Post on 19-May-2020
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438thmeeting of SEAC-Gujarat, Dated 03.10.2018
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Minutes of the 438th meeting of the State Level Expert Appraisal Committee held on 03/10/2018
at Committee Room, GEER Foundation, Gandhinagar.
The 438h meeting of the State Level Expert Appraisal Committee (SEAC) was held on 03rd October
2018 at Committee Room, GEER foundation, Gandhinagar. Following members attended the
meeting:
1. Dr. Dinesh Misra, Chairman, SEAC
2. Shri S. C. Srivastav, Vice Chairman, SEAC
3. Dr. V. K. Jain, Member, SEAC
4. Shri R. J. Shah, Member, SEAC
5. Shri Rajesh I Shah, Member, SEAC
6. Shri A. K. Muley, Member, SEAC
The agenda of TOR/Scoping cases and Appraisal was taken up. The applicants made presentations on
the activities to be carried out along with other details furnished in the Form-1, PFR, EIA-EMP reports
and other reports.
7. SIA/GJ/IND2/20649/2017 M/s. Meghmani LLP [Earlier named as M/s. Meghmani Unichem LLP] Plot No. CH-3, GIDC Industrial Estate, Dahej, Taluka-Vagra, District-Bharuch.
Appraisal
Project / Activity No.: 5(f)
Project status: Expansion
• PP has submitted online application vide no. SIA/GJ/IND2/20649/2017 dated 14/11/2017 for
obtaining Environmental Clearance.
• SEAC has recommended the project to SEIAA and SEIAA has issued TOR to PP vide letter
SEIAA/GUJ/TOR/5(f)/158/2018 dated 28/02/2018.
• Project proponent has submitted EIA Report prepared by M/s. Anand Environmental Consultants Pvt.
Ltd. based on the TOR issued by SEIAA.
• This is an existing unit engaged in Synthetic Organic Chemicals and now proposes for expansion as
tabulated below:
Sr. No.
Name of Product CAS no. Quantity (MT/Month) End-use of product
Existing Proposed Total
1. Para Amino Phenol 123-30-8 300 900 1200 For Mfg. Paracetamol
2. Paracetamol 103-90-2 1250 0 1250 For Mfg. Antipyretic Drug
By-Product
Dil. Acetic Acid (from Paracetamol)
64-19-7 1750 0 1750 In Textile &Glacial Acetic Acid
• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.
• PP was called for presentation in the SEAC meeting dated 03/10/2018.
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• Salient features of the project are as under:
Sr. no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores):
Existing: 600 Lacs Proposed:45 Crores Total: 51 Crores
B Total Plot area ( sq. meter)
Existing: 10000 sq. m Proposed: Nil Total: 10000 sq. m
Green belt area,/Tree Plantation area ( sq. meter)
Existing: Proposed: Total:5924 m2
C Employment generation Existing: Proposed: Total:
Direct 120 40
160
Indirect 70 40
110
D Water
i
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC
Status of permission from the concern authority. Yes
ii
Water consumption (KLD)
Existing KLD
Proposed * (Additional)
KLD
Total after* Expansion
KLD
(A) Domestic 15 0 15
(B) Gardening 5 1 6
(C) Industrial
Process 85 135 220
Washing 20 20 40*
Boiler 44 -- 44
Cooling 20 80 100
Others -- -- --
Industrial Total 169 235 404
Grand Total (A+B+C)
189 236 425
* This is 1st day fresh water requirement, from second day onwards 40 m3/day recycled water will be reused. Therefore from the second day onwards fresh water requirement will be 385 m3 /day (425 – 40).
1) Total water requirement for the project: 425KLD 2) Quantity to be recycle: 40KLD 3) Total fresh water requirement: 385 KLD
iii
Waste water generation (KLD)
Category Existing KLD
Proposed (Additional) KLD
Total after Expansion KLD
(A) Domestic 13 0 13
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(B) Industrial
Process 58 174 232
Washing 20 20 40
Boiler 10 -- 10
Cooling 20 80 100
Others
Total Industrial waste water
108 274 382
Grand Total (A+B) 121 271 395
-
iv Treatment facility within premises with capacity [For existing and Proposed] [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
• Effluent generated from industry and domestic will be treated in our existing effluent treatment plant (capacity-125 m3/day) and proposed effluent treatment plant (capacity-400 m3/day). Treated effluent will be reused in miscellaneous washing (40 m3/day) and remaining will be discharge into underground GIDC -drainage line and ultimately disposal into deep sea.
v Mode of Disposal & Final meeting point
Domestic: GIDC -drainage line ultimately disposal into deep sea.
Industrial: GIDC -drainage line ultimately disposal into deep sea.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility
Not applicable, since our Effluent generated from industry and domestic will be treated in our existing effluent treatment plant (capacity-125 m3/day) and proposed effluent treatment plant (capacity-400 m3/day).
Membership of Common facility (CF)
Not applicable, since our Effluent generated from industry and domestic will be treated in our existing effluent treatment plant (capacity-125 m3/day) and proposed effluent treatment plant (capacity-400 m3/day).
vii Reuse/Recycle details (KLD)
Treated effluent will be reused in miscellaneous washing (40 m3/day) and remaining will be discharge into underground GIDC -drainage line and ultimately
E Air
i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. Existing & Proposed
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Name of the fuel
Quantity of Fuel MT/hr & MT/Day
Type of emissions
i.e. Air Pollutants
Air Pollution Control Measures
(APCM)
Existing
1. Steam boiler (3 ton/hr)
30 Coal
15 MT/day
SPM
SO2 NOx
Multi-cyclone & bag filter
2. Thermic fluid heater
15 LDO
50 LPH SPM
SO2 NOx
Adequate stack height
3. D.G. set * (400 KVA)
15 LDO
15 LPH SPM
SO2 Adequate stack height
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NOx
Proposed
4. Steam boiler (5 ton/hr)
30 Natural Gas
300 SCM/hr
SPM
SO2 NOx
Adequate stack height
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) Existing & Proposed
-
Sr. no.
Source of emission
Type of emission
Stack/Vent Height (meter)
Air Pollution Control Measures
(APCM)
1 Not Applicable It may be noted that our manufacturing process is such that there is no process gas emission.
-
iii Fugitive emission details with its mitigation measures.
All possible preventive measure taken to control / minimize the Fugitive emissions
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)
Mode of Disposal**
Existing Proposed Total
1. ETP Sludge
ETP 35.3 2880 MT
6540 MT
9420 MT
Will be collected, stored, transported & disposed at authorized TSDF site.
2. Spent Catalyst
Manufacturing process
28.2 0.3 MT
0.222 MT
0.522 MT
Will be sent back for regeneration/ reactivation
3. Used Drums
Manufacturing process
33.1 0.54 MT
0.96 MT
1.5 MT
Will be collected, stored and reused /sold to authorized recycler Liners /
PPBags 0.84 MT 1.16 MT 2.0
MT
4. Used Spent Oil
Manufacturing process
5.1 0.30 MT
0.90 MT
1.2 MT
Will be collected, stored and sold to authorized recycler.
5. Dil. Acetic Acid
Manufacturing process
-- 21000 MT
0
21000 MT
Collection, storage and sell to registered recycler/end user.
6. Waste resin from wastewater treatment
Wastewater treatment
35.2 0 12 MT
12 MT
Will be collected, stored, transported & disposed at authorized Common Haz. Waste Management Facility (CHWMF)
-
ii Membership details of TSDF, CHWIF etc. We have obtained membership of BEIL-Dahej for TSDF
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iii Details of Non-Hazardous waste & its disposal(MSW and others)
Not applicable
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
• Not applicable
ii VOC emission sources and its mitigation measures
• Not applicable
• During the meeting dated 03/10/2018, technical presentation made by project proponent.
• At present unit is engaged in manufacturing of organic products for which they have obtained EC
from SEIAA & CC&A of the Board. The proposal is for expansion by addition of new Synthetic
Organic Chemicals.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for expansion of existing unit and for now proposes a new synthetic organic chemical
product. This unit is having valid EC & CC&A for existing unit. Copy of EC, CC&A, CC&A compliance
report is submitted. The compliance of EC is submitted by RO and it was discussed in detail and
found satisfactory. PP ensured that there are no court cases pending and no public complaints
against the project.
• Total water consumption will be 425 KLD. Total wastewater generation will be 382 KLD. After
proposed expansion, ETP proposed of 400 KLD capacity in addition to existing 125 KLD capacity &
after full-fledged treatment, 40 KLD treated effluent shall be reused back in washing purpose and rest
of treated effluent shall be discharged into underground drainage of GIDC which ultimately meets to
Deep sea. Domestic effluent will be 13 KLD and shall be treated in proposed ETP along with
industrial effluent.
• Coal or Natural gas will be used as fuel for proposed boiler.
• Adequate APCM will be provided for proposed flue gas emission.
• Hazardous waste management will be as per the HW Rules.
• The baseline environmental quality has been assessed for various components of the environment
viz. air, noise, water, biological and socioeconomic aspect. The baseline environmental study has
been conducted for the study area of 10 km radial distance from project site for the period October
2017 to December 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2,
NOx, HCl, Cl2, HBr, NH3, CO and VOC at eight locations, including the project site. Values conform
to the prescribed standards for Ambient Air Quality. The incremental Ground Level Concentration
(GLC) has been computed using AIRMOD. The resultant concentrations are within the NAAQS. The
modelling study proved that the air emissions from the proposed plant would not affect the ambient
air quality of the region in any significant manner. The ambient air quality around the proposed
project site will remain within the National Ambient Air Quality Standards (NAAQS).
• Risk assessment including prediction of the worst-case scenario and maximum credible accident
scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site
Emergency Plan has been covered in the RA report.
Discussions & Conclusion:
• Committee deliberated that PP has changed the name from M/s. Meghmani Unichem LLP to M/s.
Meghmani LLP, hence PP was asked to submit all statutory documents in this regard.
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• Committee deliberated on Compliance of existing project (CCR), automization of the manufacturing
plant, Hazardous chemicals like Cl2, Toluene & other hazardous chemicals, APCM for process gas
emission, SOP for safety precautions, Baseline, CER, HW management etc.
• PP informed that they will follow the PESO standards for unloading, storage, transportation, handling
and processing of PNCB. PP have to provide CEMS for process gas emission.
• Committee deliberated on management of acetic acid and also focused on permission of Narcotics
department for selling of dilute acetic acid.
• It is noted that capacity of boiler is increasing whereas proposed water consumption under the boiler
is shown nil. Further proposed production is increasing to 900 MTPM from 300 MTPM and water
requirement, waste water generation is not accordingly addressed.
• Referring to the baseline study for ambient air, it is noted that wind rose diagram, isopleths of gases
and particulate matter are not in consonance; hence it was decided to ask PP to readdress the same.
After detailed discussion, it was decided to ask project proponent to submit the following details and
upon receipt of the same, it was decided to consider the proposal in one of the upcoming SEAC
meeting.
1. To re-address water consumption and waste water generation considering three time expansion of
product Para Amino Phenol.
2. To re-address wind rose diagram, GLC during the study period and its associated isopleths with
coverage of area in upwind and downwind with conclusion and submit addendum in EIA report of the
same.
3. To submit all statutory documents pertaining to the change of name from M/s. Meghmani Unichem
LLP to M/s. Meghmani LLP.
8. SIA/GJ/IND2/18468/2017 M/s. Krishna Antioxidants Pvt. Ltd. Plot No. D-3/24/1, GIDC, Dahej, Village Samatpor, Taluka Vagra, Dist. Bharuch. 392130
Appraisal
Project / Activity No.: 5(f)
Project status: Expansion
• PP has submitted online application vide no. SIA/GJ/IND2/18468/2017 dated 14/02/2017 for
obtaining Environmental Clearance.
• SEAC has recommended the project to SEIAA and SEIAA has issued TOR to PP vide letter
SEIAA/GUJ/TOR/5(f)/493/2017 vide dated 30/04/2017 and ToR Amendment No.
SEIAA/GUJ/TOR/5(f)/339/2018 vide dated 28/03/2018.
• Project proponent has submitted EIA Report prepared by M/s. Kadam Environmental Consultants
based on the TOR issued by SEIAA.
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• This is an existing unit and now proposes for expansion for synthetic organic chemicals as tabulated
below:
Table 1: Details for EC Products
Sr.
No. Name of the Products
CAS no. /CI
no.
Quantity
MT/Annum End-use of products
1 Oil Soluble Demulsifier - 2400 Refinery Industry
2 Polymeric/Polyester/Polyurethane
based Polyol - 9600 Polyurethane industries
3 Octylated Butylated Diphenylamine
36878-20-3
/ 68411-46-
1
2000 Antioxidants for Lubricant
Industries
4 Amine Ethoxylate
(MDEA/MEA/DEA/TEA) - 5000
Intermediate for H2S
scavenger
5 Crude Raw (Fatty Acid) Oil Fractions - 6000 Mud Emulsifier
6 Polyol Intermediate Products such as; - 6000
a N Polyethylene Glycol -
Intermediate for Drilling
Chemicals
b Oxo Alcohol & Its Higher Derivative
Ethoxylate -
Additive for Drilling
Chemicals
c Oxo Alcohol & Its Higher Derivative
Condensate -
Additive for drilling
Chemicals
d Nonyl Phenol Ethoxylate/Condensate
127087-87-
0
Textile, Detergent & Soap
Industries
e Glycerine Propoxylate - Intermediate for Drilling
Chemicals
f Iso Propyl Alcohol Ethoxylate - Intermediate for Drilling
Chemicals
7 Drilling Additive Intermediate Products
such as; - 3000
a Primary & Secondary Surfactant for
Drilling - Mud Chemicals
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8 Surfactants & Other EO/PO
Condensate such as; - 3000
a Fatty / Lauryl Alcohol Ethoxylate 24938-91-8
Surfactants for cosmetics,
Detergent industries
b Phenoxy Ethanol 122‐99‐6 Additives for Paints & Inks
c Castor Oil Ethoxylate 61791-12-6 Additive for Personal Care
d Hydrogenated Castor Oil Ethoxylate 61788-85-0 Additive for Oil & Wax
Industries
e Tallow Amine Ethoxylate - Textile Industries
f Styrenated Phenol Ethoxylate - Additive for Industrial
Chemicals
g Phenolic Derivative Ethoxylate - Additive for Industrial
Chemicals
h Synthetic Alcohol Ethoxylate - Surfactants for Textile, Soap
& Detergent Industries
i Styrenated Phenol 61788-44-1 Antioxidants for Rubber
j Soybean Oil/Base oil Ethoxylate - Surfactants for Textile
Industries
Total 37000
Table 2: Details for Non-EC Products
Sr.
No. Name of the Products
CAS no. /CI
no.
Quantity
MT/Month End-use of products
1. Lubricity Improver
Such as Diesel Lubricity Improver - 333 Additive for Diesel
2.
Drilling Chemicals such as.
Cloud Point Glycols (CPG grades
like– 108, 208, 308, 308 P, 308 PM,
608, ADN’ etc.).
Welcol B
Drill Fast etc.
- 250 Additive for Oil Drilling
3. Polyol - 500 Additive for Oil Drilling
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Grades like Grade I, Grade II etc.
4. Emulsifier for Agrochemicals
Cristol grades like E55 A, E55 T etc. - 40
Additive for Insecticide /
Pesticide Spraying
5.
Conning oil Emulsifier
Grades like COE 70, COE 150,
Antistatic Conning oil etc.
- 150 Additive for Textile
6. Oil based Agrochemicals such as
Tree Spray Oil - 15
Additive for Apple & Tea Anti
insect Spray
7. Octane Booster - 300 Additive for Gasoline
8. Cold flow Plug Point (CFPP) - 100 Additive for Diesel for Cold
Countries
Total 1688
• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.
• PP was called for presentation in the SEAC meeting dated 03/10/2018.
• Salient features of the project are as under:
Sr.
no. Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing: 9.82 Crores
Proposed: 26.18 Crores Total: 36 Crores
B Total Plot area
( sq. meter)
Existing: 24094 Sq. m.
Proposed: 16063.67 Sq. m.
Total: 40157.67 Sq. m.
Green belt area,/Tree Plantation area
( sq. meter)
Existing: 6289 Sq. m.
Proposed: 6010 Sq. m.
Total: 12299 Sq. m.
C Employment generation
Existing: 15
Proposed: ~145 People (30 Direct +15
Indirect (contract employee during
operation phase) +100 Contractor Workers
will involve only during Project Phase)
Total: ~160
D Water
i Source of Water Supply Water will be sourced from GIDC water
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(GIDC Bore well, Surface water, Tanker supply etc...) supply authority.
Status of permission from the concern authority. Letter from GIDC for water supply is
shown in Annexure 5 in EIA Report.
ii Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 0.5 2 2.5
(B) Gardening 2 8 10
(C) Industrial
Process 0 9 9
Washing 1 5 6
Boiler 4 19.5 23.5
Cooling Tower 20 183 203
Softener Unit 1 3.5 4.5
DM Unit 1 4 5
Blending 9 2 11
Scrubber 0 3 3
Industrial Total 36 229 265
Grand Total (A+B+C)
38.5 239 278
278 KLD is
Including 40 KLD
recycled water
from RO
1) Total water requirement for the project: 278 KLD
2) Quantity to be recycle: 40 KLD
3) Total fresh water requirement: 238 KLD
iii Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 0.4 1.6 2 To ETP followed by
RO, 40 KLD RO
permeate to be
recycled and 21
KLD RO Reject will
(B) Industrial
Process 0 9 9
Washing 1 3 4
Boiler 0.4 3 3.4
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Cooling Tower 1 28 29 be discharged into
GIDC Drain Softener Unit 1 3.5 4.5
DM Unit 1 4 5
Blending 0 0 0
Scrubber 0 3 3
Lab Equipment Washing 0 2 2
Total Industrial waste
water 4.4 55.5 59
RO Reject to GIDC
Drain - - 21
To GIDC drain for
Sea disposal
iv
Treatment facility within premises with capacity [For existing and Proposed]
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
The process wastewater and utilities blow down will be treated in ETP followed by RO. Capacity of
ETP is 70 KLD (35 KLD x 2).
v
Mode of Disposal & Final meeting point
Domestic: Treated wastewater will be discharged into GIDC drain matching with GPCB
standards.
The permission letter from the GIDC for effluent discharge into drain is shown in
Annexure 6 in EIA Report.
Industrial:
vi
In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility
Not Applicable
Membership of Common facility (CF)
Not Applicable
vii Reuse/Recycle details (KLD)
40 KLD RO permeate to be recycled.
E Air
i
Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
Existing & Proposed
-
Sr.
no.
Source of
emission
With
Capacity
Stack
Height
(meter)
Type of
Fuel
Quantity of
Fuel
Kg/Hr
Type of
emissions i.e.
Air Pollutants
Air Pollution
Control
Measures
(APCM)
Existing
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1
Steam Boiler
– 1
(1500 Kg/hr.)
31 Furnace
Oil 94
PM, SO2, NOx
Adequate Stack
Height is
provided 2
DG set -1
(600 kVA) 11 HSD 127
Proposed
1
Steam Boiler
– 2
(1500 Kg/hr.)
31 Furnace
Oil 94
PM, SO2, NOx
Adequate Stack
Height is
provided
2
Steam Boiler
– 3
(2000 Kg/hr.)
31 Furnace
Oil 127
3
Thermic
Fluid Heater
(10 Lac
Kcal/hr.)
31 Furnace
Oil 120
After Proposed Expansion
1
Steam Boiler
– 1
(1500 Kg/hr.)
31
Furnace
Oil 94 Kg/hr.
PM, SO2, NOx
Adequate Stack
Height is
provided
2
Thermic
Fluid Heater
(10 Lac
Kcal/hr.)
Furnace
Oil 120 Kg/hr.
3
Steam Boiler
– 2
(1500 Kg/hr.) 31
Furnace
Oil 94 Kg/hr.
4
Steam Boiler
– 3
(2000 Kg/hr.)
Furnace
Oil 127 Kg/hr.
5 DG set -1
(600 kVA) 11 HSD 127 Kg/hr.
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing & Proposed
-
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Sr. no. Source of
emission
Type of
emission
Stack/Vent
Height (meter)
Air Pollution Control
Measures
(APCM)
1 Reactor (6 Nos.) VOC 10 Water Scrubber
2 Storage Tank Area VOC 10 Water Scrubber
-
iii Fugitive emission details with its mitigation measures.
Fugitive Emission:
Dust from the Road during transportation, leaks from Pressure vessel, valves, pumps, compressor
& flanges.
Mitigation Measures:
Routine inspections of process & Storage equipment/vessel with gas detectors, Hydro-test to
identify leaks and estimate the leak rate in order to decide on appropriate corrective action.
Replacement of old gaskets, tightening of flanges, Replacement/repair of valves etc. Water
sprinkling at road & Green belt development in plant and nearby road area.
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
Ex
isti
ng
Pro
po
se
d
To
tal
1 Skimmed oil
in ETP
Equipment
washing,
spillage or
leakage during
process/
drumming
35.4 0.4 0.36 0.76
Store in
Carboys &
resale for
reuse
2 ETP Sludge Microbiological
activity in ETP 35.3 0.12 36
36.1
2
Collect in bags
send to GPCB
approved
party for
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disposal
3 Used oil
Gear, pump,
DG, Forklift,
Transformer
5.1 0.2 0.12 0.32
GPCB
approved
authorized
recycler
4 Cotton waste Generate during
cleaning 33.2 0.16 0.12 0.28
Collect in bags
GPCB
approved
authorized
recycler
5
Used
container/
barrel
Manufacturing
Process 33.1
130
Nos.
120
Nos.
250
Nos.
GPCB
approved
party
6
Waste drum
seals and
caps
Manufacturing
Process 33.1 0.16 0.012
0.17
2
GPCB
approved
party
7 Waste
Catalyst
Spent catalyst in
process 18.1 0 14.4 14.4
Collect in bags
for land filling
as per CPCB
guideline for
waste disposal
8 Waste Filter
Cloth
Waste filter cloth
after filtration 36.2 0 1.2 1.2
Collect in bags
and Send to
GPCB
approved
party for
disposal
9 Spent Carbon
From
manufacturing
Process and
ETP
36.2 0 12 12
Collect in bags
and send to
GPCB
approved
party for
disposal
ii Membership details of TSDF, CHWIF etc. TSDF: Membership letters from the M/s.
BEIL & RSPL for Liquid waste & hazardous
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waste disposal is given in Annexure 7 in
EIA Report.
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
Bio-medical waste:
The generated waste will be collected
separately and handed over to bio medical
waste treatment agencies as per the GPCB
regulation and bio-medical waste
management rule 2011. Quantity of Bio-
medical waste generation is 0.030
MT/Annum.
Domestic Waste:
Electronic Wastes
Generated Electronic wastes will be
collected separately and handover to e-
waste disposal agencies to dispose as per
the provisions of the E-Wastes
(Management and Handling) Rules, 2011.
Quantity of E-waste generation is 0.2
MT/Annum.
Kitchen/canteen waste and other
biodegradable waste is collected separately
and sent to authorize agencies of
Vermicomposting.
The non-hazardous recyclable waste like
paper, plastic, metal and wooden waste will
be sold further to Authorize Re-Processor &
recycler. Quantity of Non-Hazardous solid
waste is 0.05 MT/Annum.
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
There are different types of Aromatic & Hydrocarbon solvents are used in the Process. Quantity &
Name of each solvent is mentioned in above Table. Most of the solvents are mixed for the dilution
of the product as per the requirement. Only in Octylated/Butylated Di Phenyl Amine based product
the excess solvent is added into the feed to reactivate the catalyst and steady the rate of reaction.
The excess solvent is recovered by flash distillation method and same will be reused as a raw
material for next batch. The mass balance of the same is given below.
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S.
No. Name of Solvent
Solvent
Used in
MTPM
Spent Solvent
recovered in
MTPM
%
Recovery Remark
1 Fresh C4 Olefins
Solvent 83 22 27
Recovered
solvent is reused
in the process
ii VOC emission sources and its mitigation measures
• Source:
S. No. Stack Attached to Nos. of
Stack
Stack Height
in m
Pollutants
Emitted
Air Pollution Control
Measures Attached to
1 Reactor (6 Nos.) 1 10 VOC Water Scrubber
2 Storage Tank Area 1 10 VOC Water Scrubber
• Mitigation Measures:
Water Scrubber
VOC is pulled out through vacuum after completion of reaction and passed through packed column
water scrubber and majority VOC will be dissolved in water while ppm level VOC will be discharged
through vent along with air. Dissolved VOC will be sent to ETP for the further treatment.
Detection and monitoring of VOC’s / gases
For the detection of VOC's /Gases fixed detector will be installed at prominent locations and
portable leak detector sensors will be used whenever required.
• During the meeting dated 03/10/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for expansion of existing unit and for now proposes a new synthetic organic chemical
product. This unit is having CTE for existing unit and production is not yet started. Copy of CTE and
CTE compliance report is submitted. PP ensured that there is no court cases pending and no public
complaint is there against the project.
• Total water consumption will be 278 KLD. Total wastewater generation will be 59 KLD. After
proposed expansion, ETP proposed of 70 KLD capacity & after full-fledged ETP treatment and RO
plant treatment, 40 KLD treated effluent i.e. RO permeate shall be reused back in washing purpose
and rest of treated effluent i.e. RO reject shall be discharged into underground drainage of GIDC
which ultimately meets to Deep sea. Domestic effluent will be 2 KLD and shall be treated in proposed
ETP along with industrial effluent.
• Furnace oil will be used as fuel for proposed boilers and thermic fluid heater.
• Adequate APCM will be provided for proposed process gas emission.
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• Hazardous waste management will be as per the HW Rules.
• The baseline environmental quality has been assessed for various components of the environment
viz. air, noise, water, biological and socioeconomic aspect. The baseline environmental study has
been conducted for the study area of 5 km radial distance from project site for the period March,
2017-May, 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, HCl,
Cl2, HBr, CO and VOC at eight locations, including the project site. Values conform to the prescribed
standards for Ambient Air Quality. The incremental Ground Level Concentration (GLC) has been
computed using AIRMOD. The resultant concentrations are within the NAAQS. The modelling study
proved that the air emissions from the proposed plant would not affect the ambient air quality of the
region in any significant manner. The ambient air quality around the proposed project site will remain
within the National Ambient Air Quality Standards (NAAQS).
• Risk assessment including prediction of the worst-case scenario and maximum credible accident
scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site
Emergency Plan has been covered in the RA report.
Discussions & Conclusion:
• Committee deliberated on Compliance of existing project (CCR), possibilities of automization of the
manufacturing plant, handling and storage of Hazardous chemicals like Cl2, Toluene & other
hazardous chemicals, APCM for process gas emission, SOP for safety precautions, Baseline, CER,
HW management etc.
• PP informed that they will follow the PESO standards for unloading, storage, transportation, handling
and processing of solvents.
• During appraisal committee noticed that quantities of waste water generation, permeate and RO
rejection are not in consonance and asked PP to submit revised water balance.
• It is noted that solvent recovery for Fresh C4-Olefin is 24 % and could not justify its balance quantity,
hence PP was asked to address details solvent recovery after considering its quantity used in
product.
• Need based survey for implementing CER with outlay of upcoming years could not be addressed
satisfactorily by the PP.
After detailed discussion, it was decided to ask project proponent to submit the following details and
upon receipt of the same, it was decided to consider the proposal in one of the upcoming SEAC
meeting.
1. Revised Water balance with detailed break up of water consumption, reuse and waste water
generation with quality of treated waste water discharge to underground GIDC drain.
2. Revised details for recovery of fresh C4 Olefin solvent along with other high vapour pressure solvents
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considering consumption in product.
3. Revised CER details as per the MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment
Responsibility” (CER). The details of fund allocation and activities for CER shall be incorporated in
EIA/EMP report based on need-based survey.
4. .Revised details of Hazardous waste as per the Hazardous and Other Waste (Management and
Transboundary Movement)Rules 2016.
9 SIA/GJ/IND2/19982/2017 Tatva Chintan Pharma Chem Pvt. Ltd. (Unit-2),Plot: Z/103/F/2, Dahej, SEZ, Part-II,Vagra,Bharuch
EC Amendment
Project Proponent could not attend the meeting. Committee decided to defer the proposal in one of
the upcoming SEAC meeting.
10 SIA/GJ/IND2/28455/2018 M/s. Vaidik Industries Plot No- C-218, Saykha Industrial Estate, Ta: Vagra, Dist.: Bharuch
Screening and scoping
Project / Activity No.: 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/28455/2018 dated
10/08/2018 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is a new unit proposes for Synthetic Organic Chemicals manufacturing plant as tabulated below:
SR. NO PRODUCT NAME Proposed
1. Dyes
1. Reactive Orange ME2RL
600
MT/Month
2. Reactive Orange 122 AA
3. Reactive Orange H2R
4. Reactive Yellow 160
5. Reactive Yellow M8G
6. Reactive Red 223
7. Reactive Blue R
8. Reactive Violet 5R
9. Reactive Red ME6BL
10. Reactive Yellow ME4GL
11. Reactive Blue M2R
12. Reactive Blue 220
13. Reactive Blue 221
14. Reactive Blue 21
15. Reactive Blue 25
16. Reactive Blue PGR
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17. Reactive Black 5
18. Reactive Black B
19. Reactive Black HN
20. Reactive Black RL
21. Reactive Blue 194
22. Reactive Blue 203
23. Reactive Blue 222
24. Reactive Blue 5RH
25. Reactive Blue P3R
26. Reactive Blue BB,BF
27. Reactive Blue GG(203)
28. Reactive Blue HEGN
29. Reactive Blue HERD(Blue 160)
30. Reactive Blue ME2RL
31. Reactive Golden Yellow RNL
32. Reactive Green HE4BD
33. Reactive Orange M2R
34. Reactive Orange W3R
35. Reactive Red BB(21)
36. Reactive Red CD
37. Reactive Red H7B(Red 227)
38. Reactive Red H8B
39. Reactive Red HE3B
40. Reactive Red HE7B
41. Reactive Red ME3BL(Red 194)
42. Reactive red ME4BL
43. Reactive Red P2B
44. Reactive Red P6B
45. Reactive Red PB
46. Reactive Yellow F3R
47. Reactive Yellow H7GL (Yellow 157)
48. Reactive Yellow HE4G (Yellow 88)
49. Reactive Yellow HE4R(84)
50. Reactive Yellow HE6G(Yellow 135)
51. Reactive Yellow MERL
52. Reactive Yellow P6G
53. Acid Black 194
54. Acid Black 234
55. Direct Black 22
56. Acid Black 210
57. Direct black 168
58. Direct Black 80
59. Acid Brown 14
2. Intermediates
1. NMJ (N Methyl J Acid) 20
2. Sulfo J Acid 20
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• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.
• PP was called for presentation in the SEAC meeting dated 03/10/2018.
• The project proponent along with their expert /consultant M/s. Satva Environ Consultancy attended
the meeting and made presentation before the committee
• Salient features of the project are as under:
Sr. no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores):
5.0 Crores
B Total Plot area ( sq. meter) 3978 Sq. m.
Green belt area ( sq. meter)
800 Sq. m.
C Employment generation Direct: 20 Indirect : 10 Total : 30
D Water
i
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Supply
Status of permission from the concern authority.
ii Water consumption (KLD)
Category Water Consumption KLD Remarks
(D) Domestic 4.0
Out of total Water requirement of 120 KLD, 53.5 KLD Water reuse in process and washing and 66.5 KLD Water received through GIDC
(E) Gardening
(F) Industrial
Process *50.5 (R) + 43.5 (F)
Washing *3.0 (R)
Boiler 20.0
Cooling 10.0
Industrial Total 116.0
Total (A + B + C) 120.0
Note: *53.5 KLD Reuse From MEE Condense Water
4) Total water requirement for the project: 120 KLD 5) Quantity to be recycled: 53.5 KLD 6) Total fresh water requirement: 66.5 KLD
iii Waste water generation (KLD)
Category Waste water generation KLD Remarks (C) Domestic 1.8 (D) Industrial
Process 63.0 69.0 KLD waste water send to
Washing 3.0
Boiler 2.0
3. 2-Pyridone 10
4. OVAS 10
5. K acid 5
6. G Salt 20
7. Bromamine Acid 5
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Cooling 1.0 primary, secondary and tertiary ETP plant followed by MEE
Scrubber spent Acid 0.08
Total Industrial waste water
69.0
Total [A + B] 72.0
-
iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
Sr. No. Name of Unit Capacity
1 Collection Tank 100 KL
2 Primary Settling Tank 25 M3
3 Aeration Tank 100 M3
4 Secondary Settling Tank 25 M3
5 Sludge Drying Bed 15 M3
6 Filter Feed Tank 5 M3
7 Activated Carbon Filter 5 M3
8 Multi Effect Evaporator 10 M3/Hour
v Mode of Disposal & Final meeting point
Domestic:
Domestic 1.8 KLD sewage generated will be disposed through soak pit/septic tank.
Industrial:
Total Waste Water generation 69.0 KLD from manufacturing activity and other ancillary operation Waste Water treated Primary and secondary and tertiary Effluent treatment. After than it will be send In House MEE. The Condensate of MEE will reuse in Process and Washing to achieve Zero liquid Discharge. We will maintain Zero Liquid Discharge till CETP of Saykha will commission. After commissioning of Saykha CETP, we will discharge wastewater to CETP after obtaining requisite permission from concern Authority. We assure you that we will operate adequate treatment technology to achieve norms prescribed by CETP
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , Name of CF
We will obtain necessary permission to discharge generated wastewater to CETP Saykha and till then we will maintain Zero Liquid Discharge.
Membership of Common facility (CF) (For waste water treatment)
Unit will achieve Zero liquid Discharge. We will maintain Zero Liquid Discharge till CETP of Saykha will commission. After commissioning of Saykha CETP, we will discharge wastewater to CETP after obtaining requisite permission from concern Authority. We will obtain membership of common facility for disposal of Hazardous waste after before obtaining CC&A from State PCB
vii Simplified water balance diagram with reuse / recycle of waste water
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viii Reuse/Recycle details (KLD)
Total reuse 53.5 KLD
Source of waste water for reuse with quantity in KLD
Application area with quantity in KLD
Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.)
Condensate of MEE 53.5 KLD
Process 50.5 KLD COD : 200 – 300 mg/L BOD: 50-70 mg/L TDS: 1200-1500 mg/L Washing 3.0 KLD
E Air
i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
-
Sr. no.
Source of emission
With Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions
i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
1
Industrial steam
Boiler (4 TPH)
11.00 Imported Coal OR
Agro waste
17 MT/Day
OR 20
MT/Day
PM SO2
NOx
Multi cyclone
Separator followed by Bag Filter with water scrubber
2 Hot Air
Generator (2 Nos.)
11.00 Imported Coal OR
Agro waste
13 MT/Day
OR
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15 MT/Day
3 D. G. Set 5.00 HSD 10 L/hr Acoustic Enclosure
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr. no. Source of emission Type of
emission
Stack/Vent Height (meter)
Air Pollution Control Measures
(APCM)
1 Spray Dryer (1000
LPH) PM 11.00
Multi cyclone Separator followed by water scrubber 2
Spray Dryer (1500 LPH)
3 Reactor (NMJ product) SO2 7.00 Alkali scrubber
4 Reactor (OAVS) HCl 7.00 Two Stage Water
scrubber
5 Reactor (K Acid) SO2 7.00 Alkali scrubber
6 Reactor (G Salt) HCl SO2
7.00 Water scrubber
followed by Alkali Scrubber
7 Reactor (Bromamine
Acid ) HCL 7.00
Two Stage Water scrubber
-
iii Fugitive emission details with its mitigation measures. As below:
� The entire manufacturing activities will be carried out in the closed reactors and regular checking and maintenance of reactors will be carried out to avoid any leakages.
� The tank vents will be equipped with either a carbon filter or an oil trap to prevent water vapor from entering the tank as it breathes.
� All the motors of pumps for the handling of hazardous chemicals will be flame proof and provided with suitable mechanical seal with stand-by arrangement
� Control of all parameters on a continuous basis will be done by adequate control valves, pressure release valves and safety valves etc.
� All the flange joints of the pipe lines will be covered with flange guards. � All the raw materials will be stored in isolated storage area and containers tightly
closed. � There will also be provision of adequate ventilation system in process plant and
hazardous chemical storage area. � A regular preventive maintenance will be planned to replace or rectify all gaskets,
joints etc. � The unit will also develop green belt within the factory premises to control the
fugitive emission from spreading into surrounding environment
F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
i
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Sr. No
Types of Hazardous
Waste
Specific Source of generation
Category and Schedule as per HW Rules.
Quantity (MT/Annum)
Management of HW
1 ETP
Sludge ETP Area 35.3
108.0 MT/Year
Collection, storage, Transportation and Dispose to Active
TSDF Site
2 Used Oil Plant
Machinery 5.1
5 lit/year
Collection, storage, Reuse within premises in
maintenance work.
3 Discarded Container/
Bags
Material storage and
Handling 33.1
42 MT/Year
Collection, storage, Transportation and
Dispose to Registered Recycler
4 Process Waste Sludge
Dyes Intermediates
26.1 24
MT/Year
Collection, storage, Transportation and
Dispose to TSDF Site
5
Spent Sulphuric Acid (30-
35%)
Dyes Intermediates
(OAVS, K Acid, NMJ
Acid )
26.3 4800
MT/Year
Collection, storage and partially reuse
(3550 MT/Annum) in OAVS, Supho J Acid,
NMJ Acid, G Salt Transportation and
remaining will sell to Rule-9 Authorized
Units
6 Spent HCl
Acid (18-25 %)
Reactive Blue Dyes, OAVS G
Salt, Bromamine
Acid
26.3 2400
MT/Year
Collection, storage and partially reuse
(1500 MT/Annum) in reactive dyes with
fresh HCl and remaining will sell to Rule-9 Authorized
Units
7 Acetic Acid (70 % to 75
%)
Dyes Intermediates
OAVS 26.3
120 MT/Year
Collection, storage, Transportation and
sell to Rule-9 Authorized parties
8 Solvent Residue
Distillation Unit
26.1 12
MT/Year
Collection, storage, Transportation and
Dispose by sending to common facility
9 Spent
Solvent Bromamine
Acid 26.4
260.4 MT/Year
Collection, storage and Reuse With in
Plant Premises after in house Distillation in
solvent dyes
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10 Glauber Salt/ Salt
from ATFD
MEE Operation,
ATFD Operation &
OAVS
26.1 300
MT/Month
Collection, storage, Transportation and
Dispose by sending to common facility
11.
SBS (20 To 25%)
K Acid 26.3 80
MT/Annum
Collection, storage and Partially (72
MT/Annum Reuse With in Plant
Premises in OAVS and remaining will be
sell to units having permission of Rules 9
ii Membership details of TSDF, CHWIF etc. (For HW management)
We will obtained after getting NOC from GPCB
iii Details of Non-Hazardous waste & its disposal (MSW and others)
Not applicable
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
• Types of Solvent : ODCB
• Spent solvents will be recovered through in-house distillation column with double condenser system with chilling water to achieve optimum recovery
• 95-98% recovery will be carried out.
• Recovered solvents will be collected in receiver and transferred to reaction vessel through vaccum and completely reused within process.
ii VOC emission sources and its mitigation measures • Sources of fugitive emissions include storage of chemicals, solvents storage, loading
and unloading section, raw material handling and, hazardous waste storage area
Measures : • The fugitive emissions in terms of handling losses will get reduced by proper storage
and handling.
• Hazardous chemicals will be stored as per standard criteria. • Periodically monitoring will be carried out as per the post project monitoring plan.
• Proper ventilation in storage & production area shall be ensured
• All materials must be stored in suitable packing to prevent contamination of air .
• Enclosed system & efficient procedures for materials charging shall be ensured.
• Procedures for start-up shut down, operation & maintenance procedures shall be established & maintained.
• The coverage of greenbelt around the plant also acts as natural barrier to stop carrying of dust along with the wind current
• During the meeting dated 03/10/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for a new synthetic organic chemical product.
• Total water consumption will be 120.0 KLD. Total wastewater generation will be 69.0 KLD. 69.0 KLD
waste water send to primary, secondary and tertiary ETP plant and then treated effluent will be sent
to four stage evaporator and thus maintain complete zero liquid discharge.
• They will maintain Zero Liquid Discharge till CETP of Saykha will commission. After commissioning of
Saykha CETP, they will discharge wastewater to CETP after obtaining requisite permission from
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concern Authority. They assure you that we will operate adequate treatment technology to achieve
norms prescribed by CETP
• Imported coal and agro waste will be used as fuel for boiler and Hot air Generator.
• Adequate APCM will be provided commonly with boiler and hot air generator.
• Separated adequate APCM will be provided with reactors.
• Hazardous waste management will be as per the HW Rules 2016.
Discussions & Conclusion:
Committee deliberated on area adequacy, waste water management, waste streams, APCM, Hazardous
waste, safety aspects for handling of all the proposed raw materials, products and hazardous waste to be
handled during manufacturing activities.
Considering the above project details, after detailed discussion, the terms of reference (ToR) were
prescribed as below and as per the standard TOR for the Synthetic Organic Chemical projects
recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and approved by SEIAA
in its 12th meeting dated 16/09/2017 for the EIA study to be done covering 10 Km radial distance from
the project boundary.
1. Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment
Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be
made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities
therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP
report.
2. Adequacy of proposed area with respect to plant machineries , EMS, green belt , safety aspect,
raw material & product storage considering worst case scenario. Submit proper lay out plan
clearly demarcating all activities with scale.
3. Segregation of waste water streams based on characteristics and its proper management and
detailed treated waste water management after ETP with qualitative analysis.
4. Treatability & adequacy report for complete ZLD system. Feasibility report for complete reuse
condensate waste water for industrial purpose.
5. Explore the use of renewable energy to the maximum extent possible. Details of provisions to
make the project energy-efficient through of energy efficient devices and adoption of modes of
alternative eco-friendly sources of energy like solar water heater, solar lighting etc. Measures
proposed for energy conservation.
6. Selling of hazardous waste like spent acid to units having permission under Rule-9 of HWR 2016
and also submit MoU with them with quantity.
7. Qualitative and quantitative analysis of hazardous waste streams like Spent Sulphuric Acid (25-
30%), Spent HCl Acid (18-20 %) from the manufacturing process (Product wise) with their
proposed use within premises with feasibility and adequacy.
8. Qualitative and quantitative analysis of hazardous waste streams like Process Waste Sludge
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(26.1) and solvent residue generation from the manufacturing process (Product wise).
9. To Explore the possibility to reuse such waste streams within premises as raw materials for other
products or to convert it into valuable products instead of selling out side. Sound management of
such waste streams as per the HW Rules 2016 as amended time to time. Feasibility report for
utilization of hazardous waste shall be incorporated in EIA report.
10. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard &
Occupational health hazards during unloading, storage, transportation, handling and processing
of hazardous chemicals like solvents, Toluene etc.
11. Safety precautions for solvents as per the PESO standards.
12. Submit Narcotics department permission for use of acetic anhydride and its management of
handling.
13. Justification for water consumption and waste water generation not in proportion with the product
quantity
The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs
available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be
considered as generic TORs for preparation of the EIA report in addition to all the relevant information as per
the generic structure of EIA given in Appendix III in the EIA Notification, 2006.
The project proponent shall have to apply for Environmental clearance through online portal http://environmentclearance.nic.in/ along with final EIA report.
11. SIA/GJ/IND2/28468/2018 M/s. Uma Pharma Chem Plot No. : 111, GIDC Gozaria, Taluka: Mehsana, District: Mehsana, Gujarat.
Screening and scoping
Project / Activity No.: 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/28468/2018 dated
04/08/2018 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is a new unit proposes for Synthetic Organic Chemicals manufacturing plant as tabulated below:
Sr. No.
Name of the Products
CAS no. /CI no.
Quantity MT/Month
End-use of products
1 Metallic Stearate (Zinc, Magnesium, Lead, Calcium)
557-05-01, 557-04-01, 1072-35-1, 1592-23-0
800 Use in Polymers & Rubber, Pharmaceutical & Cosmetics, Building & Construction.
2 Metallic Octoate (Zinc, Lead, Cobalt)
557-09-5, 7319-86-0, 13586-82-8
600 Use in Polymers & Rubber industries.
3 PVC Stabilizer 26636-01-1 300 Use in Construction application.
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• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.
• PP was called for presentation in the SEAC meeting dated 03/10/2018.
• The project proponent along with their expert /consultant M/s. Enviro Fluid Consultants., Ahmedabad attended the meeting and made presentation before the committee
• Salient features of the project are as under :
Sr. no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores): 0.95 Crores
B Total Plot area ( sq. meter) 1088 Sq. m.
Green belt area ( sq. meter) 360 Sq. m. (33%)
C Employment generation 12
D Water
i
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)
GIDC water supply
Status of permission from the concern authority. Permission obtained from GIDC
ii Water consumption (KLD)
Category KLD Remarks
(G) Domestic 4 Fresh water (H) Gardening 1.8 Fresh water (I) Industrial
Process 0.0
Washing 0.2 Fresh water
Boiler 0.0
Cooling 0.0
Others 0.0
Industrial Total 0.2
Total (A + B + C) 6.0
7) Total water requirement for the project: 6.0 KLD 8) Quantity to be recycled: 0.0 KLD 9) Total fresh water requirement: 6.0 KLD
iii Waste water generation (KLD)
Category Waste water KLD
Remarks
(E) Domestic 3.0 Septic tank followed by soak pit
(F) Industrial
Process 0.0
Washing 0.2 To ETP
Boiler 0.0
Cooling 0.0
Others 0.0
Total Industrial waste water
0.2
iv Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
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ETP – Neutralization followed by Sludge separation followed by Evaporation (50 L/Hr capacity Thermic Evaporator).
v Mode of Disposal & Final meeting point
Domestic: Domestic: Soak pit
Industrial: Industrial: Zero liquid discharge
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , Name of CF
Not applicable
Membership of Common facility (CF) (For waste water treatment)
Not applicable
vii Simplified water balance diagram with reuse / recycle of waste water
Source of Water Supply: GIDC Supply
Total: 6 KL/day
Domestic
4.0 KL/day
Sewage to septic tank & Soak Pit
3.0 KL/day
Washing
0.2 KL/day
Industrial
0.2 KL/day
Wastewater
0.2 KL/day
Gardening
1.8 KL/day
ETP followed by
Evaporator
Zero liquid discharge
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Effluent Quality:
Particular Unit Untreated Effluent
Treated Effluent
(Completely evaporated)
pH -- 6.0 - 6.5 7.0 - 7.5
Total Suspended Solids mg/l 150 - 200 < 50
Chemical Oxygen Demand mg/l 300 - 400 < 100
Total Dissolved Solid mg/l 2500 – 3000 2500 - 3000
viii Reuse/Recycle details (KLD)
Total reuse 0.0 KLD
Source of waste water for reuse with quantity in KLD
Application area with quantity in KLD
Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.)
Not Applicable
E Air
i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
-Sr. no.
Source of
emission With
Capacity
Stack Height (meter)
Type of Fuel
Quantity of Fuel MT/Day
Type of emissions
i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
1 Thermic
Fluid Heater
15 Briquettes/
Coal 65 Kg/Hr
Particulate Matter ≤ 150 mg/Nm
3,
SO2 ≤ 100 ppm, NOx ≤ 50 ppm
Multi Cyclone Separator
followed by Adequate
Stack height
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emission
Stack/Vent Height (meter)
Air Pollution Control
Measures (APCM)
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Not Applicable
-
iii Fugitive emission details with its mitigation measures. As below:
Standard handling practices are adopted for powdered chemical. Proper storage, charging system, handling system and online monitoring systems are provided and same will be taken care for proposed project.
F Hazardous wastes (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.
i
Sr. no.
Type/ Name of
Hazardous waste
Specific Source of generation (Name of the
Activity, Product etc.)
Category and
Schedule as per
HW Rules.
Quantity (MT/Annum)
Management of HW
1 Used/spent
Oil Plant & Machineries 5.1 0.01
Collection, storage,
Transportation and reuse
within premises for lubrication or disposal to registered recycler.
2 Discarded
Containers/ bags
Raw materials and products
33.1 6
Collection, storage,
Transportation & sell to
authorized vendor
3 ETP Sludge
and Wastewater treatment
systems 35.3 9.7
Collection, storage,
Transportation and Disposal
at TSDF 4
Evaporation Salt
Treated water evaporation
35.3 0.3
-
ii Membership details of TSDF, CHWIF etc. (For HW management)
iii Details of Non-Hazardous waste & its disposal (MSW and others)
Not applicable
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
• There is not any Solvent use as raw material in manufacturing process.
ii VOC emission sources and its mitigation measures • Due to Manufacturing process chances of VOC emissions. Entire process and
material charging has been carried out in closed loop. Regular work place monitoring will be done. Standard SOP will be followed to handle powder and liquid raw materials.
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• During the meeting dated 03/10/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for a new synthetic organic chemical product.
• Total water consumption will be 5.0 KLD. Total wastewater generation will be 0.2 KLD. 0.2 KLD
waste water send to Neutralization followed by Sludge separation followed by Evaporation (50 L/Hr
capacity Thermic fluid Evaporator).
• Briquette/coal will be used as fuel for thermic fluid heater.
• Adequate APCM will be provided commonly with thermic fluid heater.
• Hazardous waste management will be as per the HW Rules 2016.
Discussions & Conclusion:
• Committee deliberated on area adequacy, waste water management, ,APCM, Hazardous waste,
safety aspects etc.
Considering the above project details, after detailed discussion, the terms of reference (ToR) were
prescribed as below and as per the standard TOR for the Synthetic Organic Chemical projects
recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and approved by SEIAA
in its 12th meeting dated 16/09/2017 for the EIA study to be done covering 10 Km radial distance from
the project boundary.
1. To address treated waste water quality and evaporation salt generation in consonance to each
other. Feasibility and Adequacy of operation of thermic fluid based evaporator.
2. Adequacy of proposed area with respect to plant machineries , EMS, green belt , safety aspect,
raw material & product storage considering worst case scenario. Submit proper lay out plan clearly
demarcating all activities with scale.
3. Explore the use of renewable energy to the maximum extent possible. Details of provisions to
make the project energy-efficient through of energy efficient devices and adoption of modes of
alternative eco-friendly sources of energy like solar water heater, solar lighting etc. Measures
proposed for energy conservation.
4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard &
Occupational health hazards during unloading, storage, transportation, handling.
The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs
available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be
considered as generic TORs for preparation of the EIA report in addition to all the relevant information as per
the generic structure of EIA given in Appendix III in the EIA Notification, 2006.
The project proponent shall have to apply for Environmental clearance through online portal
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http://environmentclearance.nic.in/ along with final EIA report.
12. SIA/GJ/IND2/28481/2018 M/s. Gulshan Polyols Ltd . Plot No. 762, 762/1, 762/2, 762/3, 769/1 & 769/2, GIDC Jhagadia, Dist.: Bharuch, Gujarat
Screening & Scoping
+Project / Activity No.: 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/28481/2018 dated
10/08/2018 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is an expansion unit and proposes for expansion of Synthetic Organic Chemicals manufacturing
plant as tabulated below:
Sr. No.
Products Capacity, TPM*
End-use E P T
1. Starch Slurry Powder (90.0 %) 3750 2250 6000 Textile & Food industry
2. Sorbitol (70 %) 6000 6000 12000 Gel toothpaste and ingredient to pharmaceutical products
3. Dextrose Mono–hydrate (98.5 %)
1250 750 2000 Food industry
4. Mannitol Powder (99.5 %) 416 Nil 416 As excipient to Pharmaceutical industries
5. Glucose (99.0 %) 1250 Nil 1250 Food industry
6. Sorbitol Powder (98.5 %) 215 Nil 215 As excipient to pharmaceutical industries
7. Calcium Carbonate (GCC/Wet/ACC), (98.0 %)
1250 Nil 1250 As a filler for PVC, Rubber and Paint
Total 14131 9000 23131
8. Co-Gen power 3.0 MW 1.5 MW 4.5 MW Captive consumption
Sr. No.
By- Products Generation, TPM*
E P T
1. Maize Germ Oil Cake 440 270 710
Used for Cattle feed 2. Maize Germ Oil (88 %) 550 330 880
3. Maize Germ -- 1350 1350
4. Wet Fiber (92 %) 2,750 2500 5250
5. Gluten (90 %) 915 550 1465 Used for poultry food
6. Filter Cake 150 1500 1650 Used for Brick manufacturing
7. Lime Stone Grit (10 %) 150 Nil 150 As a filler for PVC, Rubber and Paint
8. Mud Lime Clay (5 %) 100 Nil 100 Used for Brick manufacturing
*E: Existing, P: Proposed, T: Total
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• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.
• PP was called for presentation in the SEAC meeting dated 05/09/2018.
• The project proponent along with their expert / consultant M/s. Envisafe Environment Consultants
attended the meeting and made presentation before the committee
• Salient features of the project are as under:
Sr. No.
Particulars Details
A Total cost of the proposed project (Rs. in Crores)
Existing: 122.29 Proposed: 28.43 Total: 150.72
B Total Plot area (sq. meter) 1,27,503
Green belt area / Tree Plantation area (sq. meter)
Existing: 32,593 Proposed: 9,507 Total: 42,100
C Employment Generation Existing: 246 Proposed: 534 Total: 280
D Water
i
Source of Water Supply (GIDC, Bore well, Surface water etc...)
GIDC
Status of permission from the concerned authority.: Permission obtained from GIDC
ii Water consumption (KL/day)
-
Category Existing KL/day
Proposed (Additional)
KL/day
Total after Expansion
KL/day Remarks
(J) Domestic 17.5 7.5 25.0 Fresh (K) Industrial
Process
Fresh 260.0 1,680.0 1,940.0 Fresh
Reuse 480.0 280.0 760.0 Reuse
Boiler 340.0 760.0 1,100.0 Fresh
Cooling 246.0 480.0 725.0 Fresh
Washing 40.0 160.0 200.0 Fresh
Total (A+B) 1,383.5 3,367.5 4,750 Fresh: 3,990 Reuse: 760
1) Total water requirement for the project: 4,750 KLD 2) Quantity to be recycle: 760 KLD 3) Total Fresh water requirement: 3,990 KLD
iii Waste water generation (KL/day)
Category Existing KL/Day
Proposed (Additional)
KL/day
Total after Expansion
KL/day Remarks
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(G) Domestic 17.5 2.5 20.0
(H) Industrial
Process 690.0 1,650.0 2,340.0
Boiler 100.0 720.0 820.0
Cooling 30.0 370.0 400.0
Washing 40.0 160.0 200.0
Total Industrial waste water
860 2,900.0 3,760.0 Generation: 3,760 Reuse: 760 Discharge: 3000
-
iv Treatment facility with capacity (ETP, CETP, MEE, STP etc).
Unit Status
Hydraulic Load, KLD Design
Capacity, KLD Existing
After Proposed Expansion
ETP-1
Existing
325 670 1150
ETP-2 540 3090 4200
RO 325 760 1100
MEE-1 480 670 850
MEE-2 Proposed -- 190 350
v Mode of Disposal & Final meeting point
Domestic: 20 KLD, To soak pit through septic tank
Industrial: 3,000 KLD, After treatment in ETP, discharge into NCTL through GIDC drainage system
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc name of CF
Narmada Clean Tech (NCT)
Membership of CF
Obtained membership from NCT for discharge of 380 KLD industrial effluent. Unit has booked for additional discharge of 2571 KLD. Unit will apply for additional discharge for proposed expansion.
vii Simplified water balance diagram with reuse / recycle of waste water
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viii Reuse/Recycle details (KL/day)
Total Reuse: 760 KLD
Source of waste water for reuse with quantity in
KLD
Application area with
quantity in KLD
Remarks regarding feasibility to reuse i.e. w/w characteristics
(COD, BOD, TDS etc.)
TDS COD BOD
RO – ETP (Permeate): 570 Process & APCM: 760
275 67 17 MEE Condensate: 190
E Air
i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
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Details of Flue Gas Stacks
Sr. No.
Source of emission
with capacity
Status Ht &
Dia, m
Fuel Name & Qty.
Type of Emission & Permissible
limit
APCM
1. Steam Boiler-1 (20TPH)
Existing
40 & 1.2
(Com-mon
Stack)
Coal/ Lignite
300 MT/day
PM ≤ 150 mg/Nm
3
SO2 ≤ 100
ppm
NOx ≤ 50
ppm
Electrostatic Precipitator-1
2. Steam Boiler-2 (30 TPH)
Proposed Electrostatic Precipitator-2
(Common)
3. Steam Boiler -3 (30 TPH)
Proposed
4. DG Set (1450 KVA)
Existing (Standby -
To Be Dismantled)
8.0 & 0.25
HSD 200
Lit/Day
Adequate stack height
5. DG Set (1450 KVA)
Existing (Standby -
To Be Dismantled)
8.0 & 0.25
Adequate stack height
6. DG Set (1250 KVA)
Proposed (Stand-By)
3.0 & 0.10
Adequate stack height
ii Process gas i.e. Type of pollutant gases (Existing and Proposed)
Details of Process Gas Stacks
Sr.
No. Stack attached to
Ht &
Dia
Meter
Air
Pollutant
Air Pollution Control
Equipment
Type of Emission & Permissible
limit 1st Stage 2nd Stage
1. Absorption tower of
SO2 water plant (Existing)
12*0.3 Sulphur Dioxide
Water Scrubber-A
Absorption Tower-B
SO2≤ 40 mg/NM3
2. Absorption tower of
SO2 water plant (Proposed)
12*0.3 Sulphur Dioxide
Water Scrubber-C
Absorption Tower-D
iii Fugitive emission details with its mitigation measures. (Existing and Proposed)
There will be a chance of fugitive emission and odor nuisance during manufacturing process as well as due to storage & handling of raw materials and products. The unit takes following precaution for the control of fugitive emission and will implement the
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same for the proposed expansion.
Probable Sources Control Measures
Manufacturing activities during charging into reactors
• Liquid raw materials are charged by pumping & closed
loops.
• Dosing is done by metering system to avoid fugitive
emissions.
• Dedicated measuring tanks are provided to each reactor.
• Usage of closed handling system for odorous chemicals
/solvents as far as possible.
Chemical vapor from wet cake in filtration and drying area
• Covered transfer systems will be adopted, workers shall be provided PPE.
• Fume extraction systems will be provided, wherever required
Emission from bulk storage tanks during storage, loading, unloading
• Breather valves, PSVs, Rupture disc, Vapor recovery
system are installed for process/storage tank vents.
• Unit adopts bulk handling of odorous chemicals and avoid
usage of drums/carboys for such materials
Hazardous chemical storage area
• Dedicated storage area is provided
• Adequate ventilation systems are provided
• All the containers are kept tightly closed
• Trolley/Forklift is used for transfer of drums and containers
• Transfers of odorous waste is preferably during day time.
Transfers during odd hours is avoided.
Pump and compressor Emissions
• Mechanical seals are provided in pumps and agitators
• Standby arrangement for critical equipment and parts is
ensured.
• Drip trays will be placed for each pump to collect leakages
and spillages.
Pressure relief valve emission from pipelines
• For highly pressurized lines, vent pipes of PRVs are
connected in case of toxic gases.
Valves, Flanges, plugs and instrument connections
• Welded pipes are used wherever feasible.
• Suitable gasket materials are used.
• Suitable glad packing is used in valves.
• Periodic inspection and maintenance of pipes and pipe
fittings is carried out.
Release from sampling lines
• Closed loop system is used.
Hazardous chemical storage area
• Provision of dedicated storage area
• Adequate ventilation system to be provided
• All the containers will be kept tightly closed
• Trolley/Forklift will be used for transfer of drums and containers
F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. (Existing and Proposed)
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i Type of waste
Source Catego-
ry
Quantity per Annum
Method of Disposal Existing
Proposed
Total
ETP Sludge
ETP Sch - 1
35.3 700 MT 1344 MT
2044 MT
Collection, Storage, Transportation and Disposal at TSDF of M/s. Bharuch Enviro Infrastructure Ltd.
Filter Acid Mfg of Prod.2
Sch - 1 35.1
40 MT 70 MT 110 MT
Collection, Storage, Transportation and Disposal at TSDF of M/s. Bharuch Enviro Infrastructure Ltd.
Off. Sp. Product
Mfg of Prod.
Sch - 1 28.4
38 MT 70 MT 108 MT
Collection, Storage, Transportation and Disposal at TSDF of M/s. Bharuch Enviro Infrastructure Ltd.
Spent Resin
Mfg of Prod.
Sch - 1 35.2
2.0 KL 5 KL 7 KL
Collection, Storage, sent to manufacturer /authorized regenerator
Spent Catalyst
Mfg of Prod2 & 4
Sch - 1 28.2
33.0 MT 72 MT 105 MT
Collection, Storage, Transportation to Registered Recycler
Discarded Containers
Raw Material Storage & Handling
Sch - 1 33.1
1120 Nos.
2100 Nos. 3220 Nos.
Collection, Storage, Décontamination, reuse/sell Bags/
Liners Sch-1 33.1
10 Nos. 25 Nos. 35
Nos.
Spent Oil/ Used Oil
Plant & Machineries
Sch - 1 5.1
0.10 KL 0.20KL 0.30 KL
Collection, Storage, Transportation, Disposal by selling to Registered Rerefiners OR Reused as Lubricant within premises
ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.
Unit has obtained membership from BEIL for disposal of hazardous waste from existing plant. Unit will obtain permission for disposal of additional hazardous waste generated from GPCB approved CHWIF/TSDF.
iii Details of Non-Hazardous waste & its disposal (MSW and others)
Not applicable
G Solvent management, VOC emissions etc
i Types of solvents, Details of Solvent Recovery, % Recovery. Reuse of recovered solvents
Not Applicable
ii VOC emission sources and its mitigation measures
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As mentioned in section E (iii) above
• During the meeting dated 03/10/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for expansion of existing unit and for now proposes a new synthetic organic chemical
product. This unit is having valid EC and CC&A for existing unit. Copy of EC and CC&A, its
compliance report is submitted. PP ensured that there are no court cases pending and no public
complaints against the project.
• Total water consumption will be 4,750 KLD. Total wastewater generation will be 3,760 KLD. Waste
water will be treated in full fledged primary, secondary and Tertiary ETP units and RO plant and
MEE. After full-fledged treatment, 760 KLD will be reused back in process while 3000 KLD will be
discharged into GIDC underground drainage.
• Unit have applied for additional quantity of discharge of effluent.
• Coal/Lignite will be used as fuel for proposed steam boilers.
• Adequate APCM will be provided with boilers.
• Adequate APCM will be provided with absorption SO2 tower plant.
• Hazardous waste management will be as per the HW Rules 2016.
Discussions & Conclusion:
• Committee deliberated on area adequacy, waste water management etc. It is noted that PP indents
to discharge 3000 KLPD treated waste water. Referring to the quality of treated waste water, PP was
asked to explore reuse of the treated waste water.
Considering the above project details, after detailed discussion, the terms of reference (ToR) were
prescribed as below and as per the standard TOR for the Synthetic Organic Chemical projects
recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and approved by SEIAA
in its 12th meeting dated 16/09/2017 for the EIA study to be done covering 10 Km radial distance from
the project boundary.
1) To address requirement of additional water considering proposed expansion with details of
process advancement used for existing and proposed product.
2) To explore quality of treated waste water of 3000 KLPD intended for discharge and its reuse with
revised water balance diagram.
3) Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment
Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be
made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities
therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP
report.
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4) Adequacy of proposed area with respect to plant machineries , EMS, Reuse of treated
wastewater, green belt , safety aspect, raw material & product storage considering worst case
scenario. Submit proper lay out plan clearly demarcating all activities with scale.
5) Explore the use of renewable energy to the maximum extent possible. Details of provisions to
make the project energy-efficient through of energy efficient devices and adoption of modes of
alternative eco-friendly sources of energy like solar water heater, solar lighting etc. Measures
proposed for energy conservation.
6) Details of the treatability and feasibility of waste water to be disposed off by means of MEE and
its impact on Environment and Human Health. Submit Adequacy of MEE alongwith quantity of
MEE condensate generation and evaporation of waste water in MEE.
7) Submit certificate regarding additional discharge of waste water into GIDC underground drainage
leading to NCTL.
8) Submit EC order compliance verification report from RO-Ankleshwar for existing plant.
• The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model
ToRs available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical
Industry’ shall be considered as generic TORs,for preparation of the EIA report in addition to all the
relevant information as per the generic structure of EIA given in Appendix III in the EIA Notification,
2006.
• The project proponent shall have to apply for Environmental clearance through online portal
http://environmentclearance.nic.in/ along with final EIA report.
13. SIA/GJ/IND2/28110/2018 M/s. Kenrik Polymers Pvt. Ltd. Survey No: 160, Village: Rayaniya, Tehsil: Talod, Dist.: Sabarkantha
Screening & Scoping
Project Proponent could not attend the meeting. Committee decided to defer the proposal in one of
the upcoming SEAC meeting.
14. SIA/GJ/IND2/28501/2018 M/s. Pravin Industries Plot No: C1-6118, Phase IV, Notified Industrial Area, GIDC-Vapi, 396195, Tal.: Pardi, Dist.: Valsad (Gujarat)
Screening & Scoping
Project / Activity No.: 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no.
SIA/GJ/IND2/28501/2018 dated 10/08/2018 regarding grant of Terms of Reference [ToR] for
preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is a expansion unit proposes for Synthetic Organic Chemicals manufacturing plant as
tabulated below:
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Sr.No. Product CAS No. Capacity, TPM
Existing Proposed Total
1.1 Direct Scarlet 4 BS 3441-14-3 8.0 0
8.0
1.2 Direct Red 12 B 5001-72-9
1.3 Acid Scarlet MOO 5413-75-2
1.4 Basic Bismarck Brown 8005-77-4
1.5 Chroysidine 4438-16-8
1.6 Acid Orange-II 633-96-5
1.7 Basic Auramine-O (Basic Yellow-2)
2465-27-2 17.0 25.0
2.0 Methyl Violet Liquid OR
Malachite Green Liquid OR
Diamond Green Liquid OR
Victoria Blue Liquid OR
Auramine Liquid
8004-87-3
569-64-2
18015-76-4
2580-56-5
492-80-8
0 25.0 25.0
3.0 Methyl Violet Crystal (Crude)
OR Malachite Green Crystal
(Crude) OR
Diamond Green Crystal (Crude)
OR Victoria Blue Crystal (Crude)
OR Auramine-OF (Solvent
Yellow-34)
8004-87-3
569-64-2
18015-76-4
2580-56-5
492-80-8
0 25.0
25.0
Total 8.0 67.0 75.0
• The project falls under Category B of project activity 5(f) as per the schedule of EIA
Notification 2006.
• PP was called for presentation in the SEAC meeting dated 3/10/2018.
• The project proponent along with their expert / consultant M/s. Eco Chem Sales & Services,
Surat attended the meeting and made presentation before the committee
• Salient features of the project are as under:
Sr.no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores):
Existing: 112.33 Lakhs Proposed: 51.50 Lakhs Total: 163.83 Lakhs
(1) Capital cost for EMS (Environmental Management System): 10.00 Lakhs (2) Recurring cost towards the environmental protection measures: 17.25 Lakhs per Annum.
B Total Plot Area ( sq. meter)
Existing: 806.00 sq. meter Proposed: 0.00 sq. meter (development on open land of existing plant) Total: 806.00 sq. meter
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Green belt Area,/Tree Plantation Area ( sq. meter)
Existing: 150 sq. meter Proposed: 00 sq. meter Total: 150 sq. meter
C Employment Generation:
1. Direct Existing: 10 Nos. Proposed: 10 Nos. Total: 20 Nos.
2. Indirect Existing: 4 - 7 Nos. Proposed: 5 - 9 Nos. Total: 9 - 15 Nos.
D Water:
i
Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc.)
GIDC, Vapi Water Supply
Status of permission from the concern authority Water Permission Letter Vide Letter No.: GIDC/DEE/(W/S)/NA/VAPI/1582 dated 18/07/2018.
ii Water consumption (KLD):
# Particulars
Water Consumption, KLD
Existing Proposed Total
A. Domestic 2.0 0 2.0
B. Industrial
1. Processing, Washing & Scrubber 8.0 21.58 29.58
2. Boiler 1.0 2.0 3.0
3. Cooling 2.0 1.0 3.0
4. Floor/Container Washing 1.0 0.5 1.5
Total Industrial 12.0 25.08 37.08
C. Gardening 1.0 0 1.0
Grand Total (A+B+C) 15.0 25.08 40.08
D. Recycle as MEE Condensate 0 26.46 26.46
Net Fresh Water (A+B+C-D) 15.0 -1.38 13.62
1) Total water requirement for the project: 40.08 KLD 2) Quantity to be recycle: 26.46 KLD 3) Total fresh water requirement: 13.62 KLD
iii Wastewater generation (KLD):
# Particulars
Effluent Generation, KLD
Existing Proposed Total
A. Domestic 1.8 00 1.80
B. Industrial
1. Processing, Washing & Scrubber 8.00 25.66 33.66
2. Boiler 0.00 0.50 0.50
3. Cooling 0.00 0.50 0.50
4. Floor/container washing 1.00 0.50 1.50
Total Industrial 9.00 27.16 36.16
C. Gardening 0.00 00 00
Grand Total (A+B+C) 10.80 27.16 37.96
Septic Tank/Soak Pit 1.80 00 1.80
To CETP 9.00 00 9.00
To MEE/Centrifuge 00 27.16 27.16
iv Treatment facility within premises with capacity (ETP, MEE, STP etc.)
ETP: 10 KLD MEE: 30 KLD
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v Mode of Disposal & Final meeting point Domestic Effluent: Domestic waste water (1.80 KLD) is being/will be passed through Septic Tank.
Industrial Effluent: Total Industrial Waste Water Generation will be 36.16 KLD, 27.16 KLD process effluents will be treated in proposed MEE Plant and 9.00 KLD will be treated in existing primary, & tertiary effluent treatment plant and finally treated effluent will be disposed off into CETP Vapi for further treatment and disposal into Arabian Sea.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , name of CF
CETP, Vapi.
Membership of Common facility (CF) CETP Membership Certificate Vide Letter No.: REF:CETP_Member.Certi/150/18282 dated:01/12/2012
vii Reuse/Recycle details (KLD) 26.46 KLD of MEE Condensate will be reused.
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.
Existing: There is no flue gas as well as process gas emission from existing plant. Unit is not used any D.G. set also, hence no emission from D. G. set is expected.
#
Source of Emission
With Capacity e.g. Boiler (8 TPH)
Stack Height (meter)
Name of the Fuel
Quantity of Fuel MT/h & MT/Day
Type of emissions
i.e. Air Pollutants
APCM Emission Standard
EXISTING
1. Steam Boiler (300 kgs/hr)
11
Natural Gas
20 SCM/hr
PM SOx NOx
Adequate Stack Height
<PM: 150 mg/Nm3,
<SOx:100 ppm <NOx: 50 ppm
2. Thermopack
(2 Lacs K Cal) 11 20 SCM/hr
3. Hot Air Generator
(4 Lacs K Cal) -- 50 SCM/hr
PROPOSED
1. Steam Boiler (600 kgs/hr)
11 Natural
Gas 60 SCM/hr PM
SOx NOx
Adequate Stack Height
<PM: 150 mg/Nm3,
<SOx:100 ppm <NOx: 50 ppm
2. DG Set
(82.5 KVA) 11 HSD 15 Lit/hr
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) [Existing & Proposed]
# Particulars
Details
Remarks Existing
After proposed Expansion
1.0 Stack attached to Reactor Reactor
Existing will be Modified
APC Provided Three Stage Alkali
followed by Water and Acid Scrubber
Three Stage Alkali followed by Water and
Acid Scrubber
Height of Vent 11 meters 11 meters
Expected Emission NH3: <175 mg/Nm3
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H2S : < 10 mg/Nm3
2.0 Stack attached to Spin Flash dryer Spin Flash dryer
Existing
APC Provided Cyclone Separator
followed by Bag Filter Cyclone Separator
followed by Bag Filter
Height of Vent 11 meters 11 meters
Expected Emission PM: <150 mg/Nm3
iii Fugitive emission details with its mitigation measures. [Existing & Proposed]..As below
• Concrete road is already developed within plot premises to avoid fugitive dust due to vehicle movement.
• Manufacturing activity is/will be carried out in closed reactors/vessels and
• Regular checking and maintenance of the same is/will be carried out to avoid any leakages. All the raw materials are/will be stored in closed containers and in sealed bags and will be handled through closed system to avoid the handling losses.
F Hazardous Waste: (As per the Hazardous and Other Wastes (Management and Trans boundary Movement) Rules 2016. [Existing & Proposed]
i
Quantity of discarded containers must be in MT/Annum.
# Type Quantity, TPA
Disposal Existing Proposed Total
1. Process Residue (Auramine Sludge)
(Sch: I/26.1) 18.00 391.57 409.57
Sell to actual/authorized users or Dispose off into TSDF, Vapi
2 Process Residue
(Sch: I/26.1) 0.00 199.90 199.90
Dispose off into TSDF, Vapi
3. ETP Waste/MEE Salt
(Sch:I/35.3) 1.80 194.8 196.60
Dispose off into TSDF, Vapi
4. Used Oil
(Sch: I/5.1) 0.01 0.01 0.02
Collection, storage & sell to register recycler
5. Discarded Containers
(Sch:I/33.1) 2.00 1.00 3.00
Collection, storage & sell to register recycler
6. Sludge from Wet Scrubber
(Sch:I/37.1) 0.00 1.00 1.00
Dispose off into ETP along with scrubbing water
ii Membership details of TSDF, CHWIF etc.
VWEMCL certificate for CETP for acceptance of additional effluent vide letter No. CETP_Member.Certi/150/18282 dated: 01/12/2012 & Common Solid waste disposal membership No. 87 dated 01/12/2012
iii Details of Non-Hazardous waste & its disposal (MSW and others)
Nil
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. Reuse of recovered Solvents.
No Solvents are being/will be used
ii VOC emission sources and its mitigation measures NIL
• During the meeting dated 03/10/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
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Observation:
• This proposal is for expansion of unit proposes for a synthetic organic chemical product.
• The project falls under the activity 5(f) as per the schedule of EIA Notification 2006.
• Total Water consumption will be 40.08 KLD. Total Waste Water generation 36.16 KLD from
manufacturing activity and other ancillary operation in which 27.16 KLD process effluent will
be treated in proposed MEE Plant and 9.00 KLD will be treated in existing primary, & tertiary
effluent treatment plant and finally treated effluent will be disposed off into CETP Vapi for
further treatment and disposal into Arabian sea.
• Natural gas will be used as fuel for proposed boiler, thermopack and hot air generator.
• Separate Adequate APCM will be provided to control process gas emission with existing and
proposed reactor.
Discussions & Conclusion:
• As the proposal is for expansion, compliance of action taken by the GPCB was deliberated. It
is noted that three subsequent show cause notices have been issued to the unit which was
not satisfactorily addressed by the PP. Committee felt a latest status on compliance of CCA
conditions verified by the GPCB. It is further noted that plot area is 806 M2 and unit is
intending to expand from 8 MTPM to 75 MTPM with provision of green belt. Hence PP was
asked to submit area adequacy in context to storage of the raw materials, erection of new
equipments, area for storage of finished goods etc. for the existing and proposed products
with proposed green belt. Detailed water consumption and waste water generation was
deliberated and Committee asked PP to readdress water balance with detailed treatability and
adequacy of treated waste water management.
• Committee also deliberated on hazardous waste management, process gas emission, Safety
aspects etc.
After detailed discussion, it was decided to ask project proponent to submit the following details and
upon receipt of the same, it was decided to consider the proposal in one of the upcoming SEAC
meeting.
1. Certified compliance report of CCA conditions validated by GPCB along with details status of reasons
mentioned in show cause notices issued by GPCB.
2. Area adequacy in context to storage of the raw materials, erection of new equipments, area for
storage of finished goods etc. for the existing and proposed products with proposed green belt.
3. To readdress water balance with detailed water consumption, waste water generation, its treatability
and adequacy of reuse.
15. SIA/GJ/IND2/28513/2018 M/s. Rishabh Dye Chem Industries
Plot No. 223, GIDC Industrial Estate, GIDC Ankleshwar, Dist-Bharuch.
Screening & Scoping
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Project / Activity No.: 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/28513/2018
dated 10/08/2018 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is new unit proposes for Synthetic Organic Chemicals as tabulated below:
Sr. No.
Name of the Products CAS no. Quantity
MT/Month End-use of products
1 2 Amino 2' Methyl Di Phenyl Crysyl Ether
3840-18-4
36.00
In Dyes Intermediates & Pharmaceuticals Industry
2 2,4 Di-Chlro O-Amino Di Phenyl Ether
26306-64-9 In Dyes Intermediates & Pharmaceuticals Industry
3 2 Amino 4 Chloro Diphenyl Ether
93-67-4 In Dyes Intermediates & Pharmaceuticals Industry
4 Amino Resorcinol Di O Crysyl Ether
73637-04-4 In Dyes Intermediates & Pharmaceuticals Industry
5 Ortho Amino Di Phenyl Ether
2688-84-8 In Dyes Intermediates & Pharmaceuticals Industry
6 Pera Amino Di Phenyl Ether 139-59-3 In Dyes Intermediates & Pharmaceuticals Industry
7 2 Amino 4 Chloro 2'4' Di Chloro Di Phenyl Ether
56966-52-0 In Dyes Intermediates & Pharmaceuticals Industry
8 4,4' Di Chloro 2 Amino Di Phenyl Ether
121-27-7 In Dyes Intermediates & Pharmaceuticals Industry
• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification
2006.
• PP was called for presentation in the SEAC meeting dated 03/10/2018.
• The project proponent along with their expert /consultant M/s. Earthcare Enviro Solutions Pvt.
Ltd.,Surat attended the meeting and made presentation before the committee
• Salient features of the project are as under:
Sr. no.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores): Rs. 3.16 Crores
B Total Plot area ( sq. meter) 704.00 Sq. m.
Green belt area,/Tree Plantation area (sq. meter)
70.00 Sq. m.
C Employment generation Male: 21 + Female: 02 = 23
D Water
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i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
GIDC, Ankleshwar
Status of permission from the concern authority.
Unit has got permission from GIDC for water supply.
ii Water consumption (KLD)
Category KLD
(A) Domestic 1.00
(B) Gardening 0.28
(C) Industrial
Process 3.00
Washing 1.50
Boiler 22.00
Cooling 2.50
Others --
Industrial Total 29.00
Total (A + B + C) 30.28
1) Total water requirement for the project: 30.28 KLD
2) Quantity to be recycle: Nil
3) Total fresh water requirement: 30.28 KLD
iii Waste water generation (KLD)
Category Waste water
KLD
(A) Domestic 0.80
(B) Industrial
Process --
Washing 1.20
Boiler 1.00
Cooling 0.10
Others --
Total Industrial waste water
2.30
Total [A + B] 3.10
iv
Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
In-house ETP (Capacity: 5.0 KLD) having primary treatment will be installed.
v Mode of Disposal & Final meeting point
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Domestic: Domestic effluent shall be disposed in to Septic tank / Soak pit system.
Industrial:
There shall be no any process wastewater generation from manufacturing process activity. Wastewater generated from other ancillary industrial operations shall be allowed into in-house ETP for primary treatment. Primary treated water will be sent to the Common MEE facility of M/s. BEIL.
vi
In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc., Name of CF
Common MEE Facility: M/s. BEIL, Ankleshwar.
Membership of Common facility (CF)
Unit has got NOC from M/s. BEIL.
vii Reuse/Recycle details (KLD)
--
E Air
i
Flue gas emission details
No. of Boilers / TFH / Furnaces / DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
Sr. no.
Source of emission
With Capacity
Stack
Height (meter)
Type of
Fuel
Quantity of Fuel
MT/Day
Type of emissions
i.e. Air Pollutants
Air Pollution Control Measures
(APCM)
1 Steam Boiler
(Capacity: 1 TPH) 12.00 m
Natural Gas
400.00 m3/day
PM
SO2
NOx
Adequate stack height will be provided
2
Thermic Fluid Heater (2 Nos.) (Capacity: 2 Lac Kcal/hr each)
12.00 m Natural
Gas 300.00 m3/day
3
D. G Set
(Stand By)
(Capacity: 300 KVA)
6.00 m HSD 81.00
Lit/hr
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Not Applicable
iii Fugitive emission details with its mitigation measures.
As below:
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• Sources of fugitive emissions will be from raw material storage area, handling of chemicals,
manufacturing process and from vehicle movement on internal road.
• To minimize fugitive emission, powder material will be allowed in a vessel through closed loop
while liquid material will be charged through pipeline.
• Transportation of raw materials & products will be carried out by trolley within premises and
minimum manual material handling will be carried, so the fugitive emission due to process
activity and material handling will be minimized.
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
(MT/Annum) Disposal Method
1. ETP Sludge Effluent
Treatment Plant
35.3 (Sch-I)
2.00 MT/year
Collection, Storage,
Transportation and Disposal at
TSDF site – for secured landfill
2. Used Oil D. G Set &
Thermopack 5.1
(Sch-I) 0.25
MT/year
Collection, Storage,
Transportation and Disposal by
selling to Registered Re-refiners
approved by GPCB / CPCB OR
reuse for lubrication
3. Discarded Containers / Bags / Liners
Raw material & Finished
product packing material
33.1 (Sch-I)
75 MT/year
Collection, Storage,
Transportation and Disposal by
selling to registered recycler
approved by GPCB / CPCB OR
reuse within premises.
4. Distillation Residue
Process (All products)
20.3 (Sch-I)
98.18 MT/year
Collection, Storage,
Transportation and Disposal for
co-processing/incineration
5. Inorganic
Salt Process
(All products) 28.1
(Sch-I)
375.27
MT/Year
Collection, Storage,
Transportation and Disposal at
TSDF site for secured landfill
6. Iron Sludge Process
(All products) 28.1
(Sch-I)
218.16
MT/Year
Collection, Storage,
Transportation and Disposal at
TSDF site for secured landfill
7.
Sodium
Acetate/
Potassium
Acetate
Process (All products)
28.4 (Sch-I)
728.73
MT/Year
Collection, Storage,
Transportation & Disposal by
selling to Authorized end user
as per Haz. Waste Rule-9 and
after getting prior permission
from GPCB.
ii Membership details of TSDF, CHWIF etc. Unit has got NOC from M/s. BEIL for receiving Landfilling waste and Incinerable waste.
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iii Details of Non-Hazardous waste & its disposal
(MSW and others)
Sr. No.
Type of Waste Source of
Generation Category of Waste
Disposal
1. Domestic Waste
(Food waste, Plastic, Paper etc.)
Employees working in the
premises MSW
Collected in separate bin and disposed to bin of GIDC.
2. Industrial Waste
(Glass wool [Insulating Material, Scrap])
Steam Pipe & Vessels
ISW Sell to local scrap vendor
3. Industrial Waste (Wooden pellets)
From Raw Material & Product
storage area ISW
Sell to local scrap vender
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
Not Applicable
ii
VOC emission sources and its mitigation measures
• VOCs generation will be from storage and usage of raw materials.
• VOC analysers will be provided to detect any solvent leakages during storage and handling.
• During the meeting dated 03/10/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for a new synthetic organic chemical product.
• Total water consumption will be 30.28 KLD. Total wastewater generation will be 2.30 KLD.
Wastewater generated from other ancillary industrial operations shall be allowed into in-house
ETP for primary treatment. Primary treated water will be sent to the Common MEE facility of M/s.
BEIL
• Natural gas will be used as fuel for boiler after expansion.
• There will be no process gas emission.
• Hazardous waste management will be as per the HW Rules 2016.
Discussions & Conclusion:
Committee deliberated on the all the eight products with proposed manufacturing quantity of 36 MTPM and
asked PP to address worst case scenario based on pollution potential with subsequently break up of
individual production quantity for all the products. It is also noted that there is no process wastewater
generation from manufacturing process activity. Wastewater generated from other ancillary industrial
operations will be sent to ETP for primary treatment. Primary treated water will be sent to the Common MEE
facility of M/s. BEIL. Committee deliberated on area adequacy, waste water management, and safety
aspects of the raw material storage , process operations etc.
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After detailed discussion, it was decided to ask project proponent to submit the following details and
upon receipt of the same, it was decided to consider the proposal in one of the upcoming SEAC
meeting.
1. Adequacy of hazardous waste storage facility proposed/available based on quantum of
hazardous waste generation.
2. To submit break up of individual product with its proposed production.
Meeting ended with thanks to the Chair and the Members.
Minutes approved by:
1. Dr. Dinesh Misra, Chairman, SEAC 2. Shri S. C. Srivastav, Vice Chairman, SEAC
3. Dr. V. K. Jain, Member, SEAC
4. Shri. R. J. Shah, Member, SEAC
5. Shri Rajesh I Shah, Member, SEAC
6. Shri A. K. Muley, Member, SEAC