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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
Screening and Scoping
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
Screening and Scoping
Category of the unit : 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/19513/2017
dated 19/07/2017 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. 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.
• PP was called for presentation in the SEAC meeting dated 24/08/2017.
• Salient features of the project are as under:
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
Total after Expansion
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.
• The TOR prescribed as above and as per Annexure – I and the model ToRs available in the
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
http://environmentclearance.nic.in/along with final EIA report.
4. SIA/GJ/IND2/19276/2017 M/s. Ester India Plot No. 128/29-30, GIDC-Nandesari, Dist.: Vadodara.
Screening and Scoping
Category of the unit : 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/19276/2017
dated 20/07/2017 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.
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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• The project falls underCategory 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:
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
Source of Water Supply (GIDC, Bore well, Surface water etc...)
GIDC Nandesari
Status of permission from the concern authority. Confirmed Permission
ii Water consumption (KL/day)
-
Existing KL/day
Proposed (Additional) 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
-
iii Waste water generation (KL/day)
-
Category Existing KL/Day
Proposed (Additional) KL/day
Total after Expansion KL/day
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.
v Mode of Disposal & Final meeting point
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
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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
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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
aspect, raw material & product storage considering worst case scenario.
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 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.
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5 SIA/GJ/IND2/19240/2017 M/s: Kangaroo Industries Plot No. D-2/CH/79, GIDC, Dahej-2 Industrial Estate, Dahej, Dist. Bharuch
Screening and Scoping
Category of the unit : 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/19240/2017
dated 19/07/2017 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
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
• The project falls underCategory 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:
Total cost of Proposed Project (Rs. in Crores):
Project Cost: Rs. 600 Lakh &
EMS: Rs. 50 Lakh (Approximately)
Total Plot area ( sq. meter)
7430.90 Sq. m.
Green belt area,/Tree Plantation area ( sq. meter)
1486.18 Sq. m.
-
Sr. no.
Particulars Details
A Water
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i. Source of Water Supply (GIDC, Bore well, Surface water etc...)
GIDC Water Supply System
Status of permission from the concern authority.
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
Category Existing 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
Total Industrial waste water
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
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Industrial: ETP& then CETP
vi. Reuse/Recycle details (KL/day) -
B 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
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
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C 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
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
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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. 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 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 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
http://environmentclearance.nic.in/along with final EIA report.
6 SIA/GJ/IND2/19767/2017 M/s: GREEVA Plot no. C 1 5513 5514, Phase III, Vatva- GIDC, Ahmedabad.
Screening and Scoping
Category of the unit : 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/19767/2017
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dated 21/07/2017 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.
• 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.
• 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):
Existing: 1.5 Proposed: 3.10 Total: 4.6
B Total Plot area ( sq. meter)
Existing: 1737 m2
Proposed: 314 m2 Total: 2051 m2
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Green belt area,/Tree Plantation area ( sq. meter)
Existing: 225 m2 Proposed: 84 m2 Total: 309 m2
C Employment generation
Direct Existing: 21 Proposed:20 Total:41
Indirect Existing: Proposed: Total:
D Water i
Source of Water Supply (GIDC, Bore well, Surface water etc...)
Water is sourced from GIDC water supply i.e. Vatva Industrial Estate Infrastructure Development Limited (SPV) of Vatva Industries Association.
Status of permission from the concern authority: Permission of Vatva Industrial Estate Infrastructure Development Limited (SPV) OF Vatva Industrial Association is given.
ii
Water consumption (KL/day)
Existing KL/day
Proposed (Additional) KL/day
Total after Expansion 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)
Category Existing KL/Day
Proposed (Additional) KL/day
Total after Expansion 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 - - -
Total Industrial waste water
22.5 0 22.5
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iv Treatment facility with capacity (ETP, CETP, MEE, STP etc).
The industrial effluent is treated in ETP of capacity 75 KLD & treated water is going to CETP for further treatment.
v Mode of Disposal & Final meeting point
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]
-
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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
Source of generation
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
Quantity of discarded containers must be in MT/Annum.
ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.
CETP:Membership Certificate of M/s. The Green Environment Services Co-op. Society Ltd. For Effluent Treatment
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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.
1. Adequacy of proposed area with respect to plant machineries, EMS, green belt, safety
aspect, raw material & product storage considering worst case scenario.
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.
• The TOR prescribed as above and as per Annexure – I 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.
7. SIA/GJ/IND2/19872/2017 M/s. Krishna Enterprise Plot No. 7612, GIDC Estate, near Karmatur Chokdi, Ankleshwar, Dist- Bharuch.
Screening and Scoping
Category of the unit : 5(f)
Project status: New
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• This office has received an application vide their online proposal no. SIA/GJ/IND2/19872/2017
dated 19/07/2017 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
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
• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification
2006.
• PP was called for presentation in the SEAC meeting dated 24/08/2017.
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• Salient features of the project are as under:
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
Source of Water Supply (GIDC, Bore well, Surface water etc...)
GIDC
Status of permission from the concern authority.
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)
-
Category Existing KL/Day
Remarks
(G) Domestic 4
(H) Industrial
Process 16
Washing 3 For reactor washing
Boiler 1
Cooling
Others 0
Total Industrial waste water
20
-
iv Treatment facility with capacity (ETP, CETP, MEE, STP etc).
ETP: 16 KLD CETP: 4 KLD
v Mode of Disposal & Final meeting point
Domestic: Soak Pit
Industrial: 4 KLD concentrated effluent to the
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Common MEE and 16 KLD will be treated in ETP and reused within unit.
vi Reuse/Recycle details (KL/day) 16 KLD
B 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
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.
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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.
Type/Name of Hazardous waste
Source of generation
Category and Schedule as per HW Rules.
Quantity (MT/Annum)
Disposal Method
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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.
Quantity of all the wastes including discarded containers must be in MT/Annum.
ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.
Attached as Annexure-1.
ii Details of Non-Hazardous waste & its disposal (MSW and others)
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.
1. Adequacy of proposed area with respect to plant machineries, EMS, green belt, safety
aspect, raw material & product storage considering worst case scenario.
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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.
• 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.
8 SIA/GJ/IND2/19877/2017 M/s: Aarti Industries Limited(Unit-II) Plot No. Z/103/D, GIDC Estate, SEZ-II Dahej, Bharuch
Screening and Scoping
Category of the unit : 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/19877/2017
dated 20/07/2017 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 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.
• 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):
Total: 178.4
• Capital cost for EMS (Environmental Management System):.12.4 Crores
B Total Plot area Total: 57970 sq. m.
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( sq. meter)
Green belt area,/Tree Plantation area ( sq. meter)
Total: 17391 sq. m.
C Employment generation
• Direct Total: 134
• Indirect Total: 50
D Water i
Source of Water Supply (GIDC, Bore well, Surface water etc...)
Dahej SEZ
Status of permission from the concern authority.
ii Water consumption (KL/day)
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)
iii Waste water generation (KL/day)
-
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 --
Total Industrial waste water
530
-
iv Treatment facility with capacity (ETP, CETP, MEE, STP etc).
Primary, Secondary and tertiary treatment Plant: 480 KLD
v Mode of Disposal & Final meeting point
Domestic: STP
Industrial: GIDC Pipeline
vi Reuse/Recycle details (KL/day) 50 KLD
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vii Details of rainwater harvesting Rain water harvesting will be carried out through roof tops.
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
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
-
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 --
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5 Scrubber connected to tanks
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.
Type/Name of Hazardous waste
Source of generation
Category and Schedule as per HW Rules.
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.
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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
Collection, Storage, transportation, disposal at CHWIF
ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.
Membership will be given 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 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.
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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
Screening and Scoping
Category of the unit : 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/19878/2017
dated 19/07/2017 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 Product CAS No. Total
quantity in MT/Month
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
quantity in MT/Month
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.
• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification
2006.
• PP was called for presentation in the SEAC meeting dated 24/08/2017.
• Salient features of the project are as under:
Sr. no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores):
Total: 178.4
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Capital cost for EMS (Environmental Management System):.12.4 Crores
B Total Plot area ( sq. meter)
Total:42625 sq. m.
Green belt area,/Tree Plantation area ( sq. meter)
Total:14897 sq. m.
C Employment generation
Direct Total: 134
Indirect Total: 50
D Water i
Source of Water Supply (GIDC, Bore well, Surface water etc...)
GIDC Jhagadia
Status of permission from the concern authority.
ii Water consumption (KL/day)
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
iii Waste water generation (KL/day)
-
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 --
Total Industrial waste water
530
-
iv Treatment facility with capacity (ETP, CETP, MEE, STP etc).
Primary, Secondary and Tertiary treatment: 480 KLD
v Mode of Disposal & Final meeting point
Domestic: STP
Industrial: GIDC Pipeline
vi Reuse/Recycle details (KL/day) 50
vii Details of rainwater harvesting Rain water harvesting will be carried out through roof tops.
E Air
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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
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
-
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
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
5 Scrubber connected to tanks
11 Water Scrubber
VOCs --
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6 Scrubber connected to tanks
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.
Type/Name of Hazardous waste
Source of generation
Category and Schedule as per HW Rules.
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.
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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
Collection, Storage, transportation, disposal at CHWIF
Quantity of all the wastes including discarded containers must be in MT/Annum.
ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.
Membership will be given 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 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.
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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
Screening and Scoping
Category of the unit : 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/19777/2017
dated 24/07017 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. 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
Catalyst Pharma industries
7. Benzyl tri butyl ammonium chloride
23616-79-0 Nil 2.0 2.0
Catalyst Pharma industries
8. Tetra butyl ammonium chloride 50% solution
1112-67-0 Nil 2.0 2.0
Catalyst Pharma
industries
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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
• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification
2006.
• PP was called for presentation in the SEAC meeting dated 24/08/2017.
• Salient features of the project are as under:
Total cost of Proposed Project (Rs. in Crores):
Existing: Rs. 30 Lac approx Proposed: Rs. 15 Lac approx Total: Rs. 45 Lac approx
Total Plot area ( sq. meter)
Existing: 280.10 sq. m. Proposed:-- Total: 280.10 sq. m.
Green belt area,/Tree Plantation area ( sq. meter)
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
Status of permission from the concern authority.
ii Water consumption (KL/day)
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-
Category Existing KL/day
Proposed (Additional)
KL/day
Total after Expansion
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 --
-
iii Waste water generation (KL/day)
-
Category Existing KL/Day
Proposed (Additional)
KL/day
Total after Expansion
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 - - - --
Total Industrial waste water
0.5 0.3 0.8 --
-
iv Treatment facility with capacity (ETP, CETP, MEE, STP etc).
ETP – 2 KLD
v Mode of Disposal & Final meeting point
Domestic: Soak Pit
Industrial: common Spray Drier
vi Reuse/Recycle details (KL/day) -
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.
-
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)
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(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
Source of generation
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
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Quantity of discarded containers must be in MT/Annum.
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
ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.
CETP – Naroda Enviro Projects Ltd.- Capacity 10KLD
ii Details of Non-Hazardous waste & its disposal (MSW and others)
-
D
i Spent Solvent management (If any)
Disposal at co-processing or registered recycler , CHWIF
ii VOC emission sources and its mitigation measures
--
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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
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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
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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
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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