Minutes of the 341 st meeting of the ... Minutes of the 341th.pdf · Heater 5 Lac kcal/hr 11 m LDO...

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341stmeeting of SEAC-Gujarat, Dated 24.08.2017

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Minutes of the 341st meeting of the StateLevelExpertAppraisalCommittee held on 24/08/2017

at Committee Room, Gujarat PollutionControl Board, Gandhinagar.

The 341st meeting of the StateLevelExpertAppraisalCommittee (SEAC) was held on 24thAugust,

2017 at Committee Room, Gujarat PollutionControl Board, 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. Shri Natrajan Pratap, Member, SEAC.

6. Shri A. K. Mule, Member, SEAC.

6. Shri K. C. Mistry, Secretary, SEAC.

The agenda of TOR/Scopingcases was taken up. Total nine (9) cases of TOR/Scopingwere taken up.

The applicants made presentations on the activities to be carried out along with other details furnished

in the Form-1 and other reports.

1. SIA/GJ/MIS/19216/2016 M/s: Bharuch Enviro Infrastructure Limited.(BEIL) plot number 911/C, Jhagadia Industrial Estate, Dist. Bharuch

Screening and Scoping

Project proponent remained absent during meeting, hence committee decided to defer the proposal in one of the upcoming SEAC meeting.

2. SIA/GJ/IND2/19254/2017 M/s: Madhav Polymers & Plastic Industries Plot No. C1B/4737, Opp. IPCA Lab., Nr. Rallies India, Ankleshwar GIDC, Ta. : Ankleshwar, Dist. : Bharuch


Category of the unit : 5(f)

Project status: New

• This office has received an application vide their online proposal no. SIA/GJ/IND2/19254/2017

dated 07/07/2017 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.

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

Sr.

No.

Name of the Products CAS no. Quantity

MT/Month

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1. Unsaturated Polyester Resin

[General Purpose, ISO/PET

Resin , Vinyl Ester Resin, etc.]

26123-45-5 100

2. Fiber Reinforce Plastics Not

Applicable

50

• The project falls under the Category B of project activity5(f)asper the schedule of EIA Notification

2006.

• PP was called for presentation in the SEAC meeting dated 24/08/2017.

• Salient features of the project are as under:

Sr. no. Particulars Details

A Total cost of Proposed Project (Rs. in Crores): Proposed: Rs. 2.3 Crores

• Capital cost for EMS (Environmental Management System): 0.1 Crores

• Recurring cost towards the environmental protection measures:.0.05

Crores per Annum.

B Total Plot area ( sq. meter) 704 sq.m.

Green belt area,/Tree Plantation area ( sq. meter) 150 Sq.m.

C Employment generation

• Direct 10

• Indirect 10

D Water

i

Source of Water Supply

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

GIDC

Status of permission from the concern authority.

ii Water consumption (KL/day) :- 7.5 KL/day

Proposed

KL/day

(A) Domestic 4.0

(B) Gardening 0.5

(C) Industrial

Process 0.0

Washing 0.0

Boiler 0.0

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Cooling 3.0

Others 0.0

Total 7.5

iii Waste water generation (KL/day)

-

Category Proposed

KL/Day

Remarks

(A) Domestic 3.2 The generated cooling

bleed off will be mixed

with the fresh water and

utilized within the plant

premises.

(B) Industrial

Process 0.0

Washing 0.0

Boiler 0.0

Cooling 0.02

Others 0.0

Total Industrial waste

water

3.22

-

iv Treatment facility with capacity

(ETP, CETP, MEE, STP etc).

Not Applicable as there will not

be any waste water generation.

v Mode of Disposal & Final meeting point

Domestic: septic tank system.

Industrial: ---

vi Reuse/Recycle details (KL/day) ---

vii Details of rainwater harvesting ---

E Air

i Flue gas emission details

No. of Boilers/TFH/Furnaces/DG sets etc. with

capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

Sr

.

no

.

Source of

emissionW

ith

Capacity

e.g. Boiler

(8 TPH)

Stack

Height

(meter

)

Name

of the

fuel

Quantity

of Fuel

MT/hr&M

T/Day

APC

M

Type

of

emissi

ons

i.e. Air

Pollut

ants

Emission

Standard

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1. Thermic

Fluid

Heater

5 Lac

kcal/hr

11 m LDO /

Furnac

e oil

6000

Lit/month

--- PM

SO2

NOx

PM < 150

mg/Nm3

SO2 <

100 ppm

NOx< 50

ppm

2. D. G. set 10

KVA

Diesel 7.5 L/hr. --- PM

SO2

NOx

PM < 150

mg/Nm3

SO2 <

100 ppm

NOx< 50

ppm

-

iii Fugitive emission details with its mitigation measures.

F Hazardous waste

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

Movement) Rules 2016.

i

Sr.

no

.

Type/Name

of

Hazardous

waste

Source of

generation

Category

and

Schedule

as per HW

Rules,2016

Quantity

(MT/Annum

)

Disposal

Method

1. Discarded

containers/

barrels /

liners

From raw

materials

and

products

storage

mode.

33.1 1.2 MT Collection,

Storage,

transportati

on and

sold out to

Registered

Recyclers.

2. Used Oil Industrial

Operation

5.1 0.05 KL Collection,

Storage,

transportati

on and

sold out to

Registered

Recyclers.

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Quantity of all the wastes including discarded containers must be in MT/Annum.

ii Membership details of CETP, TSDF, CHWIF,

Common MEE etc.

Not Applicable

ii Details of Non-Hazardous waste & its disposal

(MSW and others)

Not Applicable

Technical presentation was made by the project proponent.Committee noted that it is proposed to

reuse Glycol mixedwater to be recovered from the Condenser in the next batch and hence there won’t

be any industrial effluent discharge from the process.Committee felt that such complete reuse of the

industrial effluent needs to be justified technically in view of no requirement of water in the

manufacturing process. Considering the above project details, after detailed discussion, the terms of

reference (ToR) were prescribed as below and as per Annexure-I for the EIA study to be done

covering10 Kmradial 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.

2. Technical justification for complete reuse of the Glycol mixed water to be recovered from

the Condenser in the next batch in view of no requirement of water in the manufacturing

process.

• The TOR prescribed as above and as per Annexure – I and the model ToRs available in the

MoEF’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.

3. SIA/GJ/IND2/19513/2017 M/S: Black Rose Ind. Ltd. Plot no. 675,GIDC-Jhagadia, Dist.: Bharuch



Project status: Expansion



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

tabulated below:

Sr. Name of the Products CAS no. QuantityMT/Month End-use

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No. Existing

Proposed

Total of

product

1.

Acrylamide Aqueous Solution (on 50% basis)

79-06-1 1,666.66 --- 1,666.66

Acrylamide polymers, etc.

2.

Polyacrylamides (Powder)

25987-30-8, 25085-02-3, 69418-26-4 9003-05-8, and other

polyacrylamides

--- 833.33 833.33

Water treatment, oilfield chemicals, etc.

3.

Polyacrylamides (Liquid) 25987-30-8, 25085-02-3, 33882-67-6, 26100-47-0,

and other polyacrylami

des

--- 3,333.33 3,333.33

Water treatment, binders, etc.

4.

Polycarboxylates 9003-01-4, and other

polycarboxylates

--- 416.67 416.67

Textiles, paints, etc.

5. N-MethylolAcrylamide

924-42-5 --- 166.67 166.67 Adhesives, etc.

Total 1,666.66 4,750.00 6,416.66

• The project falls underCategory B of project activity5(f)asper the schedule of EIA Notification 2006.



Total cost of Proposed Project (Rs. in Crores)

Existing: 37.77 Crores Proposed: Rs.60 Crores Total:97.77 crores

Total Plot area (sq. meter)

Existing: 34,075.00, Proposed: --- Total: 34,075.00 The proposed expansion will be carried out within existing premises only. No additional land will be required for the proposed expansion.

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

Existing: 12,540.00 (36.80 %) Proposed: --- Total: 12,540.00 (36.80 %)

-

Sr. no.

Particulars Details

A. Water

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i.

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

GIDC

Status of permission from the concern authority. Existing: Already obtained permission from GIDC Proposed Expansion: Application is already submitted and permission to be obtained.

ii. Water consumption (KL/day)

-

Category Existing KL/day

Proposed (Additional) KL/day

Total after Expansion

KL/day Remarks

(A) Domestic 7.5 7.5 15 ---

(B) Gardening 16.275 19.9 36.175 ---

(C) Industrial

Process 35.66 181.5 217.16 ---

Washing 1.25 2 3.25 ---

Boiler 6.38 193 199.38 ---

Cooling 46.5 155 201.5 ---

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

Total (C) 89.79 531.5 621.29 ---

Total (A+B+C) 113.565 558.9 672.465 ---

Recycle water for industrial

10.75 195 205.75 ---

Recycle water for gardening

1.815 4.9 6.715 ---

Total fresh water requirement

101 359 460 ---

-

iii. Waste water generation (KL/day)

-

Category Existing KL/Day

Proposed (Additional)

KL/day


KL/day

Remarks

(A) Domestic 7 7 14

(B) Industrial

Process 1.5 2.5 4

Washing 1.25 0.5 1.75

Boiler 0.85 12 12.85

Cooling 3.5 5 8.5

Others --- --- ---

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Total Industrial waste water

7.1 20 27.1

-

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

Capacity of ETP – 5 m3/day Capacity of RO Plant – 28.8 m3/day Capacity of MEE Plant: 7.2 m3/day

v.

Mode of Disposal & Final meeting point Domestic:Sewage generated from the industry is treated in existing septic tank /soak pit facility. The same system shall be continued after proposed expansion.

Industrial:The process effluent is being/ shall be treated in the ETP having primary and secondary treatment facilities. The treated process effluent from the ETP along with other effluent from the utilities is being/ shall be passed through the RO System. RO Permeate water and steam condensate is being/ shall be recycled back in process whereas RO reject effluent is being/ shall be completely evaporated with help of the MEE. Condensate from MEE is being/ shall be completely reused in gardening/plantation within premises. Hence, there shall be no industrial effluent discharge from the unit, i.e. zero discharge unit.

vi.

Reuse/Recycle details (KL/day) Existing: Recycle water for Industrial – 10.75 KLD Recycle water for gardening – 1.815 KLD Proposed: Recycle water for Industrial – 195 KLD Recycle water for gardening – 4.90 KLD Total: Recycle water for Industrial – 205.75 KLD Recycle water for gardening – 6.715 KLD

B Air (Existing and Proposed)

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

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-

Sr. No.

Source of emission With Capacity e.g. Boiler (8 TPH)

Stack Heig

ht (mete

r)

Name of the fuel

Quantity of Fuel MT/hr& MT/Day

Type of emissions

i.e. Air Pollutants

APCM

NAAQS (National

Ambient Air Quality

Standards)

Existing

1. *Small Industrial Boiler- Non IBR

(400 kg/hr) 30

HSD 400

Lit/Day PM < 150 mg/NM

3

SO2< 100 ppm

NOx< 50 ppm

Adequate Stack

Height with SMF

PM < 150 mg/NM

3

SO2< 100 ppm NOx< 50 ppm

2. *Small Industrial Boiler- Non IBR

(400 kg/hr) HSD

400 Lit/Day

3. **D. G. Set (380 KVA)

9 HSD 100

Lit/Day

Proposed

1.

*Boilers (total

capacity7500 kg/hr – divided

into 2 Nos.)

30 Import

ed Coal

22 MT/Day

PM < 150 mg/NM

3

SO2< 100 ppm

NOx< 50 ppm

Multi Cyclone

Separator, Bag Filter and Water Scrubber to each boiler

PM < 150 mg/NM

3

SO2< 100 ppm NOx< 50 ppm

2. **D. G. Set (500 KVA)

11 HSD 900

Lit/Day

Adequate Stack

Height with SMF

*After proposed expansion, existing small industrial non IBR boiler will be stand-by. Only proposed two boilers will be operational and total capacity witll be 7500kg/hr. **D. G. Set is being/will be used in case of emergency and/or power failure only.

-

ii.

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

-

Sr. No.

Source of emission

Type of emission Stack/Vent Height

(meter) APCM

NAAQS (National Ambient Air Quality

Standards)

There is no process gas emission from the manufacturing process from existing as well as proposed production.

-

v.

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

• Process plant building is open on all sides to provide adequate ventilation in the work areas.

• To monitor VOC gases – Online Acrylonitrile detectors have been installed at various location, and this helps in detecting any unforeseen / accidental leakage of the gas.

• In particular, wherever Acrylonitrile is stored / transferred / consumed

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these areas have been kept open to air, i.e. not enclosed by any means. This eliminates any buildup of high concentration harmful / toxic / hazardous vapors in the work environment.

• For precautionary measures, a stand by gas scrubber for Acrylonitrile shall be installed for any emergency vent of gas.

• Third party ambient air monitoring is being regularly carried out for the existing unit and same shall be continue after proposed expansion.

• Adequate sprinkling system and firefighting arrangements have been provided.

• Storage tanks of raw materials and finished products have been provided with dyke walls to hold any unforeseen spillage/leakage.

• Unit has already developed road for prevention of dust during vehicular movement.

• Use of vehicles with PUC is/will be made compulsory for transportation vehicles entering the premises.

• Adequate greenbelt area is already developed to minimize the impact of fugitive dust due to vehicular movement.

C.

Hazardous waste (As per the Hazardous and Other Wastes (Management and TransboundaryMovement) Rules 2016. (Existing and Proposed)

i.

-

Sr. No.

Type/ Name of

Hazardous waste

Source of

generation

Category and

Schedule as per HW Rules.

Quantity (MT/Annum)

Disposal Method Existing

Proposed

Total

1. Sludge from

ETP ETP 35.3 0.73 1.095 1.825 Collection, Storage,

Transportation, Disposal to TSDF site,

BEIL Ankleshwar 2. Sludge from

MEE MEE 35.3 12.775 352.225 365.00

3. Used Oil Machiner

y 5.1 1.095 10.905 12.000

Collection storage transportation sale to

the MoEF/ CPCB registered Re-refiners

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4. Discarded

drum & Containers

Process 33.1 2.0075 597.992

5 600

Collection storage transportation

decontamination and selling to the MoEF/

CPCB registered company

5. Spent

Carbon Process 36.2 71.175 84.825 156

Collection storage, transportation, It will

be incinerated in common incinerator.

6. Waste

Polymer / Off spec product

Process 35.2 40.15 319.85 360 Collection, Storage, Transportation,

Disposal to TSDF site, BEIL Ankleshwar

7. Spent resin Process 35.2 0.50 5.50 6.00

8. Empty Bags Process 33.1 0 6.00 6.00

9. Fly Ash Boiler --- 0 3180 3180

To be sold to brick manufacturers or sent

to cement manufacturing

companies.

Quantity of discarded containers is in MT/Annum.

ii

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

The industry has a valid membership of TSDF site at BEIL, Ankleshwarfor the disposal of existing hazardous waste for land fill as well as common incinerator. The industry will be obtained membership for the additional quantity of land fill and incinerator.

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

Fly ash will be sold to the brick manufacturer and/or cement manufacturing industries.

D Spent Solvent management No solvent is being/will be used in the existing as well as proposed expansion. i

VOC emission sources and its mitigation measures

Technical presentation was made by PP before the committee.Committee noted that hazardous

chemicals compounds like Acrylonitrile and Formaldehyde are going to be handled in the project and

hence PP was asked to take all necessary safety measures for the same. Committee also asked the

PP to take adequate safety measures for control of runaway reaction. Committee observed that MEE

condensate to be discharged on land within the premises for gardening purpose will increase from

existing 1.815 m3/day to 6.715 m3/day after the proposed expansion. Upon noticing that PP is going to

change fuel from HSD in existing low capacity Boilers (2 no. X 400 kg/hr each) to Coal in proposed

high capacity Boilers(2 no. X 7500 kg/hr each) after the proposed expansion, the committee asked the

PP to furnish type & quality of coal to be used and to get the APCMs designed accordingly. Upon

watching the photographs of existing green belt, the Committee asked the PP to take up the massive

plantation including road side plantation within the premises and to sow high canopy trees. Considering

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the above project details, after detailed discussion, the terms of reference (ToR) were prescribed as

below and as per Annexure-I for the EIA study to be done covering10 Kmradial distance from the

project boundary.

1. Quality of MEE condensate water along with analysis reports of the samples collected by

the GPCB. Adequacy of the land area for complete utilization of 6.715 m3/day of MEE

condensate water for plantation / gardening. Plan for storage / utilization of MEE

condensate water during high rainy days when soil is water saturated and not in a position

to take MEE condensate water.

2. Source, type and quality of coal proposed to be used in new Boilers (2 no. X 7500 kg/hr

each) along with reports of its ultimate / proximate analysis. Inlet parameters considered in

designing of APCM based on the coal quality and design adequacy of the proposed APCM

for achieving GPCB norms at the stack outlet.

3. Safety measures for handling and storage of Acrylonitrile and Formaldehyde.

4. Safety measures for control of runaway reactions.

5. Details on measures proposed for preventing ground water contamination.


MoEF&CC’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


4. SIA/GJ/IND2/19276/2017 M/s. Ester India Plot No. 128/29-30, GIDC-Nandesari, Dist.: Vadodara.







tabulated below:

Sr. No.

Product Name CAS No.

Existing As Per CCA

No.- 84186 in MT/Month

Proposed Quantity

in MT/Month

Total Capacity

MT/ Month

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Hydantoin Derivatives

1. Dimethyl Hydantoin 174-177

27 And/or

223 And/or

250 And/or

2. Dibromo dimethyl Hydantoin 157-902

3. Dichloro dimethyl Hydantoin 77-48-5

4. Bromochloro dimethyl hydantoin 16079-88-2

5 Amino Isobyturic Acid 62-57-7

Personal Care & Cosmetics Ingredients

6. Dimethylol Dimethyl Hydantoin 6440-58-0.

7. Di hydroxyethyl Dimethyl Hydantoin

26850-24-8.

8. Blends of Dimethylol Dimethyl Hydantoin and the variants

6440-58-0

Pharma Advanced Intermediates

9. 2-Hydroxy- 5-Methylphenyl Benzotriazole

2440-22-4 0.025 0.0 0.025

10. 5-Chloro-4-[(2-imidazoline- 2yl) amino]-2,1,3-Benzothiadiazol

64461-82-1 0.020 0.0 0.020

11. 5-Chloro-4-amino-2,1,3-Benzothiadiazole-Hydrochloride

30536-19-7 0.020 0.0 0.020

12. 1-(4-cyanopheyl)methyl-1 ,2,4- triazole

212248-62-9. 0.100 0.100 0.200

13. 4,4-(1 H- 1,2,4-Triazole-I-Y methylene bisbenzonitrile

212248-62-9 0.025 0.075 0.100

14. (2-(2- Nitroanilino)- 5- methylthiophene)- 3-carbonitrile (OLZ-II )

138564-58-6, 0.050 0.050 0.100

15.

4-Amino-2-Methyl-10H- THIENO[2, 3-b](1,5) benzediazapine HCL ( OLZ -III )

--

0.050 0.050 0.100

Sartan Series Products 4.1 15.9 20

16. 4-Chloromethyl -5-Methyl-2,1,3,- Dioxolenedione

137365-09-4

4.1 And/or

15.9 And/or

20 And/or

17. Bromo OTBN 114772-54-2

18. 4-(2-butyl-4-chloro 5-hydroxymethyl)imidazolymethyl-biphenyl –carbonitrile (LOS-II)

124750-51-2

19. 4- Bromo- 2-methoxyimino- 3- oxobutyric acid

75689-09-7

20. 4-methyl-biphenyl-2-carboxylic acid

114772-34-8

21. 4-methyl-biphenyl-2- carboxylic `acid-methyl ester

114772-34-8

22. R & D Products -- 0.510 9.490 10

Total (Existing) 31.9 248.665 280.565

Proposed New Products

1. Phenyl Ethyl Chloride (LIS-I) 58274-32-1

2.

3-Ethyl-4-phenyl-2-oxobutyrate (LIS-II)

6296-54-4

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3. LIS-III (L-Proline Benzyl Ester Hydrochloride)

2133-40-6 0 And/or

20 And/or

20 And/or

4. Isopropyl Trifluoroacetate Route-1 & Route-2 (LIS-5)

400-38-4.

5. S-2-AminobutyramideTartarate (SABAM TA) and/or

141109-14-0.

6. S-2-Aminobutyramide Hydrochloride (SABAM HCl)

7682-20-4.

7. Ethyl Trifluoroacetate 383-63-1.

8. 4-Nitro 1H-imidazole (LARM-61) 705-19-1

9. 2-chloro ethyl morpholineHCl (LARM-62)

3647-69-6.

10. ANCP (2-Amino-6-chloro-3-nitropyridine)

27048-04-0

11. Diketone 431-03-8

12. Phenylglycine 2835-06-5

13. Venelafaxine Stage I & Stage II 99300-78-4.

14. P-Sulfonyl benzoic acid potassium salt (SB-201)

3871-99-6

15. 5-Chlro-2, 3-Disulfonamide Aniline (DS-201)

1635-61-6.

16. 3-amino-1,2-propanediol (AP-301)

616-30-8

17. N-Methyl-Aminomethyl Naphthalene (NM Base)

65473-13-4

18. Ethyl 2-(4-hydroxyphenyl)-4-methylthiazole-5-carboxylate (FB-1)

161797-99-5

19. Ethyl-2-(3-Cyano-4-isobutoxyphenyl)-4-methyl-1,3-thiazole-5-carboxylate (FBT)

160844-75-7

20. Exo,Exo-2,3-Camphanediol (CDO)

56614-57-4

21. 3-Ethyl-4-methyl-pyrolidine-2-one (GP1)

872-50-4

22. Adrenaline (ADIF) --

23. trans-4-aminocyclohexanol 27489-62-9

24. Isoproternol (ISL) 51-30-9

25. Azobisisobutyronitrole (AIBN) 78-67-1

26. Isophthalic Acid 121-91-5 0.0 30 30

27. Trityl Methyl Ether and/or 596-31-6 0.0 40 And/or

40 And/or 28. Trityl Chloride 76-83-5

Personal Care & Cosmetics Ingredients

29. Ethyl Hexyl Glycerine & variants 70445-33-9 0.0 20 20

30. Allantoin and similar additives 97-59-6 0.0 5 5

Total (Proposed) 0.0 115 115

Total (Existing + Proposed) 31.9 363.665 395.565

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Total cost of Proposed Project

(Rs. in Crores):

Existing: Rs. 0.97 Crores Proposed: Rs. 0.67 Crores Total: Rs. 1.64 Crores

Total Plot area ( sq. meter)

Existing: 1602 sq. m. Proposed: 0 Total: 1602 sq. m.

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

Existing: 28 sq. m. Proposed: 155 sq. m. Total: 183 sq. m.

--

Sr. no.

Particulars Details

A Water

i


GIDC Nandesari

Status of permission from the concern authority. Confirmed Permission

ii Water consumption (KL/day)

-

Existing KL/day


Total after Expansion KL/day

Remarks

(D) Domestic 1 1 2

(E) Gardening 1 5 6

(F) Industrial

Process 18.1 61.9 80

Washing

Boiler 0.2 2 2.2

Cooling 3.7 10 13.7

Others 0 0 0

Total (A+B+C) 24 79.9 103.9

-


-




Remarks

(C) Domestic 0.8 0.8 1.6

(D) Industrial

Process 18.1 97.9 116

Washing

Boiler 0.1 1.9 2

Cooling 1.11 2.89 4

Others 0 0 0

Total Industrial waste 20.11 103.49 123.6

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water

-

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

ETP and treated effluent will be sent to CETP, Nandesari.


Domestic:Soakpit

Industrial: CETP

vi Reuse/Recycle details (KL/day) 0

vii Details of rainwater harvesting Rain water harvesting will be carried out through roof tops.

B Air(Existing and 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.

Stack Attached To

Stack Height (M)

Type of Fuel

Fuel Consumption

Type of Emission

Permissible Limit

APCM

EXISTING As Per CCA No.-AWH-84186

1. Boiler 11 Natural

Gas 2400

SCM/Month

SPM

SO2

NOx

150 mg/NM3

100 PPM 50 PPM

--

2. Thermic

Fluid Heater

11 Natural

Gas --

3. D.G. Set 11 HSD 20 Lit/Hr.

SPM

SO2

NOx

150 mg/NM3

100 PPM 50 PPM

--

Proposed

1. Boiler 30 Natural

Gas 220

SCM/hour SPM

SO2

NOx

150 mg/NM3

100 PPM 50 PPM

--

2. Boiler 30 Bio

Coal 350 kg/hour

Multi Dust

Collector

3. D.G. Set 11 HSD 40

Lit / Hr

SPM

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.

Stack Attached To

Stack Height In

Meter

Probable Pollutant Emission

Permissible Limit

APCM

Existing As Per CCA No.-AWH-84186

1. Reactor 12 HCl Cl2

HBR

20 mg/Nm3 09 mg/Nm3 30 mg/Nm3

Venturi Lime

Scrubber

Page 17 of 56


Page 17 of 56

2. Reactor 12 NH3 175 mg/Nm3 Acid

Scrubber

3. Spin Flash

Dryer 11 PM 150 mg/Nm3

Dust Collector, Bag Filter

Proposed

1. Reactor 11 NH3 175 mg/Nm3 Acid

Scrubber

2 All Reactors 11

SO2

HCl Cl2 Br2 HBr

40 mg/Nm3 20 mg/Nm3 09 mg/Nm3 09 mg/Nm3 20 mg/Nm3

Water Venturi

Scrubber Followed By

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.

Type/Name of Hazardous waste

Source of generation

Category and Schedule as per HW Rules.

Quantity after proposed expansion (MT/Annum)

Disposal Method

1

ETP Sludge

ETP 35.3 1420 Disposal at TSDF of Nandesari Environment Control Ltd. (NECL)

2 Discarded Containers

Raw materials

33.3 10 Decontamination within company premises

3

Spent Carbon

Process and ETP

28.3 4 Disposal at CHWFI for incineration facility/ co processing

4

Distillation residue

process 20.3 720 Disposal at CHWFI for incineration facility/ co processing

Quantity of discarded containers must be in MT/Annum.

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

Will be provided in EIA report

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

Non-Hazardous waste will be disposed to GPCB authorized disposers and

Page 18 of 56


Page 18 of 56

as per new hazardous and other wastes rules, 2016.

D

i Spent Solvent management (If any)

Solvent recovery system will be provided in order to recover 92% to 95% of Solvent.

ii VOC emission sources and its mitigation measures

Closed loop systems, double mechanical seal pumps will be provided to reduce VOC as minimum as possible.

Technical presentation was made by PP before the committee.Committee noted that the unit is going

to use hazardous chemicals like Chlorine, Bromine, Ammonia, Thionyl Chloride, Formaldehyde etc. as

well as many Volatile Organic Compounds and hence,Committee desired to have MSDS of materials

to be handled, information on storage of each hazardous chemical and safety measures thereof.

Considering that effluent discharge to CETP of Nandesari Environment Control Ltd, (NECL) is going to

increase after the proposed expansion, the Committee asked the project proponent to submit a

permission letter from the NIA, Nandesari for the additional effluent quantity. Committee emphasized

on reuse of treated waste water instead of sending to CETP. PP informed that they will explore the

possibility to reuse treated waste water. Committee also asked the PP to take adequate precautions for

preventing ground water contamination. Considering the above project details, after detailed

discussion, the terms of reference (ToR) were prescribed as below and as per Annexure-I for the EIA

study to be done covering10 Kmradial distance from the project boundary.

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


2. Safety measures for handling and storage of Chlorine, Bromine, Ammonia, Formaldehyde,

Thionyl Chloride, Volatile Organic Compounds and other hazardous chemicals.

3. Explore possibility to reuse treated waste water and to reduce waste water discharge to

CETP.

4. Details on measures proposed for preventing ground water contamination.




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


Page 19 of 56


Page 19 of 56

5 SIA/GJ/IND2/19240/2017 M/s: Kangaroo Industries Plot No. D-2/CH/79, GIDC, Dahej-2 Industrial Estate, Dahej, Dist. Bharuch



Project status: New




Sr. No.

Name of the Products

CAS no. Quantity MT/Month

Enduse of

product

1 2-Chloro 5-Toludine 4-

Sulphonic Acid (CLT Acid)

88-51-7

150

Pigment

2 2-Chloro 4-Aminotoluene 5-

Sulphonic Acid (2B Acid)

88-51-7

25

Pigment

3 4-Aminotoluene 3-Sulphonic

Acid (4B Acid)

88-44-8

25

Pigment

OR

ANY ONE ABOVE 200

4 AZO Pigment - 50 Inks / Paints

Total 250




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

Project Cost: Rs. 600 Lakh &

EMS: Rs. 50 Lakh (Approximately)


7430.90 Sq. m.


1486.18 Sq. m.

-

Sr. no.

Particulars Details

A Water

Page 20 of 56


Page 20 of 56

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

GIDC Water Supply System


Permission has been taken from GIDC

ii. Water consumption (KL/day) – 40 KL / day

Existing KL/day

(A) Domestic 4.75

(B) Gardening 1.25

(C) Industrial 34

Process 29

Washing 01

Boiler 02

Cooling 01

Others 01

Total (A + B + C) = 40

iii. Waste water generation (KL/day) – 32 KL /day


Remarks

(A) Domestic 4.75

(B) Gardening 1.25

(C) Industrial 32

Process 29.60

Washing 01.00

Boiler 00.20

Cooling 00.20

Others 01.00


32.00

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

ETP – 32 KLD

v. Mode of Disposal & Final meeting point Domestic: Soak Pit & Septic

Tank

Page 21 of 56


Page 21 of 56

Industrial: ETP& then CETP

vi. Reuse/Recycle details (KL/day) -

B Air


SR. no.

Source of emission With Capacity e.g. Boiler

Stack Height

(meter)

Name of the

fuel

Quantity of Fuel MT/hr&

MT/Day

APCM Type of emissions i.e. Air

Pollutants

Emission Standards

1. Non IBR

Boiler

(1 TPH)

11

Meter

Natur

al

Gas

2000

M3/day

- SO2 100 ppm

NOx 50 ppm

SPM 150 mg/Nm3

2. DG Set

(250KVA)

11

Meter

diesel 5000 Ltr

/ month

(apprx.)

- SO2 100 ppm

NOx 50 ppm

SPM 150 mg/Nm3

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

Sr. no.

Source of emission

Stack/Vent Height (meter)

APCM Type of emissions i.e. Air Pollutants

Emission Standards

1 From

Reaction

Vessel

09 Meter

Alkali

Scrubber

followed by

water

scrubber –

2 followed

by water

scrubber - 1

HCl

20 mg/Nm3

Cl2

09 mg/Nm3

v Fugitive emission details with its mitigation measures. – Not Applicable

Page 22 of 56


Page 22 of 56

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

i.

Sr. no



Category and Schedule as per HW Rules

Quantity ( MT/Annum)

Disposal Method

1 Discarded Container/Bags

Storage of Raw material

34.2 1500 Nos Collection, Storage, Transportation, Disposal by selling to registered recycler

2 Used oil Process 5.1 12

3 ETP Sludge ETP 34.2 25 Collection, Storage, Transportation, Disposal to TSDF.

4 Iron Sludge Process 21.1 5000

Quantity of all the wastes including discarded containers must be in MT/ Annum.

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

Membership of BEIL discharge hazardous landfill waste of Qty. 400MT/Month

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

D Solvent management Relevant details will be covered in EIA report.

ii. Details of solvent recovery

iii. VOC emission sources and its mitigation measures

Technical presentation was made by PP before the committee.Committee noted that the industrial

wastewater generation will be 32 KL/day. PP has proposed to treat the industrial effluent to the extent

to achieve the GPCB norms and to discharge treated effluent into the GIDC drainage line until the

CETP is commissioned in Dahej. PP has also proposed that after the CETP is made operative in

Dahej, effluent will be treated to the extent to achieve the CETP inlet norms and effluent will be sent to

the CETP then after. Committee felt that such flexibility can’t be allowed and it would be difficult for the

industry to achieve the GPCB norms looking to the product profile. Hence, the Committee suggested

the PP to achieve Zero Liquid Discharge (ZLD) until the CETP is made operative in Dahej, which was

agreed to by the project proponent. Committee also asked the PP to explore feasibilities of going for

hydrogenation instead of using CI powder for reduction in order to eliminate generation of iron sludge.

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

Page 23 of 56


Page 23 of 56

prescribed as below and as per Annexure-I for the EIA study to be done covering10 Kmradial distance

from the project boundary.

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


2. Project implementation schedule vis-a-vis schedule for establishment of CETP-Dahej.

3. Proposal to Zero Liquid Discharge (ZLD) until the CETP is made operative. The proposal

should include technical details of all the proposed ETP units along with adequacy report

from Schedule I auditor.

4. Explore feasibilities to go for hydrogenation instead of conventional iron-acid reduction for

elimination of iron sludge generation.

5. Safety measures for handling and storage of Chlorine, Bromine, Ammonia, Volatile Organic

Compounds and other hazardous chemicals.

6. Details on measures proposed for containment of accidental spillages / leakages and for

preventing ground water contamination.

7. Explore the possibilities for co-processing of the Hazardous waste prior to disposal into

TSDF/CHWIF.




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


6 SIA/GJ/IND2/19767/2017 M/s: GREEVA Plot no. C 1 5513 5514, Phase III, Vatva- GIDC, Ahmedabad.





Page 24 of 56


Page 24 of 56


• This is an existing unit engaged in manufacturing of Synthetic organic chemicals [(Textile Auxiliary

Chemical (Blending & Mixing)]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 Textile Auxiliary Chemical (Blending & Mixing)

- 2000 0 2000 Used in Textile processing

2

Textile Auxiliary Chemical (Synthesis)

Such as;

Washing off Agent, Soaping Agent, Binders, Sizing Agent, Alkali Buffer

Acid Buffer, Bleaching Agent, Loop Accelerator, Peroxide Killer, Lubricant

Carrier, Defoamer, Scroping Agent, Yarn Lubricant, Sequestering Agent, Stain Remover, Wax emulsion, Dyefixer-1

Dyefixer-2, Cationic Softener, Mercerising Agent, Retarding Agent, Wetting Agent – 1, Wetting Agent – 2, Resin, Fatty Ester, Adhesive, Silicon Oil, Bleaching Agent (Powder)

- 0 3000 3000 Used in Textile processing

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

2006.



-

Sr. no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing: 1.5 Proposed: 3.10 Total: 4.6

B Total Plot area ( sq. meter)

Existing: 1737 m2

Proposed: 314 m2 Total: 2051 m2

Page 25 of 56


Page 25 of 56


Existing: 225 m2 Proposed: 84 m2 Total: 309 m2


Direct Existing: 21 Proposed:20 Total:41

Indirect Existing: Proposed: Total:

D Water i


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

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

ii

Water consumption (KL/day)

Existing KL/day



Remarks

(G) Domestic 1 1 1

(H) Gardening - - -

(I) Industrial

Process 30 40 70

Washing 19 0 19

Boiler 15 10 25

Cooling 5 4 9

Others - - -

Total (A+B+C) 125

iii

Waste water generation (KL/day)




Remarks

(E) Domestic 0.5 0 0.5 Disposed to Soak Pit

(F) Industrial Treated in ETP of capacity 75 KLD & treated water is going to CETP for further treatment

Process 0 0 0

Washing 21 -1 20

Boiler 0.5 0.5 1

Cooling 0.5 0.5 1

Others - - -


22.5 0 22.5

Page 26 of 56


Page 26 of 56


The industrial effluent is treated in ETP of capacity 75 KLD & treated water is going to CETP for further treatment.


Domestic: To Soak Pit

Industrial: The industrial effluent is treated in ETP of capacity 75 KLD & treated water is going to CETP for further treatment.

vi Reuse/Recycle details (KL/day) -

vii Details of rain water harvesting -

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

e.g. Boiler (8

TPH)

Stack

Height

(meter)

Name of the

fuel

Quantity of

Fuel

MT/hr&

MT/Day

Type of

emissions i.e.

Air Pollutants

APCM

NAAQS

(National

Ambient Air

Quality

Standards)

Existing

1 Boiler (1

TPH) 12

Natural Gas from

Adani Pipeline

70 m3/Hr.

Particulate Matter,

SO2, NOx N/A

PM- 100 ppm, SO2

– 80 µg/m3,

NOx - 80 µg/m3

Proposed

1 Boiler (2

TPH) 12

Natural Gas from

Adani Pipeline

140 m3/Hr.

Particulate Matter,

SO2, NOx N/A

PM- 100 ppm, SO2

– 80 µg/m3,

NOx - 80 µg/m3

2 D.G Set

(250 kVA) 12 Diesel 40 Lit/Hr.

Particulate Matter,

SO2, NOx N/A

PM- 100 ppm, SO2

– 80 µg/m3,

NOx - 80 µg/m3

-

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

-

Page 27 of 56


Page 27 of 56

Sr. no. Source of emission Type of

emission

Stack/Vent

Height (meter)

APCM

NAAQS

(National

Ambient Air

Quality

Standards)

There is no Process vent

-

iii Fugitive emission details with its mitigation measures. [Existing & Proposed] There is no any kind of fugitive emission in present products as well as proposed products.

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

i

Sr. no.

Type/Name of

Hazardous waste


Category and

Schedule as per

HW Rules.

Quantity (MT/Annum)

Disposal

Method Existing Proposed Total

1 ETP Sludge ETP 35.3 60 MT - 60 MT

Packed in

HDPE Bags, and

Dispose to

TSDF

2 Used Oil Machinery 5.1 - 0.1 KL 0.1 KL

Disposal by

selling to

register recycle

r

3 Discarded

Container/Liners

Manufacturing Process

33.1 2400000 MT/Annu

m

600000 MT/Annu

m

3000000 MT/Annu

m

Disposal by

selling to

register recycle

r



CETP:Membership Certificate of M/s. The Green Environment Services Co-op. Society Ltd. For Effluent Treatment

Page 28 of 56


Page 28 of 56

ICHWMF: Membership Certificate of M/s. Saurastra Enviro. Projects Pvt. Ltd. For Hazardous Waste

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

Not Applicable

G Solvent management (If any)

i Details of Solvent recovery (As per respective ToR) Not Applicable

ii VOC emission sources and its mitigation measures Not Applicable

Technical presentation was made by the project proponent. Committee noted that it is an existing unit

in the Vatva GIDC estate and located just adjacent to the residential flats. Hence, committee asked the

project proponent to be extra cautious and take all necessary measures to ensure that the nearby

residents are not affected due to industry operations. PP ensured for adequate VOC control measures

and minimum solvent losses during handling and storage of chemicals. Committee desired to have

technical justification for not increasing waste water generation in spite of increase in

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

(ToR) were prescribed as below and as per Annexure-I for the EIA study to be done covering10

Kmradial distance from the project boundary.



2. Details on provisions of barriers if any proposed towards residential flats on back side and

measures proposed for control of VOCs and noise to ensure that nearby residents are not

affected due to plant operation.


MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be




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

7. SIA/GJ/IND2/19872/2017 M/s. Krishna Enterprise Plot No. 7612, GIDC Estate, near Karmatur Chokdi, Ankleshwar, Dist- Bharuch.



Project status: New

Page 29 of 56


Page 29 of 56




Sr. No.

Name of the Products

CAS no. Quantity MT/Month

End-use of product

1. Dimethylaminoethyl chloride hydrochloride

4584-46-7 120 MT/Month

(Any product

manufacture maximum

10 MT/Month)

Pharmaceutical Industry

2. Diethylaminoethyl chloride hydrochloride

869-24-9

3. Bis-(2-chloroethylamine) hydrochloride

821-48-7

4. Mannichhydrochloride

119812-29-2

5. Dimethyl amino propyl chloride HCl

5407-04-5

6. Chlorohexanone 822-87-7

7.

Di Methyl Amino Iso Propyl Chloride Hydrochloride. (DMIPC HCl)

4584-49-0

8. Meta Bromo Anisol 2398-37-0

9. Trityl Chloride (Chlorotriphenyl methane) (TTC)

76-83-5

10. 4-(2-Chloro Ethyl) MorpholineHCl (CEM HCl)

3647-69-6

11. Cyclo Propyl Carbonyl Chloride

4023 -34-1

12.

Para Hydroxy PhenylEthyl Amine HCl (Tyramine HCl)

62-31-7

13. Iso Butyl Bromide 78-77-3 30 MT/Month Either/Or

Pharmaceutical

14. Propyl Bromide 106-94-5

15. Hexyl Bromide 111-25-1

16. Tetra Butyl Ammonium Bromide

1643-19-2

17. Methyl Acetate 79-20-9 Glues, paints, chemical industry

18. Ethyl Acetate 141-78-6

19. Hexyl Acetate 142-92-7

Total 150 MT/Month


2006.


Page 30 of 56


Page 30 of 56


Total cost of Proposed Project (Rs. in Crores): 2 Crores

Total Plot area ( sq. meter) 1521 sq. meter

Green belt area,/Tree Plantation area ( sq. meter) 501 sq. meter

-

Sr. no.

Particulars Details

A Water

i


GIDC


ii

Water consumption (KL/day)

Purpose Total fresh water consumption (KL/Day)

Total recycle water consumption (KL/Day)

Total Water consumption (KL/Day)

(J) Domestic 5 0 5

(K) Industrial

Process 7 10 17

Washing 0 3 3

Boiler 5 0 5

Cooling 0 3 3

Gardening 1 0 1

Total(B) 13 16 29

Total (A+B) 18 16 34

iii

Waste water generation (KL/day)

-


Remarks

(G) Domestic 4

(H) Industrial

Process 16

Washing 3 For reactor washing

Boiler 1

Cooling

Others 0


20

-


ETP: 16 KLD CETP: 4 KLD


Domestic: Soak Pit

Industrial: 4 KLD concentrated effluent to the

Page 31 of 56


Page 31 of 56

Common MEE and 16 KLD will be treated in ETP and reused within unit.

vi Reuse/Recycle details (KL/day) 16 KLD

B Air


-

SR.

no.

Source of

emission

With

Capacity

e.g. Boiler

(8 TPH)

Stack

Height

(meter)

Name

of the

fuel

Quantity

of Fuel

MT/hr&

MT/Day

APCM

Type of

emissions

i.e. Air

Pollutants

Emission

Standards

1. Boiler (2

Ton/hr.)

15 Natural

Gas

110

m3/Day ----

Particulate Matter SO2

NOx

150 Mg/Nm3

100 ppm 50 ppm

2.

Thermic

fluid heater

(1 lac k

cal/Hr)

3. DG set (2

Nos) 09 Diesel

130

Liter/Hr -----

Particulate Matter SO2

NOx

s150 Mg/Nm3

100 ppm 50 ppm

-

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

-

Sr.

no.

Source of

emission

Stack/Vent

Height

(meter)

APCM

Type of

emissions

i.e. Air

Pollutants

Emission

Standards

1 Reactor Vents

17 Alkaline Scrubber

SO2 HBr HCl Br2

40 mg/Nm3

30 mg/Nm3

30 mg/Nm3

2 mg/Nm3

2 Reactor Vents

17 Acid

Scrubber NH3

175

mg/Nm3

-

v Fugitive emission details with its mitigation measures.

Page 32 of 56


Page 32 of 56

Sr. No.

Source Probable Pollutant Emission

Proposed Control Measures/ APCM

FUGITIVEEMISSION

1 Solvent storage tank Air pollutant (VOC)

i) Carry out work place area monitoring to find out concentration level in ambient air Close handling system. ii) Provision of breather valve cum flame arrester.

2 Solvent recovery system Air pollutant (VOC)

i) Solvent recovery system with steam condensation system. ii) Pumps & motors are mechanical seal type.

3 Handling of raw material bags in storage area

Air pollutant (PM)

i) Provision of exhaust ventilation Provision of PPE. ii) Provision of Job rotation to reduce exposure.

4 Flange joints of pipeline, pump & motors

Air pollutant (VOC)

i) Routine &periodic inspection to check leakage.

ii) Preventive maintenance, Follow SOP for maintenance.

iii) Pumps & motors will be mechanical seal type.

iv) LDAR program will be followed.

Provision of Flange guard.

5 Solid raw material transferring to reactor

Air pollutant (PM)

Hopper will be provided with powder transfer system.

6 Liquid raw material transferring to reactor

Air pollutant (VOC)

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

7 Loading /unloading at storage area

Air pollutant (VOC)

Unloading through pipeline to tank in a close system.

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

i

Sr. no.




Quantity (MT/Annum)

Disposal Method

Page 33 of 56


Page 33 of 56

1. Used Oil From Lubrication

5.1 300 Lit/Year Collection, Storage, Sold to MoEF Approved Vendors.

2. Discarded Bags/ Barrels

From Storage

33.3 7200 Nos./Year

Collection, Storage, decontamination, Sold to GPCB approved Vendors.

Liners 60 MT/Year

3. ETP Sludge From ETP Plant

34.3 40 MT/Year ETP Sludge will Be Disposed to BEIL, Ankleshwar

4. Process waste

From different process

34.2 10 MT/Year Disposed to BEIL

5 Spent Carbon

From Process

35.3 5 MT/Year Disposed to BEIL,Ankleshwar.



Attached as Annexure-1.


MSW will be collected by Notified authority.

D

i Solvent management (If any) Details of Solvent recovery (As per respective ToR)

Solvent will be recover about 96% as the part of Process.

ii VOC emission sources and its mitigation measures From solvent recovery and carbon tower will be provide to mitigate it.

Technical presentation was made by the project proponent. Committee noted that it is proposed to

send high concentrated wastewater to CETP for treatment whereas low concentrated effluent is

proposed to be treated in the ETP and reused in the plant. PP clarified that high concentrated

wastewater will be sent to Common MEE of M/s. ETL for its evaporation and not to the CETP for

treatment. ETL MEE will not send condensate to CETP of ETL. Considering the above project details,

after detailed discussion, the terms of reference (ToR) were prescribed as below and as per Annexure-

I for the EIA study to be done covering10 Kmradial distance from the project boundary.



Page 34 of 56


Page 34 of 56

2. Safety measures for handling and storage of Solvents, Hydrogen, Bromine, Ammonia and

other hazardous chemicals.

3. Details on measures proposed for containment of accidental spillages / leakages and for

preventing ground water contamination.

4. Explore the possibilities for co-processing of the Hazardous waste i.e. process waste, spent

carbon etc. prior to disposal into TSDF/CHWIF.


MoEF’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be




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

8 SIA/GJ/IND2/19877/2017 M/s: Aarti Industries Limited(Unit-II) Plot No. Z/103/D, GIDC Estate, SEZ-II Dahej, Bharuch







Sr. No.

Name of Product CAS no. Total

quantity in MT/Month

1. 2, 5 Dichloro Aniline 95-82-9 1815

2. 2,5 Di Chloro Phenol 583-78-8 1500

3. Nitrosyl Sulphuric Acid 7782-78-7 1470

4. 98% Sulphuric Acid 7664-93-9 2350

Total 7135 MT/Month

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



Sr. no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Total: 178.4

• Capital cost for EMS (Environmental Management System):.12.4 Crores

B Total Plot area Total: 57970 sq. m.

Page 35 of 56


Page 35 of 56

( sq. meter)


Total: 17391 sq. m.


• Direct Total: 134

• Indirect Total: 50

D Water i


Dahej SEZ



Proposed New KL/day

(L) Domestic 50

(M) Gardening 50 (Recycled from Domestic)

(N) Industrial

Process 251

Washing 10

Softener 1117

Cooling(water from softener will be used)

1092*

Others --

Total 1428 (Fresh) + 50 (Recycled)


-

Category Proposed new KL/Day

Remarks

(I) Domestic 50 Recycled back to gardening

(J) Industrial

Process 289

Washing 10

Softener reject 25

Cooling 156

Others --


530

-


Primary, Secondary and tertiary treatment Plant: 480 KLD


Domestic: STP

Industrial: GIDC Pipeline

vi Reuse/Recycle details (KL/day) 50 KLD

Page 36 of 56


Page 36 of 56


E Air i Flue gas emission details

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

-

SR.

no.

Source of

emission

With

Capacity

e.g. Boiler (8

TPH)

Stack

Height

(meter)

Name

of the

fuel

Quantity

of Fuel

MT/hr&MT/

Day

APCM

Type of

emission

s i.e. Air

Pollutant

s

Emission

Standard

s

1

D.G. Set (Standby) (2 Nos)

Capacity= 1500 KVA

(Each)

11 Diesel

660

Litre/Hr. -- PM SO2

NOX

150mg/ Nm3 100 ppm

50ppm

-


-

Sr.

no.

Source of

emission

Stack/Ve

nt

Height

(meter)

APCM

Type of

emissions

i.e. Air

Pollutants

Emission

Standards

1

Scrubber connected to Sulphur Dioxide reaction and Sulphuric Acid Plant

30 Alkali Scrubber

SO2 40 Mg/Nm3

2 Scrubber connected to NSA

11 Alkali Scrubber

SO2 40 Mg/Nm3

3

Scrubber connected to DCP

11 Water Scrubber and Alkali Scrubber

NOX VOCs

25 Mg/Nm3 --

4 Scrubber connected to tanks

11 Water Scrubber

VOCs --

Page 37 of 56


Page 37 of 56


11 Water Scrubber

VOCs --

-

iii Fugitive emission details with its mitigation measures.

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

i

Sr. no.




Quantity

Disposal Method

1 ETP Waste ETP 35.3 400

MT/Month

Collection, Storage, Transportation, disposal to TSDF.

2 Distillation Residue

Process 36.1 350

MT/Month

Collection, Storage, transportation, disposal at CHWIF

3 Gypsum Process 34.3 600

MT/Month

Collection, Storage, Sold to Cement Industry or sent to TSDF site.

4 Sulphur Sludge Process B2040 7

MT/Month

Collection, Storage, transportation, disposal at TSDF

5 Discarded containers/bags

Raw Materials

33.1 Whatsoev

er

generated

Collection, Storage, Decontamination, Disposal by sold to authorize recyclers.

6 Used oil Maintenance 5.1 500Lit/Mo

nth

Collection, Storage, Transportation, Disposal by selling to registered re-processors.

Page 38 of 56


Page 38 of 56

7 Insulation Waste

Process -- Whatsoev

er

generated

Collection, Storage, Transportation disposal by at TSDF Site.

8 Spent Carbon ETP and Process

28.3 5

MT/month

Collection, Storage, transportation, sent for co-processing

9 Off Specification Product

Process 36.1 Whatsoev

er

generated



Membership will be given in EIA Report


Non-Hazardous waste will be disposed to GPCB authorized disposers and as per new hazardous and other wastes rules, 2016.

G Solvent management (If any)

i Details of Solvent recovery Solvent recovery system with double Condenser, cooling followed by chilling will be provided in order to recover 92% to 95% of Solvent.

ii VOC emission sources and its mitigation measures Closed loop systems, double mechanical seal pumps will be provided to reduce VOC as minimum as possible.

Technical presentation was made by the project proponent. Committee noted that total water

consumption will be 1432 KL/day and total industrial wastewater generation will be 480 KL/day.

Committee felt that though the product profile and production quantum of proposals for Dahej and

Jhagadia units are different industrial wastewater generation is shown as same, which is not

convincing. Hence, the Committee asked the PP to resubmit both the proposals with realistic and

correct data on water consumption, wastewater generation, etc.Committee asked to give specific name

of the solvents to be used as a raw material. After detailed discussion, Committee decided to take up

the case for scoping only after submission of revised proposal with correct details including the

following:

1. Status of GIDC pipeline for discharge of treated effluent and permission letter from the concern

authority.

Page 39 of 56


Page 39 of 56

2. Product wise factual details like raw materials, water consumption, waste water generation,

Hazardous waste generation, source its management, manufacturing process with mass

balance etc.

3. Management of spent acid streams as per the Hazardous waste rules 2016.

4. Waste water segregation scheme and its treatment method.

5. Action plan for maximum reuse of treated waste water instead of discharge into GIDC drainage.

6. Proposal CEMS for air emission and waste water discharge.

9. SIA/GJ/IND2/19878/2017 M/s: Aarti Industries Limited(Unit-III) Plot No. 778 GIDC Estate, Jhagadia, Dist.: Bharuch



Project status: New




Sr. No.

Name of Product CAS No. Total


5. 2,5 Di Chloro Nitro Benzene

89-61-2 2165

6. 2, 5 Dichloro Aniline 95-82-9 1815

7. 2,5 DiChloro Phenol 583-78-8 1500

8. Nitrosyl Sulphuric Acid 7782-78-7 1470

9. 98% Sulphuric Acid 7664-93-9 2350

10. Hydrogen 1333-74-0 3000Nm3/Hr.

Total -- 9300 MT/Month + 3000

Nm3/Hr.

Sr. No.

Name of By-Product Total


1. Spent Acid* -- 850

* Note- Spent acid will be sent to M/s. Aarti Fertilizers, Vapi which manufactures single super

phosphate as they have applied for Rule-9 Permission.


2006.



Sr. no.

Particulars Details

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

Total: 178.4

Page 40 of 56


Page 40 of 56

Capital cost for EMS (Environmental Management System):.12.4 Crores

B Total Plot area ( sq. meter)

Total:42625 sq. m.


Total:14897 sq. m.


Direct Total: 134

Indirect Total: 50

D Water i


GIDC Jhagadia



Qty KL/day

Recycled Qty. KL/day

Total Qty KL/day

(O) Domestic 50 0 50

(P) Gardening 0 50 50

(Q) Industrial

Process 251 -- 251

Washing 10 -- 10

Softener 1117 -- 1117

Cooling(to be used from softener)

1092* -- 1092*

Others - -- --

Total 1428 50 1478


-

Category Qty KL/Day

Remarks

(K) Domestic 50 Water from domestic will be sent to STP and treated wastewater from STP will be used for Gardening

(L) Industrial

Process 289

Washing 10

Softener Reject 25

Cooling 156

Others --


530

-


Primary, Secondary and Tertiary treatment: 480 KLD


Domestic: STP

Industrial: GIDC Pipeline

vi Reuse/Recycle details (KL/day) 50


E Air

Page 41 of 56


Page 41 of 56


-

SR.

no.

Source of

emission

With

Capacity

e.g. Boiler

(8 TPH)

Stack

Height

(meter)

Name

of the

fuel

Quantity

of Fuel

MT/hr&

MT/Day

APCM

Type of

emissions

i.e. Air

Pollutants

Emission

Standards

1

D.G. Set (Standby) (2 Nos) Capacity= 1500 KVA (Each)

11

Diesel 660

Litre/Hr. --

PM SO2

NOX

150mg/ Nm3 100 ppm 50ppm

-


-

Sr.

no.

Source of

emission

Stack/Vent

Height

(meter)

APCM

Type of

emissions

i.e. Air

Pollutants

Emission

Standards

1

Scrubber connected to Sulphur Dioxide reaction and Sulphuric Acid Plant

30 Alkali Scrubber

SO2 40 Mg/Nm3

2 Scrubber connected to NSA

11 Alkali Scrubber

SO2 40 Mg/Nm3

3

Scrubber connected to DCP

11 Water Scrubber and Alkali Scrubber

NOX VOCs

25 Mg/Nm3 --

4

Scrubber connected to Nitration Reactors

11 Alkali Scrubber

NOX

25 Mg/Nm3


11 Water Scrubber

VOCs --

Page 42 of 56


Page 42 of 56


11 Water Scrubber

VOCs --

7 Reformer 26 Water scrubber

CO 150 Mg/Nm3

-

v Fugitive emission details with its mitigation measures.

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

i

Sr. no.




Quantity

Disposal Method

1 ETP Waste ETP 35.3 400MT/Month Collection, Storage, Transportation, disposal to TSDF.

2 Distillation Residue

Process 36.1 350MT/Month Collection, Storage, transportation, disposal at Co-incineration

3 Gypsum Process 34.3 600MT/Month Collection, Storage, Sold to Cement Industry or sent to TSDF site.

4 Sulphur Sludge Process B2040 7MT/Month Collection, Storage, transportation, disposal at TSDF

5 Discarded containers/bags

Raw Materials

33.1 Whatsoever

generated

Collection, Storage, Decontamination, Disposal by sold to authorize recyclers.

6 Used oil Maintenance 5.1 500Lit/Month Collection, Storage, Transportation, Disposal by selling to registered re-processors.

Page 43 of 56


Page 43 of 56

Technical presentation was made by the project proponent.Committee noted that total water

consumption will be 1428 KL/day and total industrial wastewater generation will be 480 KL/day.

Committee felt that though the product profile and production quantum of proposals for Dahej and

Jhagadia units are different industrial wastewater generation is shown as same, which is not

convincing. Hence, the Committee asked the PP to resubmit both the proposals with realistic and

correct data on water consumption, wastewater generation, etc. Committee asked to give specific

name of the solvents to be used as a raw material. After detailed discussion, Committee decided to

take up the case for scoping only after submission of revised proposal with correct details including the

7 Insulation Waste

Process -- Whatsoever

generated

Collection, Storage, Transportation disposal by at TSDF Site.

8 Spent Carbon ETP and Process

28.3 5 MT/month Collection, Storage, transportation, sent for co-processing

9 Off Specification Product

Process 36.1 Whatsoever

generated




Membership will be given in EIA Report


Non-Hazardous waste will be disposed to GPCB authorized disposers and as per new hazardous and other wastes rules, 2016.

D

i Solvent management (If any) Details of Solvent recovery (As per respective ToR)

Solvent recovery system with double Condenser, cooling followed by chilling will be provided in order to recover 92% to 95% of Solvent.

ii VOC emission sources and its mitigation measures Closed loop systems, double mechanical seal pumps will be provided to reduce VOC as minimum as possible.

Page 44 of 56


Page 44 of 56

following:

1. Status of GIDC pipeline for discharge of treated effluent and permission letter from the concern

authority.

2. Product wise factual details like raw materials, water consumption, waste water generation,

Hazardous waste generation, source its management, manufacturing process with mass

balance etc.

3. Management of spent acid streams as per the Hazardous waste rules 2016.

4. Waste water segregation scheme and its treatment method.

5. Action plan for maximum reuse of treated waste water instead of discharge into GIDC drainage.

6. Proposal CEMS for air emission and waste water discharge.

10. SIA/GJ/IND2/19777/2017 M/s. Palak Chemical Industries C-3, Phase II, GIDC Estate, Naroda, Ahmedabad





dated 24/07017 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.


tabulated below:

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

End-use of product

Existing Proposed Total

1. Tri Ethyl Benzyl Ammonium Chloride

56-37-1 2.0 Nil 2.0

Insecticides

2. Tetra butyl Ammonium Bromide*

1643-19-2 3.0 -3.0 Nil

insecticides

3. Pamoic Acid

130-85-8 Nil 2.0 2.0

Drug intermediate

4. Benzyl Tri Methyl Ammonium chloride

56-93-9 Nil 2.0 2.0

Catalyst Pharma industries

5. Tetra butyl Ammonium Iodide

311-28-4 Nil 2.0 2.0

Perfume chemicals

6. Tetra butyl ammonium Hydroxide in Methanol 40 % Solution

2052-49-5 Nil 2.0 2.0


7. Benzyl tri butyl ammonium chloride

23616-79-0 Nil 2.0 2.0


8. Tetra butyl ammonium chloride 50% solution

1112-67-0 Nil 2.0 2.0

Catalyst Pharma

industries

Page 45 of 56


Page 45 of 56

9. Tetra methyl ammonium hydroxide 25% solution in Methanol

75-59-2 Nil 2.0 2.0

Catalyst Pharma

industries

10. Cetyl di methyl benzyl ammonium chloride

122-18-9 Nil 2.0 2.0 Disinfectant

11. Myristyl di methyl benzyl ammonium chloride

139-08-2 Nil 2.0 2.0 disinfectant

12. Tetra ethyl ammonium tertaFluoro Borate

429-06-1 Nil 2.0 2.0

Electolyte chemical

13. Tetra Ethyl Ammonium Bromide

71-91-0 Nil 2.0 2.0

Catalyst Pharma

industries

14. Methyl Tri butyl ammonium chloride 75 % solution

56375-79-2 Nil 2.0 2.0

Catalyst Pharma

industries

15. Methyl tri Octyl Ammonium chloride (85 % / 90 % / 95 %)

5137-55-3 Nil 2.0 2.0

Catalyst Pharma

industries

16. Cetyl tri methyl ammonium chloride 30 % Solution

112-02-7 Nil 2.0 2.0 Disinfectant

17. Tetra butyl ammonium fluoride trihydrate

87749-50-6 Nil 1.0 1.0

Catalyst Pharma

industries

Total 5.0 26.0 31.0


2006.



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

Existing: Rs. 30 Lac approx Proposed: Rs. 15 Lac approx Total: Rs. 45 Lac approx


Existing: 280.10 sq. m. Proposed:-- Total: 280.10 sq. m.


Existing: 45 sq. m. Proposed: 35 sq. m. Total: 80 sq. m.

-

Sr. no.

Particulars Details

A Water

i

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

GIDC water supply



Page 46 of 56


Page 46 of 56

-

Category Existing KL/day


KL/day


KL/day Remarks

(R) Domestic 0.5 0.5 1.0 --

(S) Gardening - - - --

(T) Industrial

Process 0.0 0.4 0.4 --

Washing 0.0 0.1 0.1 --

Boiler 2.0 1.0 3.0 --

Cooling 1.5 0.5 2.0 --

Others - - - --

Total (A+B+C) 6.5 --

-


-



KL/day


KL/day Remarks

(M) Domestic 0.5 0.5 1.0 --

Industrial

Process 0.0 0.05 0.05 --

Washing 0.0 0.1 0.1 --

Boiler 0.0 0.15 0.15 --

Cooling 0.5 0.0 0.5 --

Others - - - --


0.5 0.3 0.8 --

-


ETP – 2 KLD


Domestic: Soak Pit

Industrial: common Spray Drier

vi Reuse/Recycle details (KL/day) -

B Air (Existing and Proposed)


-

S

R.

no

.

Source

of

emissi

on

With

Capaci

ty e.g.

Boiler

Stack

Heigh

t

(mete

r)

Name of the

fuel

Quanti

ty of

Fuel

MT/hr

&

MT/Da

y

Type of

emissio

ns i.e.

Air

Pollutan

ts

APCM

NAAQS

(National

Ambient

Air

Quality

Standar

ds)

Page 47 of 56


Page 47 of 56

(8 TPH)

1 Boiler 11 m

Firewood/agriculture Briquettes

0.3 MT/Da

y

-

Cyclone

Separat

or +

Bag

Filter

PM 150 mg/Nm3 Sox100

ppm

Nox150

ppm

Natural gas 500

SCM/Day

-

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

Stack/ Vent

Height

(meter)

APCM

NAAQS (National

Ambient Air

Quality Standards)

1 Solvent Extraction System

Gas 8 m Scrubber

PM 150 mg/Nm3 Sox100 ppm

Nox150 ppm

-

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.

Type of waste with


Category and

Schedule as per

HW Rules.

Quantity

Disposal Existing Proposed Total

1.ETP

Sludge

Effluent Treatment

Plant 35.3 --

2.5 MT/month

2.5 MT/mont

h

Collection, Storage, Transportation and disposal to TSDF or CHWIF

2.

Discarde

d Containers/Drums

Manufacturing process

33.1 20

Nos./month

100 Nos./mont

h

120 Nos./mo

nth

Collection storage Decontamination disposal to GPCB Authorized user or

Page 48 of 56


Page 48 of 56


reuse within the premises

3.Spent solvent

Manufacturing process/

Effluent Treatment

Plant

28.6 -- 36 MT/month

36 MT/mont

h

Collection Storage, Transportation, Disposal at co-processing or registered recycler , CHWIF

4.Solvent Residue

Manufacturing process/

Effluent Treatment

Plant

28.1 -- 5 MT/Month

5 MT/Mont

h

Collection Storage, Transportation, Disposal at co-processing or registered recycler , CHWIF

5.Spent carbon

Manufacturi

ng process/

Effluent

Treatment

Plant

28.3 -- 10

MT/month

10 MT/mont

h

Collection Storage, Transportation, Disposal at co-processing or CHWIF

6.

Distillation Residue

Manufacturi

ng process/

Effluent

Treatment

Plant

36.1 -- 10

MT/month

10 MT/mont

h

Collection Storage, Transportation, Disposal at co-processing or CHWIF


CETP – Naroda Enviro Projects Ltd.- Capacity 10KLD


-

D

i Spent Solvent management (If any)

Disposal at co-processing or registered recycler , CHWIF

ii VOC emission sources and its mitigation measures

--

Page 49 of 56


Page 49 of 56

Technical presentation was made by the project proponent. Committee noted that the plot area is only

263 sq.m. and the unit has proposed to increase production quantity from 5 MT/Month to 31 MT/Month

with addition of 15 new products. Committee felt that expansion to the tune of six times with

manufacturing of so many products cannotbe permitted in such a small plot. Hence, PP was asked to

come with a new proposal with reasonable number of products as well as production quantity

considering the very small size of the plot area.

Annexure –I

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

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

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

EMP and the post-project monitoring plan in brief.

3. Justification for selecting the proposed product and unit size.

4. Land requirement for the project including its break up for various purposes, its availability and

optimization.

5. Land possession documents. Copy of NA order showing permission to use the project land for

industrial purpose. If located in GIDC, copy of plot holding certificate obtained from GIDC

Authority.

6. Location of the project site and nearest habitats with distances from the project site to be

demarcated on a toposheet (1: 50000 scale).

7. Topography details of the project area.

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

9. In case of project located outside notified area: Legal Undertaking stating that unit is complying the

three conditions [i.e. water consumption less than 25 M3/day; Fuel consumption less than 25 TPD;

and not covered in the category of MAH units as per the Management, Storage, Import of

Hazardous Chemical Rules (MSIHC Rules), 1989] as per the amendment to EIA Notification, 2006

vide SO 1599 (E) dated 25/06/2014.

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

11. Layout plan of the factory premises clearly demarcating various units within the plant. Provision of

separate entry & exit and adequate margin all round the periphery for unobstructed easy

movement of the emergency vehicle / fire tenders without reversing back. Mark the same in the

plant layout.

12. Technical details of the plant/s along with details on best available technologies (BAT), proposed

technology and reasons for selecting the same.

13. Product spectrum (Proposed products along with production Capacity) and processes.

14. Chemical name of each proposed product to be manufactured. Details on end use of each

product. (Provide CAS number of all the products & raw materials. In case of Dyes, CI number).

15. Details on raw materials, source and storage within the premises.

16. Details of complete manufacturing process / operations of each product along with chemical

Page 50 of 56


Page 50 of 56

reactions, process flow diagram describing each unit processes and unit operations along with

material balance, consumption of raw materials etc.

17. Details on strategy for the implementation of cleaner production activities.

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

requirements for the project. Permission obtained from the concern authority for supply of raw

water.

19. Undertaking stating that no bore well shall be dug within the premises (If project is located within

the Industrial estate).

20. Details on water balance including quantity of effluent generated, recycled & reused. Details of

methods to be adopted for the water conservation.

21. Efforts to minimize effluent discharge and to maintain quality of receiving water body.

22. Explore the possibilities for Zero Liquid Discharge (ZLD) option for the proposed project.

23. Segregation of waste streams, characterization and quality with specific treatment and disposal of

each stream including action plan for maximum recycle of treated waste water and minimum

discharge for effluent.

24. Capacity of ETP in KL/day. Details of ETP including dimensions of each unit along with schematic

flow diagram. Inlet, transitional and treated effluent qualities with specific efficiency of each

treatment unit in reduction in respect of all concerned/regulated environmental parameters. Inlet

effluent quality should be based on worst case scenario considering production of most polluting

products that can be manufactured in the plant concurrently.

25. In case of discharge into GIDC drainage / Pipeline:

I. 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.

II. Characteristics of the combined effluent and treated water to be sent to Common pipeline

with reference to the MoEFCC/CPCB/GPCB discharge norms.

III. Provision for Continuous Monitoring System for waste water discharge.

26. In case of waste water sent to Common Facilities (CF) like CETP, MEE, Spray Dryer etc.

a. Details of Common facilities including (1) Total capacity of the CF (2) Copy of CC&A of the

CF. (3) Actual load at present (Qualitative and Quantitative – KL per day) (4) Booked

quantity & Spare capacity of CF (5) 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. (6)

Copies of Show- cause notices, closure notices etc. served by the GPCB and its

compliance (6) Recommendations and suggestions of the last two Environment Audit

reports of CETP and its compliance report. (7) Common Facility Up gradation scheme, if

any.

b. Status of compliance to the 18(1) (b) direction issued by the CPCB with respect to CETP

compliance & CEPI area action plan along with relevant supportive document.

c. Give status of compliance of Environmental norms of existing Common Infrastructure i.e.

CETP, MEE & Spray Dryer (Whichever is applicable) in which you are a member.

d. Submit adequacy of Common Infrastructure i.e. CETP, MEE & Spray Dryer for additional

Page 51 of 56


Page 51 of 56

load (Whichever is applicable) along with written confirmation/membership certificate

mentioning the same (Total consented quantity, total quantity booked so far, quantity

booked for the unit, spare quantity available).

27. In case of Zero Liquid Discharge (ZLD) :

I. Action plan for ‘Zero’ discharge of effluent shall be included. Notarized undertaking for

assuring that underground drainage connection will not be taken in the unit and there

shall be no effluent discharge outside the plant premises.

II. Economical and technical viability of the effluent treatment system to achieve Zero

Liquid Discharge (ZLD).

III. Certification of adequacy of proposed ZLD scheme through credible institutes of

National repute.

IV. To estimate & monitor ground water quality & its contamination status, piezometer wells,

one on up gradient of the groundwater flow and other three on the down gradient side of

the ground water flow of the proposed project at different depth based on available

ground water depth shall be established and all the parameters mentioned in IS 10:500

for potable water standard shall be monitored.

28. In case of in-house MEE/Spray dryer for waste water treatment: Capacity of MEE/Spray dryer in

KL/hr. Technical details of MEE including evaporation capacity, steam required for evaporation,

adequacy of the proposed boiler to supply steam for evaporation in addition to the steam required

for the process etc. Techno-economical viability of the evaporation system. Control measures

proposed for the evaporation system in order to avoid/reduce gaseous emission/VOC from

evaporation of industrial effluent containing solvents & other chemicals.

29. Technical details of ATFD/Crystallizer/ spray Dryer, RO/NF system etc. (If any).

30. Undertaking stating that a separate electric meter will be provided for the waste water treatment

system viz. ETP, RO, MEE, Spray dryer etc. (Whichever is applicable)

31. Economical and technical viability of the effluent treatment system.

32. Plans formanagement, collection and disposal of waste streams tobe generated from spillage,

leakages, vessel washing, used container washing etc. Measures proposed for preventing effluent

discharge during unforeseen circumstances.

33. Action plan for reuse of liquid waste streams like Spent acids, Poly Aluminium Chloride etc. within

premises to convert into valuable products instead of sending outside to actual end-users.

34. Adequacy of the proposed EMS with respect to the pollution load envisaged in terms of Air, Water

and hazardous waste.

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

wind speed and directionand rainfall should be incorporated.

36. 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 for all

the concerned/identified VECs and likely impacts will have to be assessed for their magnitude in

order to identify mitigation measures.

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

Page 52 of 56


Page 52 of 56

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

revised National Ambient Air Quality Standards (NAAQS) as well as project specific parameters

like NH3, HCl, CL2, HBr, VOC etc. Locations of the monitoring stations should be so decided so

as to take into consideration the pre-dominant downwind direction, population zone and sensitive

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

be at least one monitoring station in the pre dominant downwind direction at a location where

maximum ground level concentration is likely to occur.

38. 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.

39. Base linestatus of the noise environment, impact of noise on present environment dueto the

project and proposed measures for noise reduction including engineering controls.

40. Specific details of

a) Process gas emission from each unit process with its quantification.

b) Air pollution Control Measures (APCM) proposed for process gas emission. Adequacy of

the air pollution control measures (APCM) for process gas emission measures to

achieve the GPCB norms.

c) Details of the utilities required.

d) Type and quantity (MT/hr& MT/Day) of fuel to be used for each utility.

e) Flue gas emission rate emission from each utility.

f) Air Pollution Control Measures (APCM) proposed to each of the utility along with its

adequacy

g) List the project specific sources of fugitive emission along with its quantification and

proposed measures to control it.

h) Details on tail gas treatment.(If any)

41. Provision of CEMS (Continuous Emission Monitoring system).

42. Action plan for odour control to be submitted.

43. Management plan for hazardous/Solid waste including storage, handling, utilization and safe

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

Rules 2016. CPCB guidelines in respect of specific treatment, such as solar evaporation,

incineration, etc., need to be followed.

44. How the manual handling of the hazardous wastes will be minimized? Methodology of de-

contamination and disposal of discarded containers and its record keeping.

45. Management of by-products which fall under the purview of the Hazardous and Other Wastes

(Management and Transboundary Movement) Rules 2016 as per the said rules and necessary

permissions from the concern authority.

46. Membership of Common Environmental Infrastructure like TSDF, Common Incineration Facility

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(CHWIF), MEE, Spray dryer etc.

47. Name and quantity of each type of solvents to be used for proposed production. Details of in-

house solvent recovery system including mass balance, solvent loss, recovery efficiency (%

recovery), feasibility of reusing the recovered solvents etc. for each type of solvent.

48. Appropriate monitoring network has to be designed and proposed, to assess the possible residual

impacts on VECs.

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

environment as well as detailed monitoring plan and environmental management cell proposed for

implementation and monitoring of EMP. The EMP should also include the concept of waste-

minimization, recycle/reuse/recover techniques, energy conservation, and natural resource

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

control measures.

50. Details of in-house monitoring capabilities and the recognized agencies if proposed for conducting

monitoring.

51. Permission from PESO, Nagpur for storage of solvents, other toxic chemicals, if any.

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

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

industrial hygienist and monitoring of the occupational injury to workers as well as impact on the

workers. Plan for periodic medical checkup of the workers exposed. Details of work place ambient

air quality monitoring plan as per Gujarat Factories Rules.

53. Details on volatile organic compounds (VOCs) from the plant operations and occupational safety

and health protection measures. Proposal for Leak Detection and Repair (LDAR) program as per

the CPCB guidelines.

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

scenarios should be carried out. The worst-case scenario should take into account the maximum

inventory of storage at site at any point of time. The risk contours should be plotted on the plant

layout map clearly showing which of the facilities 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.

55. MSDS of all the products and raw materials.

56. Details of hazardous characteristics and toxicity of raw materials and products to be handled and

the control measures proposed to ensuresafety and avoid the human health impacts. This shall

include the details of Antidotes also.

57. Details of quantity of each hazardous chemical (including solvents) tobe stored, Material of

Construction (MoC) of major hazardous chemical storage tanks, dyke details, threshold storage

quantity asper schedules of the Manufacture, Storage &Import of Hazardous Chemicals Rules of

major hazardous chemicals, size of the biggest storage tank to be provided for each raw material

& product etc. How the manual handling of the hazardous chemicals will be minimized?

58. Details of the separate isolated storage area for flammable chemicals. Details of flame proof

electrical fittings, DCP extinguishers and other safety measures proposed. Detailed fire

controlplanfor flammable substances and processes showing hydrant pipeline network, provision

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of DG Sets, fire pumps, jockey pump, toxic gas detectors etc.

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

manufacturing utility staff for safety related measures.

60. Specify safety precautions to be taken for Chemical storage, process, handling& transportation

hazard.

61. Details on workers training before engaging work, periodical, in-house, outside etc.

62. Details on various SOP to be prepared.

63. Details on safety audit to be carried out and their compliance status.

64. Specific safety measures to be taken for general Public living in the vicinity.

65. Details on hazard identification i.e. HAZOP, HAZAN, Fault tree analysis, Event tree analysis,

Checklist, Audit etc. to be adopted for the safety operation of the plant.

66. Detection and monitoring of VOC’s / gases.

67. Detailed five year greenbelt development program including annual budget, planning schedule,

species, width of plantations, number of trees to be planted, area under green belt development

[with map], budgetary outlay etc. 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.

68. Action plan for the greenbelt development – species, width of plantations, planning schedule, etc.,

in accordance to CPCB published guidelines.

69. Detailed socio-economic development measures 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.

70. (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.

71. 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.

72. 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.

73. Phase wise projectimplementationschedule with bar chart and time frame, in terms ofsite

development, infrastructure provision, EMS implementation etc.

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

incorporated in the EIA Report.

75. An undertaking by the Project Proponent on the ownership of the EIA report as per the MoEF&CC

OM dated 05/10/2011 and an undertaking by the Consultant regarding the prescribed TORs have

been complied with and the data submitted is factually correct as per the MoEF&CC OM dated

04/08/2009.

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

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77. Where data are presented in the Report especially in Tables, the period in which the data were

collected and the sources should be indicated.

78. Project Proponent shall enclose all the analysis/testing reports of water, air, soil, noise etc. using

the MoEF&CC/NABL accredited laboratories. All the original analysis/testing reports should be

available during appraisal of the Project.

79. In case of Expansion of the project

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

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

c. Explore the possibility to achieve Zero Liquid Discharge (ZLD) for existing as well as

proposed activity.

d. 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.

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

compliance report.

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

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

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

all the conditions stipulated therein.

h. Compliance of MoEFCC circulars vide No: J-11011/618/2010-IAII (I) dated 30/05/2012 and

J-11013/41/2006-IA-II(I) dated 20/10/2009.

i. 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.

80. In case of project is located in Ankleshwar-Panoli, Vatva-Narol&Vapi GIDC.

(A) Compliance of MOEFCC’s OM no. J-11013/5/2010-IA.II (I) dated 25/11/2016 regarding

lifting of moratorium on the consideration of projects for environmental clearance.

(B) Compliance of direction under section 18 (1) (b) of the Water (Prevention and Control of

Pollution) act, 1974 issued by CPCB dated 31/03/2016 regarding compliance of CETP.

a) Action initiated by GPCB, if any, against proposed unit regarding non-compliance of

prescribed standards under the various environmental laws.

b) Performance of CETP with respect to current hydraulic load & prescribed standards with

No Objection Certificate of CETP regarding incorporation of the proposed unit for

acceptance of waste water.

c) Performance of TSDF site with respect to current load & prescribed standards with No

Objection Certificate of TSDF site regarding incorporation of the proposed unit for

acceptance of hazardous waste to the common infrastructure.

d) Copies of quarterly action report taken for the above points submitted to the CPCB.

e) Report of GPCB which have conducted monitoring as per the said direction by CPCB

dated 31/03/2016.

Validity of ToR:

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

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

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

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

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

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recommendation of the SEAC.

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. Shri Natrajan Pratap, Member, SEAC

6. Shri A. K. Mule, Member, SEAC.

7. Shri K. C. Mistry, Secretary, SEAC

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