-8

495 Disperse Blue339 54289-46-2

496 Disperse Blue341 73275-65-7

497 Disperse Blue344 885474-07-7

498 Disperse Blue346 885474-32-8

499 Disperse Blue347 910459-93-7


501 Disperse BRILL. PINK BRF 300% NA

Page 70 of 126


Page 70 of 126


503 Disperse Blue350 94945-20-7

504 Disperse Blue351 885474-33-9

505 Disperse Blue352 885474-36-2

506 Disperse BRILL RED 6B NA

507 Disperse Blue353 82457-22-5

508 Disperse Blue354 74239-96-6

509 Disperse YELLOW BROWN RD / goL YELL rd

NA

510 Disperse Blue355 885474-48-6

511 Disperse Blue356 118578-14-6

512 Disperse Blue359 213328-78-0

513 Disperse Pink UNXF NA

514 Disperse Blue360 885474-63-5

515 Disperse Blue361 93686-63-6


517 Disperse Blue364 108948-37-4

518 Disperse Blue365 108948-36-3

519 DisperseCYANINE VIOLET XF NA

520 Disperse Blue366 84870-65-5

521 Disperse Blue367 105076-77-5

522 Disperse Blue368 96293-52-6

523 Disperse Blue369 122063-39-2

524 Disperse Blue370 106359-94-8

525 Disperse Blue371 885474-68-0


527 Disperse BLUE HW-10GS / BLUE A NA

528 Disperse Blue373 51868-46-3

529 Disperse CYANINE PINK NA

530 Disperse Blue374 885474-73-7

531 Disperse Blue375 885474-74-8

532 Disperse Blue376 885474-75-9

533 Disperse Blue377 67674-26-4

534 Disperse Blue378 885474-76-0


536 Disperse Blue380 1107654-03-4

537 Disperse VIOLET MD NA

538 Disperse Violet1 128-95-0



541 Disperse Violet UNXF NA


543 Disperse Violet5


545 Disperse Violet7 NA






Page 71 of 126


Page 71 of 126


552 Disperse VIOLET HW - BFS NA



555 Disperse RUBINE HW - EFB NA









564 Disperse RED VIOLET XF NA




568 Disperse YELLOW BROWN MD NA






574 Disperse SCARLET RD - 2G NA



577 Disperse Black UNXF NA




581 Disperse Violet UNXF NA


583 Disperse Violet93.1 122463-28-9








591 Disperse SCARLET XF NA

592 Disperse Orange UNXF NA

Anthraquinone Solvent Dyes

593 Solvent Yellow 14 842-07-9





598 Solvent Orange 60 6925-69-5


Page 72 of 126


Page 72 of 126



602 Solvent Orange 105 31482-56-1

603 Solvent Violet 14 8005-40-1




607 Solvent Blue 4 6786-83-0

608 Liquid Red 1 92257-31-3

609 Liquid Yellow 1 29190-28-1 +

610 Automate Black 1XS 74499-36-8 +

611 Automate Blue 8A 74499-36-8

612 Automate Blue 8AHF 74499-36-8



615 Solvent Yellow 42 NA














629 Solvent Yellow 124 34432-92-3

630 Solvent Yellow 126 61968-70-5

631 Solvent Yellow 131 71819-82-4

632 Solvent Yellow 135 68427-35-0

633 Solvent Yellow 141 83929-90-2

634 Solvent Yellow 142 NA

635 Solvent Yellow 160.1 35773-43-4

636 Solvent Yellow 163 13676-91-0

637 Solvent Yellow 171 27425-55-4

638 Solvent Yellow 172 80748-21-6

639 Solvent Yellow 179 80748-21-6


641 Solvent Orange 23 NA




645 Solvent Orange 107 NA

646 Solvent Red 1 6535-42-8

647 Solvent Red 2 5098-94-2

648 Solvent Red 3 6535-42-8

649 Solvent Red 8 33270-70-1

Page 73 of 126


Page 73 of 126

650 Solvent Red 23 85-86-9

651 Solvent Red 24 85-83-6

652 Solvent Red 26 4477-79-6

653 Solvent Red 49 509-34-2

654 Solvent Red 52 81-39-0

655 Solvent Red 68 NA

656 Solvent Red 89 61725-81-3

657 Solvent Red 91 61901-92-6

658 Solvent Red 92 61901-93-7

659 Solvent Red 111 82-38-2

660 Solvent Red 119 12237-27-3

661 Solvent Red 122 12227-55-3

662 Solvent Red 125 12271-00-0

663 Solvent Red 127 77496-01-6

664 Solvent Red 130 71839-77-5

665 Solvent Red 135 71902-17-5

666 Solvent Red 149 21295-57-8

667 Solvent Red 155 110616-99-4

668 Solvent Red 175 ENCS No. 5-5084

669 Solvent Red 179 6829-22-7

670 Solvent Red 196 52372-36-8

671 Solvent Red 197 52372-39-1






677 Solvent Blue 18 2475-45-8

678 Solvent Blue 35 17354-14-2

679 Solvent Blue 36 14233-37-5

680 Solvent Blue 37 3861-73-2

681 Solvent Blue 38 1330-38-7

682 Solvent Blue 48 61711-30-6

683 Solvent Blue 58 29887-08-9

684 Solvent Blue 59 6994-46-3

685 Solvent Blue 60 NA

686 Solvent Blue 67 81457-65-0

687 Solvent Blue 68 4395-65-7

688 Solvent Blue 68 4395-65-7

689 Solvent Blue 78 2475-44-7

690 Solvent Blue 93 2475-44-7

691 Solvent Blue 97 32724-62-2

692 Solvent Blue 98 71819-49-3

693 Solvent Blue 102 15403-56-2

694 Solvent Blue 104 116-75-6

695 Solvent Blue 108 ENCS # 5-3129

696 Solvent Blue 109 ENCS # 5-5132

697 Solvent Blue 122 67905-17-3

698 Solvent Green 3 128-80-3

699 Solvent Green 7 6358-69-6

Page 74 of 126


Page 74 of 126

700 Solvent Green 20 28198-05-2

701 Solvent Green 28 71839-01-5

702 Solvent Black 7 68389-53-7

703 Solvent Black 13 NA

704 Solvent Black 27 12237-22-8

705 Solvent Black 28 12237-23-9

706 Solvent Black 29 61901-87-9

707 Solvent Black 35 61931-53-1

708 Solvent Black 29 61901-87-9

709 Solvent Black 45 94765-62-5

710 Solvent Black 46 65294-17-9

711 Solvent Black UNXF NA

712 Automate Blue 9HF 29887-08-9 +

713 Automate Brown 2XS 74499-36-8 +

714 Automate Brown 2HF XS 74499-36-8 +

715 Automate Green MX 74499-36-8 +

716 Automate Green HF MX 74499-36-8 +

717 Solvent Violet UNXF NA

718 Marker 1 111850-24-9

719 Marker 2 124719-26-2

720 Marker 3 64742-94-5

721 Marker 4 NA

722 Marker 5 NA

723 Marker 6 111850-24-9 +

724 Marker 8 NA

725 Solvent Violet UNXF NA

726 Automate Yellow 8HF 29190-28-1 +

727 Automate Bronze 1XS 29190-28-1 +

728 Automate Orange 2XS 29190-28-1 +

729 Automated Red GXS 92257-31-3 +

730 Automate Orange 2HFXS 92257-31-3 +

731 Automate Purple XS 92257-31-3 +

732 Automate Red 10BXS 92257-31-3 +

733 Automate Red 9BHF 92257-31-3 +

734 Automate Red IKHF 92257-31-3 +

735 Automate Red IKHF D50 92257-31-3 +

736 Liquid Red Dye #3 92257-28-8

737 Solvent Pink UNXF NA

738 Marker 6 111850-24-9 +

739 Mod "0" Powder 70879-65-1 +

740 Mod "0" WPC 70879-65-1 +

741 Mod "12" Powder 70879-65-1 +

742 Solvent Rubine UNXF NA

743 Liquid Red 1 92257-31-3

744 Liquid Red 2 70879-65-1 +

745 Liquid Yellow 1 29190-28-1 +

746 Liquid Red 3 92257-28-8

747 Liquid Red 4 NA

748 Solvent Red UNXF NA

749 Liquid Red 5 NA

Page 75 of 126


Page 75 of 126

750 Solvent Blue UNXF NA

751 Marker 7 56358-17-9

752 Solvent Scarlet UNXF NA

753 Liquid Blue 4 NA

754 Liquid Yellow 2 97660-72-5

755 T BPAA 2 108313-21-9

756 Automate Red PB XF 92257-28-8 +

757 Automate Blue RB 295800-70-3

758 Automate Blue RB 2 295800-70-3 +

759 Solvent Orange UNXF NA

Vat Dyes

760 Vat Yellow 2 129-09-9

761 Vat Yellow 33 12227-50-8

762 Vat Yellow 46 40783-05-9

763 Vat Black UNXF NA

764 Vat Orange 1 1324-11-4

765 Vat Orange 2 1324-35-2

766 Vat Orange 9 128-70-1

767 Vat Orange 11 2172-33-0

768 Vat Orange 15 2379-78-4

769 Vat Orange 29 71459-28-4

770 Vat Red UNXF NA

771 Vat Red 10 2379-79-5

772 Vat Red 13 4203-77-4

773 Vat Violet UNXF NA

774 Vat Violet 1 1324-55-6

775 Vat Violet 9 1324-17-0

776 Vat Violet 13 4424-87-7

777 Vat Violet UNXF NA

778 Vat Blue 4 81-77-6

779 Vat Blue 6 130-20-1

780 Vat Blue 16 6424-76-6

781 Vat Blue 18 1324-54-5

782 Vat Blue 19 1328-18-3

783 Vat Blue 20 116-71-2

784 Vat Blue 22 6373-20-2

785 Vat Orange UNXF NA

786 Vat Green 1 128-58-5

787 Vat Green 3 3271-76-9

788 Vat Green 9 6369-65-9

789 Vat Green 26 NA

790 Vat Scarlet UNXF NA

791 Vat Brown 3 131-92-0

792 Vat Brown 11 NA

793 Vat Brown 33 70210-15-0

794 Vat Pink UNXF NA

795 Vat Black 16 1328-19-4

796 Vat Black 25 4395-53-3

797 Vat Black 27 2379-81-9

798 Vat Black 34 12271-03-3

Page 76 of 126


Page 76 of 126

799 Vat Rubine UNXF NA

800 Vat Blue UNXF NA

B Dyes Intermediates To manufacture dyes

(i) Anthroquinone based Intermediate (Indicative List)

100

1 1-Amino anthraquinone 82-45-1

2 1,4-Dihydroxyanthraquinone 81-64-1

3 Bromaminic acid 116-81-4

4 1-Amino-2-bromo-4-hydroxy-9,10-anthraquinone

116-82-5

5 3,10-diamino-6,13-dichloro-5,12-dioxa-7,14-diazapentacene-4,11-disulfonic acid

98210-99-2

6 1,4-DIAMINO-2,3-DICYANO-9,10-ANTHRAQUINONE

81-41-4

7 1,4-Diaminoanthracene-9,10-Diol 5327-72-0

8 1,8-Dihydroxy-4,5-dinitroanthraquinone 81-55-0

9 4,11-diamino-1H-naphth[2,3-f]isoindole-1,3,5,10(2H)-tetrone

128-81-4

10 3-Hydroxy-2-methyl-4-quinolinecarboxylic acid

117-57-7

11 1-Chloro anthraquinone 82-44-0

12 1,5-Diaminoanthraquinone 129-44-2

13 1,5-DICHLOROANTHRAQUINONE 82-46-2

14 1,8-DICHLOROANTHRAQUINONE 82-43-9

15 1,4-diamino-2,3-dichloroanthracene-9,10-dione

81-42-5

16 1-amino-2,4-dibromoanthracene-9,10-dione 81-49-2

17 1,5-Dihydroxy-4,8-dinitroanthraquinone 128-91-6

18 3-AMINO-2-METHYLQUINOLINE-4-CARBOXYLIC ACID

71881-80-6

19 2-METHYL-QUINOLINE-4-CARBOXYLIC ACID

634-38-8

20 1,4-Diamino-2,3-dihydroanthraquinone 81-63-0

21 1,5-diamino-4,8-dihydroxyanthracene-9,10-dione

145-49-3

22 1 8-DIAMINO-4 5-DIHYDROXYANTHRAQUINONE

128-94-9

23 1,4-diamino-9,10-dioxo-9,10-dihydroanthracene-2,3-disulfonic acid

65596-11-4

(ii) Halogenated Primary Amines (Indicative List)

500

1 6-Br-2,4-DNA 1817-73-8

2 6-Cl-2,4-DNA 3531-19-9

3 CBPNA 17601-94-4

4 Bromophthalimides NA

5 DCA 95-76-1

6 DCPT 56461-98-4

7 DBPT 6968-24-7

8 DCPNA 91-67-8

9 DBPNA 827-94-1

10 BrCNPNA 17601-94-4

11 TBA 147-82-0

Page 77 of 126


Page 77 of 126

(iii) Tertiary Amines (Indicative List) 900

SD-01, SD-01A, SD-1.2, SD-1M, SD-01EC, SD-02, SD-02A, SD-2.2, SD-2M, SD-03, SD-03A, SD-3.2, SD-3M, SD-4, SD-04A, SD-4.2, SD-4M, SD-5A, SD-05, SD-5.2, SD-5M ,SD-6A, SD-6CN, SD-6CE, SD-6, SD-07CN, SD-07A, SD-7AC, SD-7B, SD-07, SD-7M, SD-7.2, SD-08, SD-8.2, SD-8M, SD-09, SD-9.2, SD-9M, SD-10CN, SD-10, SD-10BC, SD-11CN, SD-11A ,SD-11, SD-11.2, SD-11M, SD-11AC, SD-12 ,SD-12.1, SD-12BC, SD-13, SD-14 ,SD-14A, SD-14CN, SD-14.2, SD-14M, SD-15, SD-15A ,SD-15B, SD-16, SD-16A, SD-17, SD-18, SD-19, SD-19A, SD-20, SD-21 ,SD-22, SD-23, SD-24, SD-25, SD-26, SD-27, SD-29, SD-31, SD-35, SD-34B, SD-34P, SD-37, SD-38, SD-39, SD-40, SD-41, SD-50, SD-51, SD-53, SD-54, SD-55, SD-56, DT-100, MP, HMQ, OA-Omega, Aniline Omega,++

92-00-2, 101510-32-1, 103-06-0, 1075-76-9, 119-95-9,

120-07-0, 148-69-6, 148-87-8, 1555-66-4, 1677-46-9, 17754-90-4, 186453-43-0, 18934-20-8, 19249-34-4, 19433-93-3, 19433-94-4

,21608-06-0, 21615-36-1, 21678-63-7, 21678-64-8, 22031-33-0, 22185-75-7, 22588-78-9, 23128-51-0, 24294-01-7, 24294-03-9, 24530-67-4, 25047-90-9, 26322-20-3, 26408-28-6, 26692-46-6, 26841-42-9, 27059-08-01, 27419-90-5, 28321-56-4, 28505-89-7, 29103-58-0, 29333-76-4, 38954-40-4, 39240-08-9, 51228-92-3, 51868-45-2, 51920-03-7, 52603-47-1, 53733-94-1, 55379-84-5, 61038-96-8, 62072-82-6, 62323-09-5, 6247-00-3, 6375-46-8, 67338-58-3,

67892-95-9, 68189-36-6, 73862-13-2, 74228-24-3,

87182-67-0, 91-67-8, 91-88-3, 91-99-6, 92-02-4, 92-50-

2,92-64-8, 92-79-5, 93-13-0, 94-89-3, NA -

(iv) Primary Amines (Indicative List) 750

1 PNA 106-47-8

2 2,4DNA 121-87-9

3 MAA 102-28-3

4 GP Base 96-96-8

5 MPDA 108-45-2

6 OCPNA 121-87-9

7 AMA 6375-47-9

(v) Other Intermediates (Indicative List) 150

1 DEMAP 91-68-9

2 MAP 591-27-5

3 MHA 1829-82-9

4 MHAL 1829-82-9

5 MAMS 37045-73-1

6 PNBA Ester NA

7 EP 28141-13-1

8 SO-3 NA

9 BP 39108-47-9

10 IOA NA

11 DMP 39621-10-8

12 DCPSL NA

13 IP 68612-94-2

14 Pyridone 5444-02-0

15 Pyridine 110-86-1

16 SD-33 NA

17 DCDAAQ NA

Page 78 of 126


Page 78 of 126

18 FB 118-12-7

19 SRT NA

20 CMB 4414-88-4

21 AQ-1 NA

22 SD-28 614-27-7

23 MYC NA

24 SD-30 1127-35-1

25 2-Amino Thiophene 616-46-6

26 SBD NA

27 2-Chlorothiophene 96-43-5

28 3,5-Dinitro-2-Aminothiophene 2045-70-7

29 SD-36 NA

30 2-amino-5-nitrobenzothioamide 25026-97-5

31 ST-1 NA

32 1-(4-nitrophenyl)thiourea 3696-22-8

33 1-(4-methoxyphenyl)thiourea 2293-07-4

34 MSD NA

C Dispersing Agent 2500

α /β, NaphthaleneFormaldehydeCondensate

Phenol / Cresol Formaldehyde Condensate

Sodium LignoSuphonate Condensate

1 NKS 9084 - 06 -4

2 TK-85 8061-51-6

3 Dyetol DF 9003-25-

D Nitrosyl Sulphuric Acid 7782-78-7 600

E Optical Brightening Agent 13001-40-6, ++ 100

TOTAL DYES AND DYE INTERMEDIATE PRODUCTION 9600

F Captive Power Plant 4 MW


2006



project proponent.


Sr. no.

Particulars Details

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

Rs. 278.95 Crore

B Total Plot area ( sq. meter) 1,26,050.02 sq. m..


41,805 sq.m.


Direct : 1200 nos. Indirect: 300 nos.

D Water i


GIDC-Sayakha

Status of permission from the concern authority. Letter obtained from GIDC


Page 79 of 126


Page 79 of 126

-

Category

KLD Remarks

(J) Domestic 100 Fresh water

(K) Gardening 20 Total requirement is 105 KL in which 85 KL reuse from treated sewage wastewater and 20 KL freshwater

(L) Industrial

Process 3000 -

Washing 21 Used for Drum & Floor washing

Boiler 1010 -

Cooling 384 -

Others 20 Dust suspension at coal storage area and within plant premises etc.

Industrial Total 4435 Fresh and treated water

Total (A + B + C) 4555 -

1) Total water requirement for the project: 4555 KLD 2) Quantity to be recycle: 3557 KLD 3) Total fresh water requirement: 998 KLD


-

Category Waste water KLD

Remarks

(E) Domestic 85 Treated in STP

(F) Industrial

Process 3103 Low COD stream

Washing 21 -

Boiler 141 -

Cooling 235 -

Others - -


3500 Treated in ETP followed by RO and MEE

-


• Solvent containing stream will be stripped out in in-

house solvent stripper. Recovered solvent will be

reused in process and remaining mass will be washed

with water, which will be treated in ETP.

• Wastewater from process, washing, boiler and cooling

having low COD. It will be treated in ETP followed by

RO plant and MEE.

• RO permeate (2100 KLD) and MEE condensate (1372

KLD) will reuse to process.

• Treated effluent will not be disposed outside the

premises to achieve Zero Liquid Discharge (ZLD).

• Sewage from domestic activities will be treated in STP of capacity 100 KLD. Treated STP water (85 KLD) will be reused to process.


• Domestic: treated in STP and treated water will be reuse for greenbelt

Page 80 of 126


Page 80 of 126

• Industrial: Zero Liquid Discharge.


Common Hazardous Waste Incineration Facility (CHWIF)

Membership of Common facility (CF) Will be obtained after ToR.

vii Reuse/Recycle details (KLD) 3557 KLD

E Air i Flue gas emission details


-

SR. no.

Source of emission

With Capacity e.g. Boiler (8 TPH)


Name of the fuel


Type of emissions

i.e. Air Pollutants

APCM

1 Steam Boiler -1 10 TPH capacity

Common Stack

Dia.=2.0 m; Ht.=50 m

Coal or Lignite

Coal: 32.29 MTPD OR Lignite: 57.9 MTPD

PM, SO2 , NOx

Trema Cyclon, Electostatic Precipitator

2 Thermic Fluid Heater 1500 U capacity

Coal or Lignite

Coal:9.12 MTPD OR Lignite: 16.34 MTPD

PM, SO2 , NOx

Trema Cyclon, Bag Filter

3 Hot Air Generator 2 Nos. (45,00,000 Kcal/hr)

Coal or Lignite


PM, SO2 , NOx


4 Steam Boiler -2 30 TPH capacity

Dia.=2.0 m; Ht.=50 m

Coal or Lignite

Coal:96.86 MTPD OR Lignite: 173.68 MTPD

PM, SO2 , NOx


5 Hot Air Generator 2Nos. (45,00,000

Kcal/ hr )

Dia.=1.5 m; Ht.=42.5 m

Coal or Lignite


PM, SO2 , NOx


6 D. G. Sets 1000 KW - Stand by

Dia.=0.12m; Ht.=11.0 m

Diesel Diesel 200 Litre/Hr

PM, SO2 , NOx

Acoustic Enclosure


Dia.=0.12m; Ht.=11.0 m


PM, SO2 , NOx

Acoustic Enclosure


Dia.=0.12m; Ht.=11.0 m


PM, SO2 , NOx

Acoustic Enclosure


Dia.=0.12m; Ht.=11.0 m


PM, SO2 , NOx

Acoustic Enclosure


Dia.=0.12m; Ht.=11.0 m


PM, SO2 , NOx

Acoustic Enclosure


Dia.=0.12m; Ht.=11.0 m


PM, SO2 , NOx

Acoustic Enclosure


Dia.=0.12m; Ht.=11.0 m


PM, SO2 , NOx

Acoustic Enclosure


Dia.=0.12m; Ht.=11.0 m


PM, SO2 , NOx

Acoustic Enclosure

-


-

Sr. no.

Source of emission

Type of emissions i.e. Air Pollutants with emission

standards

Stack/Vent Height & Diameter (meter)

APCM

Page 81 of 126


Page 81 of 126

1. NKS (Condensation)

SO2< 40 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Caustic Scrubber Jet Type

2. NKS (Sulphonation)

SO2< 40 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Caustic 2 Stage Packed Column

3. Chlorination (Reaction)

HCl < 20mg/Nm3, Cl2 < 9 mg/Nm3

Ht:-15 mt, Dia:- 4 inch

2 Stage 1 stage Water and 2 Stage

caustic

4. Chlorination Tonner emergency scrubber

Cl2 < 9 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Cl2, recycling with jet compressor

5. Aminolysis NH3< 175 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Note: See below description *

6. Crude Dyes (Coupling)

Odour and fugitive emission Ht:-15 mt, Dia:- 4 inch

Caustic Scrubber Packed Column

7. Crude Dyes (Diazo)

NOx < 25 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Urea & Caustic 2 stage one venturi and one packed

column

8. Rosa Bromide BR2< 2 mg/Nm3, HBr< 30 mg/Nm3


SBS Scrubber

9. NSA Plant SO2< 40 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Caustic 2 Stage Packed Column

10. EO Reaction Vessel

EO Ht:-15 mt, Dia:- 4 inch

Packed Tower

11. Chlorosulfonation SO2< 40 mg/Nm3, HCl < 20mg/Nm3,


Two Stage Alkali Scrubbing System

12. Chlorosulfonation H2S < mg/Nm3 Ht:-15 mt, Dia:- 4 inch


13. Spray Dryer PM < 150 mg/Nm3 Ht:-27 mt, Dia:- 4.3 mt

Cyclone & Water Scrubber

14. SFD PM < 150 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Water Scrubber

15. ETP (Equalization Tank)

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


Single Stage Alkali Scrubbing System

16. FBD PM < 150 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Bag filter

17. Paddle Dryer PM < 150 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Bag filter

18. Tray Dryer PM < 150 mg/Nm3 Ht:-15 mt, Dia:- 4 inch

Bag filter

19. Reaction Vessels Odour and fugitive emission Ht:-15 mt, Dia:- 4 inch

Single stage Alkali Scrubbing System

20. Ethylation HCl < 20mg/Nm3, Cl2 < 9 mg/Nm3



21. Ethylation SO2< 40 mg/Nm3 Ht:-15 mt, Dia:- 4 inch


22. Bromination Br2 < 2 mg/Nm3, HBr< 30 mg/Nm3



23. Nitration Nox: < 25 mg/Nm3 Ht:-15 mt, Dia:- 4 inch


24. Detoxification Cl2 < 9 mg/Nm3, NOx: < 25 Ht:-15 mt, Packed Tower with

Page 82 of 126


Page 82 of 126

mg/Nm3 Dia:- 4 inch Alkali Scrubber

-


Fugitive emission will be expected from during raw material handling, transportation activities, coal handling, etc. Following mitigation measures will be implemented, - Water shall be sprinkled during the construction

- Water shall be sprinkled on fly ash

- Mechanical seals for pumps etc. should be used and maintained.

- Closed unloading, conveying and packing system

- All the reactors shall be closed.

- Safety devices shall be provided to workers

- Raw material storage in closed storage area

- Regular monitoring of solvents’ concentration in work zone.

- Greenbelt development around the plant.


i - Sr No

Name of The Waste


Category & Schedule as

per HW Rules

Quantity (MTPM)

Disposal Method

1. ETP Sludge Primary and secondary treatment

plant of ETP

35.3 4000 Collection, Storage Transportation, Disposal at GPCB approved TSDF site

2. Distillation Residue

Solvent Distillation

36.1 600

Collection, storage, Transportation and sent for incineration or co/pre-processing authorised common facility.

3. Spent Solvent

Process Reactor

26.4 3000 Collection, Storage and in-house distillation for recover.

4. Used/spent Oil

D. G. set and Utility

5.1 60 L/month

Collection, Storage, Transportation, Disposal by selling to registered re-refiner

5. Discarded Containers

RM Handling 33.1 15000 Nos./Month

Collection, Storage, Decontamination, Transportation, Disposal by selling to registered party

6. Gypsum From neutralization

of effluent

D2 2000 Collection, Storage, Transportation, Disposal at GPCB approved TSDF site or Cement Industries

7. MEE Salt ETP 37.3 840 Collection, storage, Transportation and sent to TSDF site for disposal.

8. Spent Carbon

ETP 36.2 210 Collection, storage, Transportation and sent for incineration or co/pre-processing to common TSDF facility.

9 Iron Sludge From D2 500 Collection, Storage,

Page 83 of 126


Page 83 of 126

Manufacturing of dyes

intermediates like AMA , PNBA RE,

Phthalimide Derivative,

etc.

Transportation, Disposal by selling to authorised party

10. Sodium Acetate

From Manufacturing

of Dyes Intermediates like SD-1A,

SD- 2A , SD-3A, SD-5, SD-

7,etc.

D2 300 Collection, Storage, Transportation, Disposal by selling to authorised party

11. Fly Ash Boiler -- 1350 Collection, Storage, Transportation and selling to brick manufacturer or Cement Industries

12. STP sludge STP -- 9 Used as manure in greenbelt area within plant premises.



TSDF and CHWIF membership will apply after obtaining ToR.


• Fly ash – 1350 MTPM (Collection, Storage,

Transportation and selling to brick manufacturer)

• STP sludge – 9 MTPM (Used as manure in

greenbelt area within plant premises.)



- DMF, Methanol, Toulene, etc. - Solvent recovery plant will be installed for

recovery of solvent - Around 95% recovery of solvent will be

achieved. - Recovered solvent will be reuse in the

manufacturing process.


- Fugitive emission from the proposed project activities shall be mainly the VOCs emissions, which results from uses of solvents.

- This emission will be taken place only at storage and handling of solvent.

- Storage is in closed area with a facility of condenser which will reduce the emission.

• Technical presentation was made by the project proponent. Committee noted that PP has shown

Indicative list of products instead of all products which was not accepted and upon asking, PP has

submitted all the names of products.

• While discussing about the huge quantum of water consumption, PP informed that they will reuse

• 3557 KLD of treated waste water in different sections. PP has requested to allow them for

discharge of treated waste water to CETP-Saykha. However, there is no existence of CETP Saykha

Page 84 of 126


Page 84 of 126

and no membership certificate obtained from the GIDC for CETP-Saykha. Hence, Committee asked

PP to provide Zero Liquid Discharge (ZLD) system. PP agreed and proposed ZLD.






1. Adequacy Certificate from schedule 1 auditor for Environmental Management System

(EMS) including complete Zero Liquid Discharge (ZLD) considering worst case scenario.

2. Detailed Leak Detection and Repairing Programme (LDAR) for all the volatile organic

solvent proposed for use in-house with detailed chemical properties including vapour

pressure. LDAR shall endeavour prevention of losses of solvents to the best minimum

extent.





2006.



10. SIA/GJ/IND2/21659/2018 M/s. Jackson Chemical Industries Plot No. 502/4, 5, 6, Nr. GIL, G.I.D.C.,

Ankleshwar, Dist: Bharuch-393002, Gujarat

Screening & Scoping







as tabulated below:

Sr. no.

Name of the Products CAS no. / CI no.

Quantity (MT/Month) End-use of the products Existing Proposed Total

1 Para Amino Azobenzene

4-Sulphonic Acid 104-23-4 50 100 150 Dyes

2 Direct Orange 39 1325-54-8 -- 200 200 Textile Ind.

3 Direct Orange 34 12222-37-6 -- 200 200 Textile Ind.

4 2,6 Dichloro 4 Nitro

Aniline 99-30-9 0.5 9.5 10 Dyes

Total 50.5 509.5 560


Page 85 of 126


Page 85 of 126

2006



project proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 3.14 Proposed: 1.20 Total: 4.34


Existing: 11,315.3 Sq. m. Proposed: 0.0 Sq. m. Total: 11,315.3 Sq. m.


Existing: 0.0 Sq. m. Proposed: 3,500 Sq. m. Total: 3,500 Sq. m.


D Water

i


The requirement of raw water shall be met through GIDC Water Supply.

Status of permission from the concern authority. Water supply later is referred as Annexure 11 in Form-1.


Existing KLD



Remarks

(A) Domestic 0.75 5.25 6

(B) Gardening 0 2.5 2.5

Industrial

Process 9.5 47.5 57

Washing 0 2 2

Boiler 1 5 6

Cooling 1 5 6

Others (Scrubber) 0 0.5 0.5

Industrial Total 11.5 60 71.5

Grand Total (A+B+C)

12.25 67.75 80








Remarks

Page 86 of 126


Page 86 of 126

(A) Domestic 0.5 4.5 5.0

Industrial

Process 7.5 16 23.5

Washing 0 2 2

Boiler 0 0.2 0.2

Cooling 0 0.2 0.2

Others (scrubber) 0 0.5 0.5


7.5 18.9 26.4

-


ETP: 26.4 KL/Day Spray Dryer: 18.9 KL/Day

v Mode of Disposal & Final meeting point Domestic: 5KL/Day Sewage is disposed in Septic Tank & Soak Pit.

Industrial: Existing: Industrial waste water 7.5 KL/day) is sent to CETP of M/s.ETL, Ankleshwar at present for treatment & disposal. Additional: Industrial waste water (18.9 KL/day) will be sent for spray drying within premises.


CETP of M/s. ETL

Membership of CF Obtained.

vii Reuse/Recycle details (KLD) We shall explore the possibility of recycle or reuse.



Existing

SR. no.

Source of emission

With Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 Boiler

(capacity:1 TPH)

15 Natur

al Gas

1,000 SCM/da

y

SPM SO2 NOX

-

2

Hot Air Generator

(Use in Spin Flash Dryer)

15

Natural

Gas

SPM SO2 NOX

-

Proposed

SR. no.

Source of emission

With Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

Page 87 of 126


Page 87 of 126

1

Boiler

(Spray

Dryer)(Coal

Fired)

30

meters Coal

10

MT/Day SPM

SO2

NOX

Multicyclone Separator With Bag Filter And

Scrubber

2

D.G.Set

(Capacity:

125 KVA)

9

meters Diesel

10

litters/day --


No Change after Proposed Expansion

Sr. no.

Source of emission

Type of emission


Air Pollution Control Measures

(APCM)

1 Reactor SO2 18 Two stage caustic

scrubber


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

any.

2. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done

to prevent leakages and thus minimizing the fugitive emissions of VOCs.

3. Entire process will be carried out in the closed reactors with proper maintenance of

pressure and temperature.

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

5. Breather valves will be provided on solvent tanks.

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

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

provided at all solvent pumps.

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

will be connected to vent chillers.

9. 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.

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

control in respect of odorous chemicals.


i Existing

Sr. no.




Quantity (MT/Annum)

Disposal Method

1 ETP Sludge ETP Schedule-I –

(35.3) 50 MT/Month

Collection, Storage, Transportation & Disposal at TSDF

2 Spent Oil Machinerie

s & Utilities Schedule-I –

(5.1) 1.67 Lit./Month

Collection, Storage, Transportation & Sale to Registered

Page 88 of 126


Page 88 of 126

Recyclerers

3

Discarded

Containers

Barrels/ Liners/

Bags

Raw

Materials &

Products

Schedule-I -(33.1)

20 Nos./Month

Collection, Storage, Transportation, Decontamination & sale to registered vendors

Total after Proposed expansion

Sr. no.

Type/ Name of Hazardous waste




Disposal Method

1 ETP Sludge ETP Schedule-I –

(35.3) 200

MT/Month


2 Spent Oil Machineries

& Utilities Schedule-I –

(5.1) 1.25

Lit./Month

Collection, Storage, Transportation & Sale to Registered Recyclerers

3

Discarded Containers Barrels/ Liners/ Bags

Raw Materials & Products

Schedule-I -(33.1)

3000 Nos./Month

Collection, Storage, Transportation, Decontamination & sale to registered vendors

4 Organic Waste

Process Schedule-I

–(26.1) 1 MT/Month

Collection, Storage, Transportation & Disposal at CHWIF

5 Salt from Spray Dryer

Spray Dryer Schedule-I

–(35.3) 45 MT/Month


6 Sodium Sulphate

Soln. Scrubber

Schedule-I –(26.1)

15 KL/Month Collection, Storage & treat in ETP.


ii Membership details of TSDF, CHWIF etc. Membership certificate of TSDF of M/s. BEIL is referred as Annexure-13 in Form-1.


No non-hazardous waste will be generated.



There is no solvent required after Proposed expansion.


There is no solvent required after Proposed expansion. No VOC emissions at all.

• Technical presentation was made by the project proponent.

• Committee observed that existing quantity of effluent will be discharged to CETP, ETL and ZLD for

additional waste water generation by means of in-house Spray Dryer.





Page 89 of 126


Page 89 of 126


1. Treatment and disposal of additional waste water in line with prevailing direction of CPCB

under section 18(1) b of the Water Act 1974.

2. Adequate ZLD system for additional waste water.





2006.



11. SIA/GJ/IND2/21556/2017 M/s. Aarpan Remedies LLP Plot No 3541, Gidc Phase – Iv, Chhatral Ta: Kalol, Dist: Gandhinagar

Appraisal


Project status: New

• PP has submitted online application vide no. SIA/GJ/IND2/21556/2017 dated 28/11/2017 for

obtaining Environmental Clearance.

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

24/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: Bhagwati Enviro Care Pvt. Ltd.,

Ahmedabad based on the TOR issued by SEIAA.

• This is a New unit proposes for Synthetic organic chemicals as tabulated below:

Sr. No.



End-use of products

1 Dimethyl Amino Ethyl Chloride HCL

4584-46-7 20 Pharma intermediates

2 Cetyl Chloride 4860-03-1 20 Pharma intermediates

3 Diphenyl Amine 155-39-4 5 Pharma intermediates

4 N’N’N’ Tritosyldiethyltriamine

52601-80-6 10 Speciality chemical


2006.


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

Report, details presented before the committee and details presented during the meeting.

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

Sr. no.

Particulars Details

Page 90 of 126


Page 90 of 126


(Rs. in Crores):

3.5 Crores

3. Capital cost for EMS (Environmental Management System):

0.305 Crores

4. Recurring cost towards the environmental protection measures:.

0.3475 Crores per Annum.

B Total Plot area ( sq. meter) 847.5 Sq. m.



3. Direct 15

4. Indirect 25

Total 40

D Water

i


GIDC


GIDC WILL GIVE PERMISSION TO SUPPLY WATER ONLY AFTER OBTAINING ENVIRONMENT CLEARANCE

ii


Category


(M) Domestic 0.5

(N) Gardening 0.1

(O) Industrial

Process 0.6

Washing 1.5

Boiler 3.0

Cooling 0.5

Others (Scrubber) 0.2


Total (A + B + C)

6.4

1) Total water requirement for the project: 6.4 KLD (including domestic +

Industrial + Gardening)

2) Quantity to be recycle: NIL


Page 91 of 126


Page 91 of 126


-


(G) Domestic 0.4

(H) Industrial

Process 0.6

Washing 0.4

Boiler 0.4

Cooling 0.05

Others (scrubbing) NIL Scrubbing waste water will be sold to actual user having rule 9 permission


1.45

-


Primary Effluent Treatment Plant With following Capacity

� Collection tank: 2.0 KL � Neutralizing Tank: 2.0

KL � Primary Settling tank:

1.5 KL � Holding Tank: 5 KL


Domestic: GIDC Septic Tank

Industrial: Treated at Primary Treatment plant at the site and will be sent for common spray drying at Chhatral environment management system pvt. Ltd. For SPRAY DRYING


Common Spray Drying @ CHHTARAL ENVIRONMENT MANAGEMENT SYSTEM PVT. LTD.

Membership of Common facility (CF)

Certificate attached as annexure – 2 (EIA report page no. 311)


NIL

E Air

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

Page 92 of 126


Page 92 of 126

KVA etc.

-

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 1000 Kg/Hr

11 Bio-coal

Lignite

0.33 MT/DayBiocoal

0.25 MT/Day Lignite

Particulate matters SOx Nox

Cyclone separator followed with bag filter

2

Thermic Fluid Heater 2.0 Lakh Kcal/Hr

11 LDO 0.06

MT/Day

Particulate matters SOx NOx


3

D.G set (as on when required to operate)

11 LDO 20

Ltrs/Hr

Particulate matters SOx NOx


-


-

Sr. no.

Source of emission

Type of emission



Measures (APCM)

1 Glass lined reactor

HCL SO2

11 Alkaline 2 way Scrubber system

-

iii Fugitive emission details with its mitigation measures. As below: SO2 & HCL scrubbing will be required. Alkaline scrubbing with 2 way path for most efficient scrubbing media will be used.


i

Sr. no.

Type of Hazardous


Category and Schedule as

Quantity (MT/Annum)

Disposal Method

Page 93 of 126


Page 93 of 126

waste per HW Rules.

1 ETP Sludge ETP 35.3 0.3 MT/Month

TSDF Site

2 Used oil Machinery 5.1 10 Ltr/Year TSDF/Recycler

3 Sodium Bi-sulfide (by – Product )*

Scrubbing 28.1 23 MT/Month

Actual users having Rule 9 permission.

4 Discard Container/ Bags

Operations 33.3 600 Nos/Month 380 Nos/Month

Recycler

*Sodium bi-sulphide generated during the alkaline scrubbing will be sold to actual user with rule 9 permission


Saurastraenviro projects pvt. Ltd, bhachau, Kutch Eco care infrastructure pvt ltd. Dasada, Surendranagar We will be member of either of the facility before obtaining CCA


NA

G Solvent management& VOC emissions etc.

i Details of Solvent recovery (As per respective ToR) Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents

Ethylene Dichloride: Total use at one time: 10 MT/Month Recovery: 98 % using in process distillation with closed system distillation facility attached to the reaction vessel. Bromobenzene: Total use: 5 MT/Month Recovery: 98 % Using in process distillation with closed system distillation facility attached to the reaction vessel.


Ethylene Dichloride: Minimum storage Closed system distillation facility on the reaction vessel Bromobenzene: Minimum Storage Closed system Distillation facility on the reaction vessel.

Page 94 of 126


Page 94 of 126

• The project proponent along with their experts/consultants attended the meeting of the SEAC

held on 04/04/2018. During the meeting, the project was appraised based on the information

furnished in the EIA Report, details presented before the committee. Technical presentation

made during the meeting by project proponent. EIA report reveals that baseline environmental

study was carried out during the month of March 2017 to May 2017 to determine the prevailing

status of ambient air, land use, noise level topography, meteorology, ecology & socioeconomic

outline. Baseline ambient air quality was measured at 8 sampling locations. Monitoring was

carried out for PM10, PM2.5, SO2, NOx, and VOC within 10 km radius from the project site. The

incremental Ground Level Concentration (GLC) has been computed using ISC-3 (Industrial

Source Complex. The maximum 24-hourly average ground level concentration for pollutant due

to proposed project calculated using mathematical model for PM10, SO2, NOx and resultant

values also meets with NAAQ standards. Committee observed that PP has proposed Bio Coal

or Lignite &LDO as fuel so cyclone separator followed by bag filter are required as an APCM.

SO2 will be generated as a process gas emission source and for that two stage alkali scrubber

is provided. Total water consumption of proposed project will be 5.2 KLD which will be sourced

from GIDC water supply.Total industrial wastewater generation will be 1.45 KLD. Generated

domestic wastewater of 0.4 KLD will be collected and treated in septic tank via soak pit. The

wastewater will be treated in primary ETP and sent to Common Spray Dryer of M/s:

ChhatralEnvironment Management System Pvt. Ltd.

• During presentation, upon asking PP informed that they will obtain membership certificate of

nearby TSDF sites. While discussing about the VOC emission, LDAR, EMP etc., Committee

observed that the ToR related to LDAR and EMP are not covered properly in the EIA report.

• After deliberation, it was unanimously decided to consider the project for further

consideration only after submission of the following:

1. Compliance of ToR no. 49 related to EMP.

2. Compliance of ToR no. 53 related to VOC & LDAR.

12. SIA/GJ/IND2/21486/2016 M/s. Roman petro chemical Survey no 922/P2, Village: MotaDahisara, Navlakhi Highway, Ta - Maliya, Dist - Morbi.

Appraisal


Project status: New

• PP has submitted online application vide no. SIA/GJ/IND2/21486/2016dated 31/01/2018 for



24/04/2017.

• Public Hearing was conducted by Gujarat Pollution Control Board on 13/12/2017 at project site

of M/s. Roman petro chemical, Survey no 922/P2, Village: MotaDahisara, Navlakhi Highway, Ta

- Maliya, Dist–Morbi.

• Project proponent has submitted EIA Report prepared by M/s: T.R. Associates, Ahmedabad

based on the TOR issued by SEIAA.

Page 95 of 126


Page 95 of 126

• This is a New unit proposes for Synthetic organic chemicals as tabulated below:

Sr. No.



End-use of products

1. Unsaturated Polyester Resin

Mixture 500 Used predominantly in making trays, shower stalls, boats, swimming pool, water tanks, etc.


2006.



project proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

2.6Crores

1. Capital cost for EMS (Environmental Management System): 0.19Crores

2. Recurring cost towards the environmental protection measures: 0.077Croresper

Annum.

B Total Plot area ( sq. meter) 12,950Sq. m.

Green belt area,/Tree Plantation area ( sq. meter) 4,270Sq. m.


1. Direct 25

2. Indirect 5

Total 30

D Water

i

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

Road Tanker (M/s Shree Bahuchar

Water Supplier)


We have obtained letter from the water supplier agency. It is attached as annexure 4 in EIA report.


Category


(A) Domestic 3.2

(B) Gardening 7.5

(C) Industrial

Process --

Washing 0.2

Boiler --

Cooling 6.0

Others --


Total (A + B + C) 16.9

Page 96 of 126


Page 96 of 126

1) Total water requirement for the project: 16.9KLD




-


(A) Domestic 0.15 To Soak pit Via Septic Tank

(B) Industrial ETP followed by Evaporator Process 1.4

Washing 0.2

Boiler --

Cooling 0.3

Others --


1.9

-

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

ETP (1.9 KLD)& Evaporator (190 Lit./hr)

v Mode of Disposal & Final meeting point Domestic: To soak pit through septic Tank

Industrial:ETP& Evaporation. Complete ZLD


NA

Membership of Common facility (CF) NA

vii Reuse/Recycle details (KLD) -NIL

E Air


-

Sr. no.

Source of emission

With Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1

Thermic Fluid Heater (6 lac kcal/h)

30 Diesel 100 L/day

SPM ≤ 150 mg/Nm3 SO2 ≤ 100 ppm NO2≤ 50 ppm

Adequate Stack Height

2 D.G. set (150 kVA)

6 HSD 32 L/hr

-

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

-

Sr. no.

Source of emission

Type of emission



1 -- -- -- --

-


Page 97 of 126


Page 97 of 126

As below:

Fugitive emissions are expected to be generated during construction & operation stages of the proposed project. During operation stage, leakage through valves, pumps, emission from open drum containing chemicals, open feeding; storage tanks, etc. are the major sources of fugitive emissions of organic chemicals and VOCs. Following measures are adopted to prevent and control fugitive emissions:

→ Entire manufacturing activity will be carried out in closed reactors / vessels and regular checking and maintenance of the same will be carried out to avoid any leakages.

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

→ The control of all parameters on a continuous basis shall be done by adequate control valves, pressure release valves and safety valves etc.

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

→ A regular preventive maintenance will be planned and performed to replace or rectify all damage gaskets, joints etc.

→ All raw materials will be stored in tanks/drums in isolated/designated storage area and will be kept tightly closed.

→ The spillages / leakages of specific chemical shall be collected and used or it shall be drained to effluent treatment plant.

→ Precautionary measures would be taken while handling various hazardous chemicals.

→ There would be provisions also of adequate ventilation system in process plant and hazardous chemical storage area.

→ Gas detectors will be provided in work area.

→ Workers will be provided with appropriate personal protective equipment’s. → The unit will also develop green belt area within the factory premises to control the

fugitive emissions from spreading into surrounding environment.

→ Unit will carry out work area monitoring twice in a year as per GFR.


I

Sr. no.





Disposal Method

1 Used oil/ spent oil

Machineries 5.1 0.55

Collection, storage and reuse within premises as

a lubricant/sell to registered recycler

2 Discarded

plastic bags/Drums

Raw material storage

area

33.1

1.7

Collection, storage and reuse within premises

/return back to supplier / sell to approved scrap

vendor.

3

ETP sludge&

Evaporation Residue

ETP 35.3 11.5 Collection, storage and disposal at authorized

TSDF site.


Unit will obtain membership of TSDF site after Commencement of proposed project.

Page 98 of 126


Page 98 of 126

G Solvent management& VOC emissions etc.

i Details of Solvent recovery (As per respective ToR) Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents

Not Applicable


The solvent used styrene which is being consumed in the process as it is used for resin dilution. Online VOC (Gas) detector will be installed in process area.

The project proponent along with their experts/consultants attended the meeting of the SEAC held on

04/04/2018. During the meeting, the project was appraised based on the information furnished in the

EIA Report, proceedings of the public hearing and details presented before the committee. Technical

presentation made during the meeting by project proponent. EIA report reveals that baseline

environmental study was carried out during the month of October 2016 to December 2016 to determine

the prevailing status of ambient air, land use, noise level topography, meteorology, ecology &

socioeconomic outline. Baseline ambient air quality was measured at five locations. Monitoring was

carried out for PM10, PM2.5, SO2, NOx, CO, and VOC within 10 km radius from the project site. The

maximum concentrations of PM10, PM2.5, SO2 and NOx at each ambient air monitoring locations were

compared with NAAQS for industrial, residential, rural and other areas. 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. Total fuel requirement of Diesel 100 Lit/day and HSD of 32 Lit/Hr. Total water

consumption of proposed project will be 16.9 KLD which will be sourced from Road Tanker (M/s Shree

Bahuchar Water Supplier). Total industrial wastewater generation will be 1.9 KLD.The wastewater will

be treated in proposed modified ETP and evaporated. Hence unit will follow zero liquid discharge

(ZLD). Unit will take membership of active TSDF site before starting the production. Compliance of the

ToR was found satisfactory.

After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant of

Environmental Clearance.

13. SIA/GJ/IND2/21413/2016 M/s.HI-Tech Coatings Plot No. 1801/10, GIDC, Vitthal,UdyognagarDist: Anand

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/21413/2016dated 26/01/2018 for



21/01/2017

• Project proponent has submitted EIA Report prepared by M/s: Satva Environ Consultancy,

Ahmedabad based on the TOR issued by SEIAA.

• This is an existing unit proposes for expansion of Synthetic organic chemicals as tabulated below:

Sr. Name of the Products CAS no. / Quantity End-use of

Page 99 of 126


Page 99 of 126

no. CI no. MT/Month the products Existing Proposed Total

1 Alkyd Resin Emulsion (Water Emulsion)

--- 12.0 12.0 24.0 Alkyds resins are used in paints and in moulds for casting.

2 Alkyd Resin (Castor Oil Based)

68333-62-0

15.0 15.0 30.0

3 Alkyd Resin (Linseed Oil Based)

68333-62-0

15.0 15.0 30.0

4 Alkyd Resin (Soyabeen Oil Based)

68333-62-0

06.0 06.0 12.0


2006.


• During the meeting dated 04/04/2018, technical presentation made during the meeting by project

proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 1.25 Cr. Proposed: 0.7 Cr. Total: 1.95 Cr.

1. Capital cost for EMS (Environmental Management System): 5.0 Lacs\

2. Recurring cost towards the environmental protection measures: 4.5 Lacs per Annum.


Existing: 739.37 Sq. m. Proposed:NIL. Total:739.37 Sq. m.


Existing:194.37 Sq. m. Proposed:NIL Total: 194.37Sq. m.


1. Direct Existing:10 Proposed: 5 Total:15

2. Indirect Existing: 15 Proposed: 5 Total: 20

D Water

i

Source of Water Supply GIDC Water Supply



Existing KLD



Remarks

(A) Domestic 2.0 NIL 2.0 Source GIDC Water Supply (B) Gardening 2.0 NIL 2.0

Industrial

Process 0.150 0.150 0.300

Page 100 of 126


Page 100 of 126

Cooling 1.00 1.00 2


Grand Total (A+B+C)

5.150 1.150 6.300


2) Quantity to be recycle:0.050 KLD






Remarks

(A) Domestic 1.50 NIL 1.50 Dispose though

Industrial

Process 0.025 0.025 0.050 Recycle back to process Cooling NIL NIL NIL


0.025 0.025 0.050

-

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

Not Applicable


Domestic: Soak Pit

Industrial: Zero discharge

E Air


-

Sr. no.

Source of emission With Capacity e.g. Boiler (8 TPH)


Name of the fuel


Type of emissions i.e. Air Pollutants

APCM Emission Standards

1 Thermic Fluid Heater

11.0 Natural Gas

100 m3/Day

PM

SOx

NOx

Not Applicable

PM:<150 mg/Nm3

SOx:< 100 ppm NOx:< 50 ppm

-Proposed Flue Gas Emission

2 Thermic Fluid Heater

11.0 Natural Gas

100 m3/Day

PM

SOx

NOx

Not Applicable

PM:<150 mg/Nm3

SOx:< 100 ppm NOx:< 50 ppm

3 D.G. Set 30 KVA

1.5 Diesel 40 Liter

-

Page 101 of 126


Page 101 of 126


No process gas emission from the proposed process.


Submitted in the EIA report


i

Sr. no.

Type/ Name of Hazardous waste



Quantity (MT/Annum)

Disposal Method

1. Used Oil Process 5.1

0.200

Collection, storage, Disposal by selling to registered recyclers or use as self-lubrication

2. Discarded Containers

Ware house

33.1 50 Collection, Storage, disposal by selling to registered decontamination facility or reuse for product packing

3. Waste/ Residue/ ETP Sludge

Process and ETP plant

23.1 0.600 Collection, Storage, Reuse again or disposal to TSDF/Co processing.


ii Membership details of TSDF, CHWIF etc. Not applicable


Not applicable


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

Not applicable

ii VOC emission sources and its mitigation measures Not applicable


held on 04/04/2018. During the meeting, the project was appraised based on the information

furnished in the EIA Report, major issues in public hearing and details presented before the

committee. Technical presentation made during the meeting by project proponent. EIA report

reveals that baseline environmental study was carried out during the month of March - 2017 to

May - 2017 to determine the prevailing status of ambient air, land use, noise level topography,

meteorology, ecology & socioeconomic outline. Baseline ambient air quality was measured at

five locations. Monitoring was carried out for PM10, PM2.5, SO2, NOx, CO and VOC within 5

km radius from the project site. The maximum concentrations of PM10, PM2.5, SO2 and NOx at

each ambient air monitoring locations were compared with NAAQS for industrial, residential,

rural and other areas.Committee observed that PP has proposed Natural gas as fuel so no

requirement of APCM.Total water consumption after expansion of proposed project will be 6.3

KLD which will be sourced from GIDC water supply. Total industrial wastewater generation will

Page 102 of 126


Page 102 of 126

be 0.05 KLD. Generated domestic wastewater of 1.5 KLD will be collected and treated in septic

tank. The generated wastewater will be recycled in propos. 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.

• Earlier PP has obtained EC for the existing unit.. They have valid CC&A for existing unit. Copy of

EC, CC&A, its compliance report is submitted. PP ensured that there are no court cases pending

and no public complaints against the project.

• While discussing about compliance of existing EC, PP informed that they have requested RO-

MoEF&CC, Bhopal as well as GPCB for Certified Compliance Report (CCR and same is awaited.

• After detailed discussion, it was decided to consider the project further only after

submission of the following:

1. Certified Compliance Report (CCR) from the Member Secretary, GPCB as per the MoEFCC’s

Circular no. J-11011/618/2010- IA (II) (I) dated 30/05/2012 and Circular no. J-11013/6/2010-IA-II

(Part) vide dated 07/09/2017.

14. SIA/GJ/IND2/21454/2017 M/s. Dhanlaxmi Pigments Pvt. Ltd. Plot no: 3020-21,GIDC industrial estate,3rd Phase, Near Garuda Cotex, Panoli-394116, Dist:-Bharuch, Gujarat.

Appraisal






21/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: Jyoti Om Chemical Research

Centre Private Limited, Ankleshwar based on the TOR issued by SEIAA.


as tabulated below:

Sr. no.


CAS no. / CI no.

Quantity (MT/Month) End-use of the products


1. Copper Phthalocyanine Blue

147- 14- 8 75 325 400 Used in

manufacturing of

Pigment alpha blue

& pigment beta blue

2. Pigment Alpha Blue

147- 14- 8 0 65 65 In textile industry &

paint Industry 3. Pigment Beta

Blue 147- 14- 8 0 60 60

4. Mono Sulpho CPC (real )

147- 14- 8 0 60 60 Used in pigment beta

blue production

5. Ammonium Sulphate*

7783-20-2 77 136 213 Pharmaceuticals &

Agro chemicals

Page 103 of 126


Page 103 of 126

Total 152 646 798


2006.



project proponent.


Report, details presented before the committee and details presented during the meeting.


Sr. no.

Particulars Details

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

Existing:4.96 Proposed:2.80 Total: 7.76

(1) Capital cost for EMS (Environmental Management System): 1.11Crores (2) Recurring cost towards the environmental protection measures: 7.97 Crores per

Annum.




Existing: 679 Sq. m. Proposed: 0.0 Sq. m. Total:679 Sq. m.


1. Direct Existing:10 Proposed: 0 Total:10

2. Indirect Existing:12 Proposed:23 Total:35

D Water

i


GIDC Local authority


Letter from GIDC for water supply is attached Annexure-VI


Existing KLD



Remarks

(A) Domestic 6 4 10

(B) Gardening 0 10 10

Industrial

Process 22.5 243.5 266 54 fresh +212 recycle

Washing 15 -15 0

Boiler 5 38 43

Cooling 1.5 23.5 25

Others - - -

Industrial Total 44 290 334

Page 104 of 126


Page 104 of 126

Grand Total (A+B+C) 50 304 (Fresh water= 92 KL/Day + Internal recycle= 212 KL/Day)

354 (Fresh water=142 KL/Day + Internal Recycle=212KL/Day)

1) Total water requirement for the project: 354 KLD 2) Quantity to be recycle: 212 KLD 3) Total fresh water requirement: 142 KLD

Iii Waste water generation (KLD)




Remarks

(A) Domestic 6 4 10

Industrial

Process 20 3 23

Washing 15 -15 0

Boiler 3 9 12

Cooling NIL 9 9

Others


44 10 54*

- 44 KLD will be discharged to CETP and 10 KLD will be treated into spray dryer.

Hence, unit will maintain existing discharge quantity 44KLD after proposed expansion

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

ETP :44 KLD (PETL=36 KL/day + ETL=8 KL/day sent to by Tanker)

v Mode of Disposal & Final meeting point Domestic: ETP

Industrial: * 44 KLD will be discharged to CETP and 10 KLD will be treated into In house spray dryer. Hence, unit will maintain existing discharge quantity 44KLD after proposed expansion.


Copy of common spray dryer membership attached is Annexure-XVII

Membership of Common facility (CF) --

vii Reuse/Recycle details (KLD) 212 KLD



-

Sr. no.

Source of emission With Capacity e.g. Boiler (8 TPH)


Name of the fuel


Type of emissions i.e. Air Pollutants


EXISTING EQUIPMENTS(AS PER CCA-AWH-80717)

1. Boiler-1 (Capacity :-3 TPH)

13 Natural Gas

3000 M3/day

Particulate Matter SOx


150mg/NM3

Page 105 of 126


Page 105 of 126

2. Thermic Fluid Heater(Capacity:-4 Lac Kcal/Hr)

Nox 100 ppm 50 ppm

3. HAG (Capacity:-4 Lac Kcal/Hr)

(AS PER CTE-83481*)

4. Thermic fluid heater (Capacity:-4 Lac Kcal/Hr)

13 Natural gas

5000 M3/day

Particulate Matter SOx NOx


150mg/NM3 100 ppm 50 ppm 5. Thermic fluid

heater (Capacity:-2 Lac Kcal/Hr)

6. Hot air generator for SFD (Capacity:-4 Lac Kcal/Hr)

7. D.G.Set (Capacity 320 KVA)

9 Diesel 100 lit/hr

Particulate Matter SOx Nox

PROPOSED EQUIPMENTS

8. Boiler (6 TPH) 13 Coal fire

12 MT/day

Particulate Matter SOx Nox

Multi cyclone separator

150mg/NM3 100 ppm 50 ppm 9. Thermic Fluid

Heater(Capacity:-20 Lac Kcal/Hr)

--

-


-

Sr. no.

Source of emission

Type of emission



EXISTING EQUIPMETNS

1. Reaction Vessel NH3

16 2-stage water scrubber

175 mg/NM3

PROPOSED EQUIPMETNS

2. Reaction Vessel (Nos:-2)

NH3

16 2-stage water scrubber (For each reactor)

175 mg/NM3

3. Reaction Vessel (Nos:-2)

iii Fugitive emission details with its mitigation measures. [Existing & Proposed]

• Routine & periodic inspection to check leakage

• Preventive maintenance, follow SOP for maintenance

• Pumps & motors mechanical seal type LDAR program is followed.

Page 106 of 126


Page 106 of 126

• Feeding of liquid raw material is carried out by closed pipeline and mechanical seal pump

• Unloading through pipeline to tank in a close system

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

i

Sr. no.




Quantity (MT/Annum)

Disposal Method

1. ETP Sludge Process 35.3 11700 TSDF Site/ Cement industry Collection, Storage, Decontamination and Transportation

2 Discarded Containers Bags/Liners

Process 33.1 12.6 Collection, Storage, Decontamination and Transportation

3. Used Oil DG set & compressor

5.1 60 Collection, Storage, Reuse and sell to register re-processor

4. Spent sulphruric acid

Process 26.3 19,440 Collection, Storage, and reuse within premises rule 9 permission will be taken remaining acid will be neutralized and sent to ETP,

5. Ammonium carbonate solution

process -- 12,001.2 Collection, Storage and convert to Ammonium sulphate crystal.



Membership Certificate from BEIL - TSDF site and PSWML - TSDF site are attached as annexure – XVIII in EIA report.


--


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

Details of solvent recovery is submitted

ii VOC emission sources and its mitigation measures Details are provided in chapter-8 in table no: 8.2 from page no.:8.12

• The project proponent along with their experts/consultants attended the meeting of the SEAC held

on 04/04/2018. During the meeting, the project was appraised based on the information furnished in

the EIA Report, details presented before the committee. Technical presentation made during the

meeting by project proponent. EIA report reveals that baseline environmental study was carried out

during the month of December 2016 to February 2017 to determine the prevailing status of ambient

air, land use, noise level topography, meteorology, ecology & socioeconomic outline. Baseline

ambient air quality was measured at 8 sampling locations. Monitoring was carried out for PM10,

PM2.5, SO2, NOx, NH3, HCl, CO and VOC within 10 km radius from the project site. The maximum

concentrations of PM10, PM2.5, SO2 and NOx at each ambient air monitoring locations were

Page 107 of 126


Page 107 of 126

compared with NAAQS for industrial, residential, rural and other areas. Concentration of PM10

ranged from 62 µg/m3 to 91 µg/m3. Concentration of PM2.5 ranged from 25µg/m3 to 40 µg/m3.

Concentration of SO2 recorded ranged from minimum 24µg/m3 to maximum 48µg/m3.

Concentration of NO2 recorded ranged from minimum 20µg/m3 to maximum 46µg/m3.

Concentration of VOC recorded ranged from minimum 1.2µg/m3 to maximum 4.4µg/m3.The

incremental Ground Level Concentration (GLC) has been computed using ISC-ST3. The maximum

incremental increase in concentration for PM, SO2 and NOx is 3.56 µg/m3, 3.64 µg/m3 and 2.57

µg/m3 respectively. The maximum incremental increase in concentration for NH3 is 0.13 µg/m3.

The maximum 24-hourly average ground level concentration for pollutant due to proposed project

calculated using mathematical model (ISCST3) for PM10, SO2, NOx and resultant values also

meets with NAAQ standards. Committee observed that PP has proposed Natural gas as fuel so no

requirement of APCM. PM, SOx, NOx will be generated as a process gas emission source and for

that multi cyclone separator will be provided and for NH3 emission, two stage water scrubber will be

provided for each reaction vessel.

• Total water consumption of proposed project will be 304 KLD which will be sourced from GIDC

water supply. Total industrial wastewater generation will be 54 KLD. Out of 54 KLD, 44 KLD waste

water will be discharged to CETP and 10 KLA will be treated into in-house spray dryer. Generated

domestic wastewater of 10 KLD will be collected and treated in ETP. The wastewater will be treated

in proposed modified ETP and evaporated. During presentation, Committee observed that unit has

mentioned waste water generation from washing activity as minus 15 KLD (-15 KLD). Upon asking

PP could not reply satisfactorily. Water balance found not in the proportion of production.

• After detailed discussion, Committee decided to defer the proposal in one of the upcoming

SEAC meeting.

15. SIA/GJ/IND2/19102/2017

M/s. Singham Bio Crop Care Pvt Ltd.

Plot No. 85/B, Village Dungri, Taluka Valia, Dist. Bharuch, Gujarat-393115

Appraisal

Project / Activity No.: 5(a)

Project status: New



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

dated 30/04/2017.


of M/s: M/s. Singham Bio Crop Care Pvt Ltd., Plot No. 85/B, Village Dungri, Taluka Valia,

Dist. Bharuch, Gujarat-393115.

• Project proponent has submitted EIA Report prepared by M/s: Eco Chem Sales& Services,

Surat based on the TOR issued by SEIAA, Gujarat.

• This is a New unit engaged in production of Synthetic organic chemicals proposes as tabulated

below:

Sr. No.

Name of the Products Quantity MT/Month

End-use of products

Page 108 of 126


Page 108 of 126

1 Single Super Phosphate (SSP) / Granular Single Super Phosphate (GSSP)

10000 As a Fertilizer

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

2006.



project proponent.


Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 8 Cr

1. Capital cost for EMS (Environmental Management System):0.93 Cr

2. Recurring cost towards the environmental protection measures: 0.032 Crper Annum.

B Total Plot area ( sq. meter) 7600 Sq. m.



1. Direct 20

2. Indirect ~30

Total ~50

D Water

i

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

GIDC, Valia

Status of permission from the concern authority. Permission letter obtained.


Category


Remarks

(A) Domestic 3.0

(B) Gardening 4.8

(C) Industrial

Process 74.6 SSP & GSSP

Washing -

Boiler -

Cooling 27.4

Others 31.2 Ventury Scrubber


Total (A + B + C) 141 Initial requirement

1) Total water requirement for the project: 141 KLD (initial stage)

2) Quantity to be recycle: 38.4 KLD


Iii Waste water generation (KLD)

-


Page 109 of 126


Page 109 of 126

(A) Domestic 2.7 Treated in septic tank/soak pit system

(B) Industrial

Process

Washing

Boiler

Cooling 7.2 Reused in process

Others 31.2 From Ventury Scrubber, reused in process


38.4 Will be reused in process

-


As the unit is ZLD. Entire quantity of waste water generated from the scrubbing system will be reused into process. Hence treatment facility not proposed


Domestic:septic tank/soak pit system

Industrial: ZLD


Not Applicable

Membership of Common facility (CF) Not Applicable

vii Reuse/Recycle details (KLD) 38.4 KL/Day will be reused into process

E Air


SR. no.

Source of emission

With Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 GSSP Plant 30

meter White Coal

30 Kg / hr

PM, SO2 NOx

PM : <150 mg/Nm3

SO2: <100 ppm

NOx : < 50 ppm

2

1 × 250 KVA DG

Set (In case of

emergency)

8.5 meter

HSD 50 L/hr PM, SO2

NOx

-


-

Sr. no.

Source of emission

Type of emission



1 SSP Plant

stack F 45

Attached to four stage scrubber having water

as scrubbing media

-


-

F Hazardous waste

Page 110 of 126


Page 110 of 126

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

i

Sr. no.




Quantity (MT/Annum)

Disposal Method

1 Used Oil D.G. Set 5.1 200Litres/A

nnum

Reuse in lubrication of gear box and drive

chains

2 Discarded

Container

Used drums/cont

ainers 33.1

~ 500 No.

To authorized re-

processor / vendors


ii Membership details of TSDF, CHWIF etc. Not Applicable


Other municipal solid waste generated would include kitchen waste, cardboards, papers, plastics and garden waste. Cardboard, papers and plastic wastes will be handed over to scrap dealers and kitchen & garden waste would be sent to the nearest municipal waste collection site.


held on 04/04/2018.


Report, Public hearing proceedings and details presented before the committee. Technical

presentation made during the meeting by project proponent. EIA report reveals that baseline

environmental study was carried out during the month of March 2017 to May 2017 to determine

the prevailing status of ambient air, land use, noise level topography, meteorology, ecology &

socioeconomic outline. Baseline ambient air quality was measured at eight locations. Monitoring

was carried out for PM10, PM2.5, SO2, NOx, CO, HC and HF within 10 km radius from the

project site.

• The highest values of incremental increase in pollutants PM10, SO2, NOX are 1.33, 4.23 & 1.12

µg/m3 at Project site respectively. While at rest of monitoring stations, PM10, SO2,NOx

concentration values are found in the range of 0.01-0.25, 0.03-0.69, 0.01-0.20µg/m3

respectively. The highest resultant concentration values of PM10, SO2, NOX are 84.53, 26.33,

27.52 µg/m3 respectively at project site compared to rest of monitoring stations.All results have

been found within the NAAQ Standard Limit. The incremental Ground Level Concentration

(GLC) has been computed using AERMOD. The maximum 24-hourly average ground level

concentration for pollutant due to proposed project calculated using mathematical model for

PM10, SO2, NOx and resultant values also meets with NAAQ standards.

• Total fuel requirement of HSD of 50 Lit/Hr. Total water consumption of proposed project will be

141 KLD which will be sourced from GIDC, Valia.The proposed manufacturing unit will run on

“Zero Liquid Discharge” principle. As mentioned earlier, the total water requirement is 141 KLD

out of which 102.6 KLD will be fresh water and 38.4 KLD will be recycled water. Wastewater

Page 111 of 126


Page 111 of 126

generated from cooling tower and Ventury Scrubber will be reused for dilution of Sulphuric acid

during making of SSP slurry. Wastewater generated from domestic use will be disposed into

soak pit/septic tank.

• Issues related to Public hearing, CSR, reuse of waste water etc. have been discussed in detail.

Committee suggested reusing spent acid as raw material. PP informed that they wil explore the

possibility in future and required permissions under Rule 9 of HW Rules will be obtained from

the concerned authority.

• 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. Compliance of the ToR

was found satisfactory.

• After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for

grant of Environmental Clearance.

16. SIA/GJ/IND2/19142/2015

M/s. Meridian Chem-Bond Pvt. Ltd. Plot No: C - 378,379 & 380,Saykha GIDC, Dist: Bharuch

Reconsideration

Category of the unit : 5(f)

Project status: New


SIA/GJ/IND2/19142/2015 dated 14/04/2017 regarding grant of Environmental Clearance.

• Project proponent has submitted EIA Report prepared by M/s: Envisafe Environment

Consultants, Ahmedabad, based on the TOR issued by SEIAA vide dated 23/03/2016 and

amended vide dated 13/10/2016.


of M/s: Meridian Chem-Bond Pvt. Ltd.,Plot no: C-378, 379 and 380, GIDC Saykha Industrial Estate,

Ta.: Vagara, Dist.: Bharuch.

• This is a new project proposing to manufacture various Synthetic Organic Chemicals. Proposed

total production will be as shown below :

Sr.

no. Name of Products CAS no.

Capacity

(TPM) End Use of Products

1 Mono Chloro Acetic Acid 79-11-8 3,000 Intermediate for Pharmaceuticals

2 Try ChloroAcetyle Chloride 76-02-8 1,500 Intermediate for Pharmaceuticals

3 ChloroAcetyle Chloride 79-04-9 750 Intermediate for Pharmaceuticals

4 Sulphur Mono Chloride 10025-67-9 500

Intermediate for Sulphur Dyes, as polymerization catalyst for vegetable oils and for hardening soft woods

Page 112 of 126


Page 112 of 126

5 Sodium Mono Chloro acetate 3926-62-3 500 Intermediate for Pharmaceuticals,Dye stuff, Textile chemicals

6 IsopropyleChloro Acetate 105-48-6 500 Intermediate for Pharmaceuticals

7 Mono Methylechloro acetate 96-34-4 500 Intermediate for Pharmaceuticals &Dye stuff.

8 Chlorinated parafin wax 85535-85-9 2,000 PVC industry, Plasticisizer

9

Benzal chloride 98-87-3

1,068 Intermediate for

Pharmaceuticals Benzyl Chloride 100-44-7

Benzo Tri Chloride 98-07-7

10 Benzaldehyde 100-52-7 500 Intermediate for

Pharmaceuticals

11

Ortho Nitro Chloro Benzene (ONCB)

38-73-3 1,000

Intermediate for

Pharmaceuticals& Dye Stuff Para Nitro Chloro Benzene (PNCB)

100-00-5

12 Meta Nitro Chloro Benzene (MNCB)

121-73-3 500 Intermediate for Pharmaceuticals & Dye Stuff

13 Glycine 56-40-6 1,000 Use in medicines, additive in animal feed, antacids, plasticizers

Total 13,318

• The proposal falls under project / activity no. 5(f) in the Schedule of the EIA Notification, 2006.

As the unit is located in to the industrial estate of Saykha GIDC, it falls under category "B" of the

schedule.

• PP was called for appraisal in the SEAC meeting dated 26/04/2017 & 03/08/2017 and

Committee recommend to grant of Environmental Clearance for the proposed project subject to

strict compliance of the condition therein.

• SEIAA, Gujarat has referred back the proposal vide their letter

no.SEIAA/GUJ/EC/5(f)/841/2017dated31/08/2017 with the following reasons:

1. Toverifypotentialofhazardouswastegenerationandfeasibilityofitsdisposal especially

consideringthehugequantumofgenerationandtransportation.Also,toprovidein-

housecaptivehazardouswastereuse/recyclefacility.

2. ToverifytheAPCMprovidedforNOxgenerationduringprocess.

PP has submitted above mentioned additional details vide their letter on 13/09/2017 as below:

• Entire quantity of all the by-products generated from proposed project viz.Hydrochloric Acid (30%),

Sodium Hypochlorite (11%), Sodium Bisulphite (14%), Ammonium Chloride (26%), Spent Sulphuric

Acid (45- 70%), Mother Liquor of MCAA and High Boilers of Benzal Chloride will be sold to GPCB

authorized end-users.

• MoU will be made with actual end-user only after ensuring that end-user has valid CC&A of GPCB

for manufacturing of products where such by-products covered under H&OW (M&TM) Rules,2016

Page 113 of 126


Page 113 of 126

will be utilized.

• It will be ensured that end-user is having permission under Rule 9 or has made an application for

the same for acceptance of hazardous waste as per H&OW (M&TM) Rules, 2016.

• Recordofsaleofhazardouswastetoend-userswillbemaintainedasperGPCBguidelines.

• There will be no generation of NOx from proposed manufacturing process. Process gas generation

from the proposed manufacturing process will be in the form HCl, Cl2, NH3 & SO2 gases. Adequate

scrubbing system of water scrubbers followed by alkali scrubbers will be provided for control of

gaseous emission into atmosphere.

Committee observed that the quantity of wastes streams like Spent HCl, Spent H2SO4, Sodium

Hypochlorite etc. is very large and management of the waste streams is as per the previously

proposed. PP has not explored in-house reuse recycle of the waste streams. Looking to the huge

quantum of hazardous waste generation, Committee decided to consider the proposal for further

appraisal only after satisfactory submission of the points raised by SEIAA, Gujarat vide letter no.

SEIAA/GUJ/EC/5(f)/841/2017 dated 31/08/2017.

PP has submitted the above mentioned details vide letter dated 13/03/2018.

PP was called for presentation in the SEAC meeting dated 04/04/2018.

During the meeting, Committee noted that PP has submitted their reply as below:

� Hazardous waste generated from the manufacturing process and APCM i.e. Spent HCL (30%)

and Spent sulphuric acid (45 – 70 %) will be captivity reused within the plant premises. PP has

proposed to manufacture Calcim Chloride, Di-Calciuum Phosphate, Chlorosulphonic Acid,

Chemical Gypsum and Ferrous Sulphate. PP has also applied for obtaining CTE/NOC

amendment to GPCB for manufacturing of these Inorganic Chemicals.

� PP ensured that they will obtain permission from the concern authority under Rule 9 of HW

Rules if it is required for captive consumption of spent acids.

While asking about the feasibility for converting spent acids into inorganic products, PP informed that

these products have wide potential and requirements in the market for manufacturing of various

specialty chemicals. PP informed that there will be no generation of NOx from the proposed

manufacturing process. However, Committee asked to submit sources of NOx generation and its

possible mitigation measures. Committee also noted that PP has not attended the remaining hazardous

waste in their reply.

After detailed discussion, It was decided to further appraise the project only after submission of

the following:

1. Toverifypotentialofhazardouswastegenerationandfeasibilityofitsdisposal especially

consideringthehugequantumofgenerationandtransportation.Also,toprovidein-

housecaptivehazardouswastereuse/recyclefacility. (Consider all types of Hazardous waste

categories mentioned in EIA report).

2. To verify the APCM provided for possible all the sources of NOx generation during process.

3. Revised details with respect to addition of inorganic products and its impact on Environment.

17. SIA/GJ/IND2/19503/2017 M/s: Suheka Industries Plot No. 545, Phase-II, GIDC, Vatva, Ahmedabad

Reconsideration

Page 114 of 126


Page 114 of 126

Category of the unit : 5(f)



dated 11/09/2017 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.

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

tabulated below:

Sr. no.


CAS no. / CI no.

Quantity MT/Month

End-use of the products Existing Proposed Total

1 Simethicone 8050-81-5

15 -- 15 Used in Tablet& Syrup

2 Simethicone Emulsion

8050-81-5

3 Diclofenac Sodium

15307-79-6

-- 20 20 Used in Tablet& Capsule

4 Diclofenac Potassium

15307-81-0

5 DiclofenacDiethylamine

78213-16-8

6 Aceclofenac 89796-99-6 -- 10 10 Used in Tablet& Capsule

7 Pentoxyfylline 6493-05-6 -- 10 10

8 Bronopol 52-51-7 -- 10 10 Used in Syrup

• By Products

1. Sodium Bromide

7647-15-6 -- 15.20 15.20 --

• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification2006.

• Earlier, PP was called for presentation in the SEAC meeting dated 06/10/2017.

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

Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 0.25 Proposed: 1.25 Total: 1.50


Existing: 1281.25 Sq. m. Proposed: 0.0 Sq. m. Total: 1281.25 Sq. m.




D Water

Page 115 of 126


Page 115 of 126

i


GIDC Vatva


Water supply available

ii


Existing KLD



Remarks

(P) Domestic 0.50 0.50 1.00

(Q) Gardening 0.05 0.20 0.25

Industrial

Process 0.40 3.00 3.40

Washing -- 0.50 0.50

Boiler -- 4.50 4.50

Cooling -- 0.50 0.50

Others (Condensate) -- 3.50 3.50


Grand Total (A+B+C)

0.95 12.70 13.65


2) Quantity to be recycle: 3.50.KLD


iii





Remarks

(I) Domestic 0.40 0.40 0.80 Septic Tank / Soak Pit

Industrial

Process -- 2.60 2.60

Washing -- 0.50 0.50

Boiler -- 0.50 0.50

Cooling -- 0.10 0.10

Others -- -- --


0.40 3.70 3.70 3.70 KL/day to ETP

-

Page 116 of 126


Page 116 of 126

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

Sr.No. Particular Size (m) Volume

1 Collection cum Neutralization Tank 1.5 x 1.5 x 2.5 5600 Lit

2 Filter Press 24” x 24” x 24 Nos. --

3 Holding Tank 1.5 x 1.5 x 2.0 4500 Lit

4 Single Effect Forced Evaporator -- 200 lit/hr


Domestic: Septic Tank / Soak Pit

Industrial: Zero Liquid Discharge.


Spray Drying: GESCSL, Vatva

Membership of CF GESCSL, Vatva


3.50


i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Boiler: 1 No DG set : 1 No

-

SR. no.

Source of

emission With

Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 Boiler (0.8 TPH)

15 Natur

al Gas

70 SCM/hr PM

SO2 NOx

--

2 D. G. Set 40 KVA (Stand By)

8 Diesel 6 Lit/hr --

-


No process emission.

iii Fugitive emission details with its mitigation measures. [Existing & Proposed]:

Details will be covered in EIA report.


i

Page 117 of 126


Page 117 of 126

Sr. no.

Type/Name of

Hazardous waste


Category and Schedule as

per HW Rules.

Quantity (MT/Annum)

Disposal Method

1.

Discarded Drum/ Containers

Raw Materials

Packaging

33.3

1.60

Send back to raw materials supplier or Sold to registered recycler

Bags with liner

1.5

Send back to raw materials supplier or Sold to registered recycler

2. ETP Effluent

Treatment 35.30

3.60

Collection. Storage, Transportation, Disposal at TSDF site.

3. Process Waste

Manufacturing Process

28.1 62.00


4. Used Oil Machineries 5.1 0.20

Collection, Storage and Sold to registered recycler

5. Spent Carbon

Manufacturing Process

28.3 7.40

Collection, Storage, Transportation, Disposal at TSDF site.

6. Evaporation Residue

E 37.3 22.00



Spray Drying - Green Vatva TSDF, Green Vatva


None



Dimethyl Aniline Toluene Dimethyl Formamide Methanol No solvent recovery plant is required as recovery will take place during reaction by reflux system.

Page 118 of 126


Page 118 of 126

ii VOC emission sources and its mitigation measures None

• Technical presentation was made by the project proponent during the SEAC meeting dated

06/10/2017. While discussing about the compliance status, Committee observed that PP is not

aware about compliance status of existing project. Looking to the casual approach of project

proponent and consultant, Committee decided to defer the proposal and asked to submit

compliance status of existing project.

• PP has submitted reply for the above mentioned queries.


• During the meeting, Committee noted that PP has submitted compliance status of existing

project. Entire quantity of waste water generation will be sent to Common spray dryer of M/s:

GESCSL, Vatva. PP has submitted membership certificate of GESCSL.

• 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. Adequacy of proposed area with respect to plant machineries , EMS, green belt , safety

aspect, raw material & product storage considering worst case scenario. Submit proper lay

out plan clearly demarcating all activities with scale.

2. Management of Sodium Bromide to be generated from manufacturing of Bronopol as per

the HW Rules 2018.

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

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

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





2006. The project proponent shall have to apply for Environmental clearance through online portal


18. SIA/GJ/IND2/22218/2018 M/s: Shreeji Industries Plot No. D2/CH/24, GIDC ESTATE, Dahej - II, Vagra, Bharuch

Reconsideration

Category of the Project: 5(f) Project Status: Expansion

• This office has received an application vide their online proposal no. SIA/IND2/22218/2018 dated 09/03/2018regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.

• This is an Expansion of unit process manufacturing of synthetic organic chemicals as tabulated below:

Page 119 of 126


Page 119 of 126

Existing Product (Inorganic)

Sr. No. Name of Products CAS No. Capacity,

TPM

1 Ammonium Molybdate 12054-85-2

600

2 Ferrous Sulphate 7720-78-7

3 Sodium Cyanate 917-61-3

4 Copper Sulphate 7758-98-7

5 Cuprous Chloride 7758-89-6

6 Cupric Chloride 7747-39-4

*Note- Unit has obtained Consent to Establish (CTE) for manufacturing of various inorganic products but yet not commissioned the project.

Product profile after proposed expansion (Organic)

Prod. Code.

Name of Products CAS No. Capacity,

TPM Use of Product Remarks

A1 Meta Ureido Aniline 59690-88-9 100 Dyes

intermediate 70% Strengh,

Actual Qty-142 TPM

B1 Naphthol ASOL 135-62-6

80

Dyeing and printing

-

B2 Naphthol AS 92-77-3 Dyeing and

printing -

B3 Naphthol ASBO 132-68-3 Dyeing and

printing -

B4 Naphthol ASBS 135-65-9 Dyeing and

printing -

B5 Naphthol ASCL 137-52-0 Dyeing and

printing -

B6 Naphthol ASD 135-61-5 Dyeing and

printing -

B7 Naphthol ASE 92-78-4 Dyeing and

printing -

C1 BON Acid 92-70-6 125 Naphthol

intermediate -

D1 Metanilic Acid 121-47-1

80

Dyes intermediate

-

D2 Aniline 2,5 Di sulphonic Acid

98-44-2 Dyes

intermediate 50% strength,

Actual Qty-160 TPM

E1 Pure Sulphanilic Acid 121-57-3

90

Dyes intermediate

-

E2 Aniline 2,4 Di sulphonic Acid

137-51-9 Dyes

Intermediate 80% strength,

Actual Qty-113 TPM

E3 Para Amino Azo Benzene 4-Sulphonic Acid (PAABSA)

104-23-4 Dyes

intermediates -

F1 Benzidine 2-2 disulphonic acid (BDSA)

117-61-3 60 Dyes

intermediates 85% strength,

Actual Qty-71 TPM

Page 120 of 126


Page 120 of 126

F2 Fast Scarlet G Base 99-55-8 Dyeing and

printing -

F3 4 Nitro 2 Amino Phenol (NAP)

99-57-0 Dyes

Intermediate -

Total 535.00 -

• The project falls under category B of project activity 5 (f) as per the schedule of the EIA

notification 2006.

• PP was called for presentation in SEAC meeting dated 04/04/2017.

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

Sr. No.

Particulars Details

A Total cost of the proposed project (Rs. in Crores)

17.50 Crores

B Total Plot area (sq. meter)

14246.38

Green belt area / Tree Plantation area (sq. meter)

4700

C Employment Generation 66

D Water

i

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

GIDC

Status of permission from the concern authority.: Permission obtained from GIDC

ii Water consumption (KL/day)

-

Category Existing KL/day


KL/day


KL/day Remarks

(R) Domestic 1.5 3.0 4.5 Fresh

(S) Gardening - 14.0 14.0 Fresh

(T) Industrial

Process 3.5 114.0 117.5 Fresh

APCE 1.0 6.0 7.0 Fresh

Boiler 1.0 45.0 46.0 Fresh

Cooling - 40.0 40.0 Fresh

Washing 11.5 1.5 13.0 Fresh

Total (A+B+C) 18.5 223.5 242.0

1) Total water requirement for the project : 242 KLD 2) Quantity to be recycle :Nil 3) Total Fresh water requirement : 242 KLD

iii Waste water generation (KL/day)

-

Category Existing KL/Day


KL/day


KL/day Remarks

(J) Domestic 1.1 2.5 3.6

(K) Gardening - - -

(L) Industrial

Process 1.8 200.0 201.8

APCE 1.0 9.0 10.0

Page 121 of 126


Page 121 of 126

Boiler 0.2 5.0 5.2

Cooling - 10.0 10.0

Washing 11.5 1.5 13.0


14.5 225.5 240.0

Generation: 240.0

Discharge: 238.5

Reuse : Nil

-

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

ETP- 250 KLD MEE- 170 KLD ATFD-170 Kg/hr


Domestic: 3.6 To soak pit through septic tank

Industrial: 238.5 KLD – Discharge into underground GIDC drainage system

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

Not Applicable

Membership of CF Not Applicable

vii Reuse/Recycle details (KL/day) None

E Air


Details of Flue Gas Stacks for Existing Project (Inorganic)

SR

. n

o.

So

urc

e o

f

em

issio

n

Wit

h

Cap

acit

y

Sta

ck

Heig

ht

(mete

r)

Nam

e o

f th

e

fuel

Qu

an

tity

of

Fu

el M

T/h

r&

MT

/Day

Typ

e o

f

em

issio

ns

i.e.

Air

Po

llu

tan

ts

AP

CM

Em

issio

n

Sta

nd

ard

s

1

Steam

boiler

(1.0 TPH)

11.0

Agrowaste/ white coal/ liquid Fuel

1.6 TPD PM SO2 NOx

Adequate Stack

Height as per CPCB guidelines

PM ≤ 150 mg/Nm3

SO2 ≤ 100 ppm

NOx ≤ 50 ppm

2

Hot Air

Generator

(800 kg)

11.0

Adequate Stack


3

Spray Dryer

(for

evaporation

of water)

15.0 - -

Cyclone Separator &

wet Scrubber

Details of Flue Gas Stacks for Proposed Expansion (Organic)

Page 122 of 126


Page 122 of 126

SR

. n

o.

So

urc

e o

f

em

issio

n

Wit

h

Cap

acit

y

Sta

ck

Heig

ht

(mete

r)

Nam

e o

f th

e

fuel

Qu

an

tity

of

Fu

el M

T/h

r&

MT

/Day

Typ

e o

f

em

issio

ns

i.e.

Air

Po

llu

tan

ts

AP

CM

Em

issio

n

Sta

nd

ard

s

1

Steam

boiler

(5.0 TPH)

15.0

Imported Coal &/or

Lignite &/or Biofuel

15 TPD PM SO2 NOx

Individual cyclone

separator followed by Common Bag Filter

PM ≤ 150 mg/Nm3

SO2 ≤ 100 ppm

NOx ≤ 50 ppm

2

Thermic

Fluid Heater

(3,00,000

kcal/hr)

3 DG set

(125 KVA) 10.0 Diesel 32 Ltres/hr

Adequate Stack


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

Details of process gas stacks (Existing-Inorganic Products)

Sr. no.

Source of emission Type of

emission


APCM Emission Standards (mg/Nm3)

1 Reactors Vessels (For Chlorination)

HCl 11.0 Hood Cover &

Two stage scrubber

HCl ≤ 20 NH3≤300 SO4 ≤ 40

2 Reactors Vessels (For Ammonia)

NH3 11.0 Two Stage Scrubber

3 Reactors Vessels

(For Copper Sulphate) SO4 11.0

Hood Cover & Two stage scrubber

Details of process gas stacks (Proposed-Organic Products)

Sr. no.

Source of emission Type of

emission


APCM Emission Standards (mg/Nm3)

1 Reactor (For Naphthol

series) HCl 11.0

Two stage Alkali

Scrubber HCl ≤ 20

2 Reactor of

PureSulphanilic Acid

Fumes &Vapors of Aniline Gas

11.0 Acidic

Scrubber -

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

There will be a chance of fugitive emission and odor nuisance during manufacturing process as well as due to storage & handling of raw materials and products. The unit takes following precaution for the control of fugitive emission and will implement the same for the proposed expansion.

Page 123 of 126


Page 123 of 126

Probable Sources Control Measures

Manufacturing activities during charging into reactors

• Liquid raw materials are charged by pumping & closed loops.

• Dosing is done by metering system to avoid fugitive

emissions.

• Dedicated measuring tanks are provided to each reactor.

• Usage of closed handling system for odorous chemicals

/solvents as far as possible.

Solvent recovery during filling and withdrawal from tanks and vessels

• Breather valves, PSVs, Rupture discs will be installed for process/storage tank vents.

• Vapor recovery systems shall be provided at required locations.

• Proper Control of the operating parameters, mainly temperature, vacuums, cooling media circulation, during plant operation and solvent recovery.

Chemical vapor from wet cake in filtration and drying area

• Covered transfer systems will be adopted, workers shall be provided PPE.

• Fume extraction systems will be provided, wherever required

Emission from bulk storage tanks during storage, loading, unloading

• Breather valves, PSVs, Rupture disc, Vapor recovery system

are installed for process/storage tank vents.

• Unit adopts bulk handling of odorous chemicals and avoid

usage of drums/carboys for such materials

Hazardous chemical storage area

• Dedicated storage area is provided

• Adequate ventilation systems are provided

• All the containers are kept tightly closed

• Trolley/Forklift is used for transfer of drums and containers

• Transfers of odorous waste is preferably during day time.

Transfers during odd hours is avoided.

Solvent recovery During filling and withdrawal from tanks and vessels

• Breather valves, PSVs, rupture discs are installed for

process/storage tank vents.

• Vapor recovery systems are provided at required locations.

• Operating parameters are controlled properly, mainly

temperature, vacuums, cooling media circulation, during plant

operation.

Chemical vapor from wet cake in filtration and drying area

• Covered transfer systems are adopted, workers are provided

with PPE.

• Fume extraction systems are provided, wherever required.

Pump and compressor Emissions

• Mechanical seals are provided in pumps and agitators

• Standby arrangement for critical equipment and parts is

ensured.

• Drip trays will be placed for each pump to collect leakages

and spillages.

Pressure relief valve emission from pipelines

• For highly pressurized lines, vent pipes of PRVs are

connected in case of toxic gases.

Page 124 of 126


Page 124 of 126

Valves, Flanges, plugs and instrument connections

• Welded pipes are used wherever feasible.

• Suitable gasket materials are used.

• Suitable glad packing is used in valves.

• Periodic inspection and maintenance of pipes and pipe fittings

is carried out.

Release from sampling lines • Closed loop system is used.

Hazardous chemical storage area

• Provision of dedicated storage area

• Adequate ventilation system to be provided

• All the containers will be kept tightly closed

• Trolley/Forklift will be used for transfer of drums and containers

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

i Type of waste

Source Cat. Quantity per Annum

Method of Disposal E* P* T*

ETP Sludge

ETP Sch-I 35.3

65 MT

535 MT

600 MT Collection, Storage,

Transportation, Disposal by land filling

at TSDF Process Waste

Process

Sch-I 26.1

720 MT

Nil 720 MT

Iron Sludge Sch-I 26.1

- 1850 MT

1850 MT

Collection, Storage, Transportation,

Disposal by land filling at TSDF or Send to Cement Industries

Calcium Sulphate

Sch-I 26.1

- 803 MT

803 MT

Collection, storage, Transportation,

disposal by land filling at TSDF

OR Sell GPCB authorized

end user

Sodium Sulphate

Sch-I 26.1

- 475 MT

475 MT

Spent Carbon

Sch-I 26.1

- 123 MT

123 MT

Collection, Storage Transportation and

Disposal by incineration at CHWIF

OR Disposal by co-

processing at cement Industries

Discarded Bags/

Containers

Raw Material

Storage & Handling

Sch-I, 33.1 2.5 MT

10 MT

12.5 MT

Collection, Storage, Decontamination and Disposal by selling to

scrap dealers

Spent oil Plant and

Machineries Sch-I, 5.1

50 Liters

100 Liters

150 Liters

Collection, Storage, Transportation, sell to

registered Re-processor / MoEF&CC

approved recyclers OR

Reused as lubricant

Page 125 of 126


Page 125 of 126

within premises

E*-As per Existing CTE Obtained, P*-For Proposed Expansion, T*-Total

ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.

Unit has obtained provisional certificate from Saurashtra Enviro Projects Pvt. Ltd. (SEPPL) for the disposal of hazardous waste


Not applicable


i Types of solvents, Details of Solvent Recovery, % Recovery. Reuse of recovered solvents

Existing Not Applicable Proposed for EC application (Synthetic organic chemicals) For the manufacturing of proposed products, unit will require Toluene as Solvent which will be recovered through in process/in situ distillation and reused in process.


As mentioned in section E (iii) above.

• Technical presentation was made by the project proponent. PP has obtained CTE for the in-organic

products. However, they have yet not commissioned project. PP has proposed ETP followed by

MEE & ATFD for waste water treatment and treated effluent will be discharge to GIDC drainage for

final discharge to deep Sea.






1. Copy of permission letter with quantity (KL/day) from the concern authority of drainage

network / pipeline with confirmation for spare capacity available to take additional effluent.

2. Provision for Continuous Monitoring System for waste water discharge.

3. Detailed 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.





2006.


Page 126 of 126


Page 126 of 126


Meeting ended with thanks to the Chair and the Members. --------------------------------

Minutes approved by:

1. Shri S. C. Srivastav, Vice Chairman, SEAC 2. Shri R. J. Shah, Member, SEAC.

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

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

5. Dr. Mayuri Pandya, Member, SEAC

6. Shri Rajesh I Shah, Member, SEAC