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454th meeting of SEAC-Gujarat, Dated 28.11.2018
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Minutes of the 454thmeeting of the StateLevelExpertAppraisalCommittee held on
28/11/2018 at Committee Room, GEER foundation, Gandhinagar
The 454thmeeting of the StateLevel ExpertAppraisalCommittee (SEAC) was held on 28th
November 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. Shri V. N. Patel, Member, SEAC
4. Shri R. J. Shah, Member, SEAC
5. Shri A.K. Muley, Member, SEAC
The agenda of TOR/Scopingcases and Appraisal was taken up. The applicants made
presentations on the activities to be carried out along with other details furnished in the Form-1,
PFR, EIA-EMP reports and other reports.
1 SIA/GJ/IND2/26041/2017 M/s Lycos Chemtech
Plot. No. 1032/3, GIDC, Panoli-394 116, Tal:
Ankleshwar, Dist. Bharuch, Gujarat
Appraisal
Project / Activity No.5(f) Project status: New
• PP has submitted online application vide no. SIA/GJ/IND2/26041/2017 dated 27/09/2018 for
obtaining Environmental Clearance.
• SEAC has recommended the project to SEIAA and SEIAA has issued TOR to PP vide letter J-
11011/208/2017-IA.II vide dated 10th-July-2017.
• Project proponent has submitted EIA Report prepared by Aqua – Air Environmental
Engineers Pvt. Ltd based on the TOR issued by SEIAA.
• This is a new engaged in synthetic organic chemicals and now proposes as tabulated below:
Sr. No.
Name of the Products CAS no. / CI no.
Quantity MT/Month
End-use of products
1 Diethylcarbamazine Citrate 1642-54-2
15
Treatment of filariasis
2 1-[2‐(2‐Hydroxyethyl) Ethoxy] Piperazine (99%)
13349-82-1 Pharmaceutical Intermediate
3 1-(2, 3‐Dichlorophenyl) Piperazine HCl
119532-26-2 Pharmaceutical Intermediate
4 1-Benzylpiperazine (99%) 2759-28-6 Pharmaceutical Intermediate
5 1-(2-Methoxyphenyl) Piperazine HCl (98%)
5464-78-8 Pharmaceutical Intermediate
6 PiperazineHexahydrate 142-63-2 Anthelmintic
7 Piperazine Citrate 144-29-6 Anthelmintic
8 PiperazineAdipate 142-88-1 Anthelmintic
9 PiperazineDihydrochloride 142-64-3 Anthelmintic
10 Piperazine Phosphate 14538-56-8 Anthelmintic
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11 Povidone Iodine 25655-41-8 Treatment of skin infection on
the skin
12 N-Phenyl Piperazine (NPP) 92-54-6 Pharmaceutical Intermediate
13 N-Methyl Piperazine 109-01-3 Pharmaceutical Intermediate
14 1-Amino-4-Methyl Piperazine 6928-85-4 Pharmaceutical Intermediate
15 1- BOCPiperazine 57260-71-6 Pharmaceutical Intermediate
16 Sodium Barbital 144-02-5 Pharmaceutical Intermediate
17 Methoxsalen 298-81-7 Pharmaceutical Intermediate
18 5-Methyl Nicotinic Acid 3222-49-9 Pharmaceutical Intermediate
19 Ciprofloxacin Lactate 97867-33-9 Antibiotic
20 Ciprofloxacin Base 86483-48-9 Antibiotic
21 Mecobalamin 13422-55-4 0.5 Dietary Supplement
Total 15.5
• 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 28/11/2018.
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores): 2 Crores
B Total Plot area( sq. meter) 1040 Sq. m.
Green belt area ( sq. meter) 300 Sq. m.
C Employment generation 8
D Water
i
Source of Water Supply(GIDC Bore well,
Surface water, Tanker supply etc...)
GIDC Water Supply
Status of permission from the concern authority. Unit has obtained permission from GIDC
for water supplyvide letter no
NO/GIDC/DEE/PNL/1498 dated
01/04/2017.
ii Water consumption (KLD)
Category
Quantity
KLD
Remarks
(A) Domestic 2.7
(B) Gardening 0.8
(C) Industrial
Process 2.86
Washing 0.4
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Boiler 6.0
Cooling 5.0
Others Nil
Industrial Total 14.26
Total (A + B + C) 17.76
1) Total water requirement for the project: 17.76 KLD
2) Quantity to be recycled: 0 KLD
3) Total fresh water requirement: 17.76 KLD
iii Waste water generation (KLD)
Category Waste water
KLD
Remarks
(A) Domestic 2.7
(B) Industrial
Process 1.73
Washing 0.4
Boiler 0.6
Cooling 0.5
Others Nil
Total Industrial
waste water
3.23
Total [A + B] 5.93
-
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
M/s. Lycos Chemtech proposes Effluent Treatment Plant (ETP) to be contained Primary and Tertiary Treatment Facilities. Treated effluent will be sent to Common MEE of M/s. Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwar for further treatment and disposal. Details of ETP are as follows. First all non-toxic and biodegradable streams of wastewater shall pass through Oil & Grease Trap (OGT-01) where floating oil, grease and other floating material shall be manually removed from top and collected in O & G Collection Tank(OGCT-01). Thereafter effluent shall be collected in Equalization cum Neutralization Tank (ENT-01) where the continuous addition and stirring of Lime solution is done to maintain neutral pH of wastewater from Lime Dosing Tank (LDT-01) as per requirement by gravity. Pipe grid will be provided at bottom of the ENT-01 to keep all suspended solids in suspension and to provide proper mixing by air supplied through air blowers (B-01). Thereafter, neutralized wastewater shall be pumped to Flash Mixer (FM-01). Alum and Polyelectrolyte shall be dosed from Alum Dosing Tank (ADT-01) and Polyelectrolyte Dosing Tank (PEDT-1) respectively by gravity into FM-01 to carry out coagulation by using a Flash
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Mixer. Thereafter, coagulated wastewater shall be settled in Primary Settling tank (PST-01). Clear supernatant from PST-01 shall be collected in Intermediate Sump(IS-01). Treated effluent from IS-01 then passed through Dual Media Filter (DMF-01) to remove remaining SS from effluent. Then clear water shall be collected in treated effluent Sump (TES-01) before sent toCommon MEE of M/s. Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwarfor further treatment and disposal. Sludge settled in PST-01 shall be sent to Sludge Drying Beds (SDBs-A/B) where, dewatering shall be carried out before storage in HWSA and ultimate disposal to TSDF. Leachate from SDBs-A/B shall be pumped back to ENT-01 for further treatment.
v Mode of Disposal & Final meeting point
Domestic:
2.7 KL/Day domestic wastewater will be disposed through Septic Tank/Soak
Pit.
Industrial:
3.23 KL/Day Industrial waste water will be sent to Common MEE of M/s.
Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwar for
further treatment and disposal after treatment in ETP within premises.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. ,
Name of CF
CMEE membership of M/s. ACPTCL, Ankleshwar
Membership of Common facility (CF)
(For waste water treatment)
Unit has obtained membership of CMEE membership of M/s. ACPTCL, Ankleshwar dated
22/01/2018 vide letter no. ACPTCL/1300000169/2017-18/138
vii Simplified water balance diagram with reuse / recycle of waste water
Total Water Requirement
17.76
Process
2.86
Boiler
6.0
Cooling
5.0
Gardeni
ng
0.8
Domestic
2.7
Domestic
wastewate
r: 2.7�
Septic
Tank/Soak
ProcessW/W
1.73
Boiler
W/W
Cooling
W/W
0.5
ETP
(Primary Treatment)
Common MEE of M/s. ACPTCL, Ankleshwar
(For further Treatment & Final Disposal)
3.23
Washing
0.4
Washing
W/W
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viii Reuse/Recycle details (KLD)
Total reuse 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 Boiler-I (1 TPH)
12 Agro Wast
e
1250 Kg/Day
SPM SO2 NOx
Multicyclone Separator with bag
filter
2 Thermic Fluid
Heater (1 Lac KL/hr.)
12 Agro Wast
e
500 Kg/Day
SPM SO2 NOx
3 D.G. Set* (125 KVA)
5
Diesel
25 Liter/hr.
SPM SO2 NOx
Adequate stack height
--* To be used in emergency only.
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
- No process gas emissions from the proposed project.
iii Fugitive emission details with its mitigation measures.
As below:
Following measures will be adopted to prevent and control fugitive emissions?
1. Airborne dust at all transfers operations/ points will be controlled either by spraying
water or providing enclosures.
2. Raw materials loading and unloading will be done in covered area
3. Care will be taken to store construction material properly to prevent fugitive
emissions, if any.
4. Regular maintenance of valves, pumps, flanges, joints and other equipment will be
done to prevent leakages and thus minimizing the fugitive emissions of VOCs.
5. Entire process will be carried out in the closed reactors with proper maintenance of
pressure and temperature.
6. Periodic monitoring of work area will be carried out to check the fugitive emission.
7. Breather valves will be provided on solvent tanks.
8. To eliminate chances of leakages from glands of pumps, mechanical seal will be
provided at all solvent pumps.
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9. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank
vents will be connected to vent chillers.
10. Minimum number of flanges, joints and valves in pipelines.
11. Enclosures to chemical storage area, collection of emission from loading of raw
materials in particular solvents through hoods and ducts by induced draft, and
control by scrubber / dust collector to be ensured.
12. Adequate ventilation will be provided.
13. Periodic monitoring of work area will be carried out to check the fugitive emission
as per the norms of Gujarat Factory Rules.
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.
Quantit
y
(MT/An
num)
Management of HW
1 ETP Sludge ETP Sch-I/ 35.3
48
Collection, Storage, Transportation and sent to common TSDF site of M/s. BEIL, Ankleshwar for disposal.
2 Process Waste
Process (5-
Methyl Nicotinic
Acid)
Sch-I/ 28.1
60
Collection, Storage, Transportation and sent to common TSDF siteof M/s. BEIL, Ankleshwar for disposal.
3 Used Oil Equipment and
Machinery
Sch-I/ 5.1
3.6
Collection, Storage, Transportation and sell to GPCB registered reprocessor/refiner
4 Discarded Drums/ Bags
Raw Material &
Storage
Sch-I/ 33.1
2.7
Collection, Storage, Decontamination, Transportation & given to GPCB authorized Vendor
5 Distillation Residue
Distillation Unit Sch-I/ 20.3
32.4
Collection, Storage, Transportation and sent for co-processing in cement industries or to CHWIFof M/s. BEIL, Ankleshwar.
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6 Manganese
Dioxide
Process (5-
Methyl Nicotinic
Acid)
Sch-I/ 28.1
11
Collection, Storage and sell to end user/s having permission under rule-9.
7 Ammonium
Chloride Process(Ciproflo
xacin Base)
Sch-I/ 28.1
9
8 Zinc
Hydroxide
Process (1-Amino-4-
Methyl Piperazine)
Sch-II/ B-32
550
9 N-Methyl
Piperazine
Process (1-Amino-4-
Methyl Piperazine)
Sch-I/ 28.1
28
10 Sodium Chloride solution
Process (1-(2-Methoxyphenyl) Piperazine HCl
(98%))
Sch-I/ 28.1
600
Collection, Storage, and sent to ETP.
11 Spent Solvent Process Sch-I/ 28.6
600 Collection, Storage, Distillation and Reuse within premises.
-
ii Membership details of TSDF, CHWIF etc.
(For HW management)
Company has membership of TSDF of
M/s. BEIL dated 11/02/2017.
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
No such waste will be generated.
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
Name of Solvent
Boiling
Point (°C)
Vapor Pressure (kPa@20
0C)
Total Solvent
Input Kg
Qty of Solvent
Recycled Kg
Qty of Losses
Kg
% Recove
ry
% Los
s
Toluene 110.6 3.8 kPa @ 250C
10500 9950 550 94.76 5.24
o-Xylene 144.4 0.9 10000 9600 400 96 4
Acetone 56.2 24 20000 18700 1300 93.5 6.5
IPA 82.5 4.4 5000 4750 250 95 5
Methanol 64.5 12.3 20000 18650 1350 93.25 6.75
Ethanol 78.5 5.7 10000 9700 300 97 3
ii VOC emission sources and its mitigation measures
During operation stage, leakage through valves/pumps, leakage and emission from open drum containing chemicals, open feeding, storage tanks, etc. will be major sources of fugitive emissions and VOCs. Excess use of solvent/s may also results fugitive emission from the process vessels.
• Solid raw material charging will be done through closed system.
• Entire process will be carried out in the closed reactors with proper maintenance of
pressure and temperature.
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• Emphasis will be given to solvent management/solvent loss prevention.
• Control by having proper scrubbing system.
• Condenser to trap VOC.
• Proper maintenance schedule will be adhered to avoid emissions through flange joints,
pump seals etc.
• Minimum number of flanges, joints and valves in pipelines.
• Proper gland packing will be maintained for pumps and valves and to the extent possible
pumps with mechanical seal.
• A regular preventive maintenance schedule will be in place to replace or rectify all
gaskets and joints etc. as a part of ISO systems to ensure no fugitive emissions take
place.
• Periodic monitoring of work area will be carried out to check the fugitive emission.
• Solvent tank vents will be connected to vent chillers.
• Adequate ventilation will be provided.
• Airborne dust at all transfers operations/ points will be controlled either by spraying water
or providing enclosures.
• Breather valves will be provided on solvent tanks.
• During the meeting dated 28/11/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for new synthetic organic chemical products.
• Total water consumption will be 17.76 KLD. Total wastewater generation will be 3.23 KLD. 3.23 KL/Day Industrial waste water will be sent to Common MEE of M/s. Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwar for further treatment and disposal after primary and tertiary treatment in ETP within premises.
• Agrowastewill be used as fuel in boiler.
• Adequate APCM like MCS and Bag filter will be provided for proposed boiler.
• There shall be no process gas emission from process.
• 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 March to May, 2017. Ambient Air Quality monitoring was carried out
for PM10, PM2.5, SO2, NOx, NH3, CO and VOC etc at ten locations including the project site.
Values conform to the prescribed standards for Ambient Air Quality. The incremental Ground
Level Concentration (GLC) has been computed using ISCST3 Model. The resultant
concentrations are within the NAAQS. The PM10values at all the locations in residential/rural
areas ranged between 72.54 – 95.94 µg/m3 respectively in pre-monsoon season. Similarly,
the values of PM2.5 varied in the range of 42.61 – 51.28 µg/m3. The PM10 and PM2.5
concentrations at all the AAQM locations were primarily caused by local phenomena including
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vehicular activities and natural dust getting air borne due to manmade activities and blowing
wind.. 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.
• Committee deliberated on waste water management, area adequacy, BAT, Baseline study,
green belt development, environmental policy, SOP for safety aspects etc.
• There is no waste water generation from the products at sr. no. 1, 2 & 3. Entire quantity of
waste water will be sent to M/s: ACPTCL, Ankleshwar.
• Committee suggested to plant local trees with broad leaf and good canopy for green belt
development.
• Compliance of the ToR was found satisfactory.
After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant
of Environmental Clearance.
2. SIA/GJ/IND2/19767/2017 M/s Greeva Plot No. C-1/5513-5514, Phase III, GIDC-Vatva, Taluka Ahmedabad, District Ahmedabad, Gujarat
Appraisal
Project / Activity No.: 5(f)
Project status: Expansion
• PP has submitted online application vide no. SIA/GJ/IND2/19767/2017for obtaining
Environmental Clearance.
• SEIAA has issued TOR to PP vide letter : SEIAA/GUJ/TOR/5(f)/876/2017 vide dated 28th
September, 2017
• Project proponent has submitted EIA Report prepared by Kadam Environmental
Consultants, Vadodara based on the TOR issued by MoEF& CC.
• This is an expansion unit and proposes for expansion of Synthetic Organic Chemicals
manufacturing plant as tabulated below:
Sr.
no. Name of the Products
CAS
no.
Quantity (MT/Month) End-use of
product Existing Proposed Total
1 Textile Auxiliary Chemical (Blending & Mixing)
- 2000 0 2000 Used in Textile processing
2
Textile Auxiliary Chemical (Synthesis)
Such as;
Washing off Agent, Soaping Agent, Binders, Sizing Agent, Alkali Buffer
Acid Buffer, Bleaching Agent, Loop
- 0 3000 3000 Used in Textile processing
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Accelerator, Peroxide Killer, Lubricant
Carrier, Defoamer, Scroping Agent, Yarn Lubricant, Sequestering Agent, Stain Remover, Wax emulsion, Dyefixer-1
Dyefixer-2, Cationic Softener, Mercerising Agent, Retarding Agent, Wetting Agent – 1, Wetting Agent – 2, Resin, Fatty Ester, Adhesive, Silicon Oil, Bleaching Agent (Powder)
• 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 28/11/2018.
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project
(Rs. in Cr.):
Existing: 1.5 Proposed: 3.10 Total: 4.6
B Total Plot area
( sq. meter)
Existing: 1737 Sq. m.
Proposed: 314 Sq. m.
Total: 2051 Sq. m.
Green belt area,/Tree Plantation area
( sq. meter)
Existing: 225 Sq. m.
Proposed: 84 Sq. m.
Total: 309 Sq. m.
C Employment generation Existing: 23
Proposed: 27
Total: 50
D Water
i
Source of Water Supply (GIDC Bore well,
Surface water, Tanker supply etc...)
Water is sourced from GIDC water
supply i.e. Vatva Industrial Estate
Infrastructure Development Limited
(SPV) of Vatva Industries Association.
Status of permission from the concern authority.
Permission of Vatva Industrial Estate
Infrastructure Development Limited
(SPV) OF Vatva Industrial Association
is given.
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ii Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 1 1 2
(B) Gardening - - -
(C) Industrial
Process 28 40 68
Washing 21 -1 20
Boiler 15 11 26
Cooling 5 4 9
Others - - -
Industrial Total 69 54 123
Grand Total
(A+B+C) 70 55 125
1) Total water requirement for the project: 125 KLD
2) Quantity to be recycle: 0 KLD
3) Total fresh water requirement: 125 KLD
iii Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 0.5 0 0.5 to Soak pit
(B) Industrial
Process 0 0 0 CETP after primary,
secondary&tertiary
treatment
Washing 21 -1 20
Boiler 0.5 0.5 1
Cooling 0.5 0.5 1
Others - - -
Total Industrial
waste water
22 0 22
iv Treatment facility within premises with capacity [For existing and Proposed]
[In-house ETP (Primary, Secondary, Tertiary).
The industrial effluent is treated in ETP of capacity 75 KLD & treated water is going to
CETP for further treatment.
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v Mode of Disposal & Final meeting point
Domestic: To Soak Pit
Industrial:
The industrial effluent is treated in ETP of capacity 75 KLD & treated water
is going to CETP for further treatment.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF
etc.
Name of Common facility:
We are discharging treated effluent to M/s. The Green Environment services Co.-Op. Society Ltd.
Phase-II, GIDC estate, Vatva, Ahmedabad for further treatment.
Membership of Common facility (CF)
Membership Certificate of M/s. The Green Environment Services Co-op. Society Ltd. For
Effluent Treatment.
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.
Existing & Proposed
-
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)
Existing
1 Boiler (1
TPH) 12
Natural Gas from
Adani Pipeline
70 SCM/Hr.
Particulate Matter,
SO2, NOx N/A
Proposed
1 Boiler (2
TPH) 12
Natural Gas from
Adani Pipeline
140 SCM/Hr.
Particulate Matter,
SO2, NOx N/A
2 D.G Set
(250 kVA) 12 Diesel 40 Lit/Hr.
Particulate Matter,
SO2, NOx N/A
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
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Existing & Proposed
There is no Process vent
iii Fugitive emission details with its mitigation measures.
There is no any kind of fugitive emission in present products as well as proposed products.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement)
Rules 2016.
Existing & Proposed
i
Sr.
no.
Type/Name of
Hazardous waste
Source of generation
Category and
Schedule as
per HW Rules.
Quantity (MT/Annum)
Disposal Method
Existing Propose
d Total
1 ETP
Sludge ETP 35.3 60 MT - 60 MT
Packed in HDPE
Bags, and Dispose to
TSDF
2 Used Oil Machinery 5.1 - 0.1 KL 0.1 KL
Disposal by selling to register recycler
3 Discarded
Container/Liners
Production 33.1 120000
Nos./Annum
30000 Nos./Ann
um
150000 Nos./Ann
um
Disposal by selling to registered recycler
-
ii Membership details of TSDF, CHWIF etc.
Membership Certificate of M/s.
SaurastraEnviro Projects Pvt. Ltd. For
Hazardous Waste.
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
List of solvents to be used:
Sr. No. Material description Storage Location Quantity in KL
1. Iso Amyl Alcohol Barrel 200
2 Acrylic Acid Barrel 200
3 Benzyl Chloride Barrel 200
4 Butyl Acrylate Barrel 180
5 Di Methyl Amine Barrel 170
6 Epichlorohydrin Barrel 230
7 Formaldehyde Barrel 230
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8 Formic Acid Barrel 35
9 Iso Propyl Alcohol Barrel 200
10 Styrene Barrel 200
11 Butyl Cello solve Barrel 200
12 Poly Vinyl Alcohol Bags 25 kg
• Solvent recovery system is not feasible as all solvents are going with products.
ii VOC emission sources and its mitigation measures
• -
• During the meeting dated 28/11/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
• This proposal is for an expansion of synthetic organic chemical product and having CCA for
existing products.CCA compliance report submitted. PP informed that no public complaints
and Litigation against unit.
• Total water consumption will be 125 KLD. Total wastewater generation will be 22 KLD.
• The industrial effluent is treated in primary, secondary and tertiary ETP & treated water is
going to CETP of M/s GESCSL, Vatva for further treatment.
• Natural gas will be used as fuel for proposed boilers
• There is no process gas emission from process.
• 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- 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 AERMOD.
• At various locations, average concentration of PM10 was observed to be varying from 127-
161µg/Nm3,which is more than the permissible limits for all locations.
• An average concentration of PM2.5 levels was observed to be in range of 41-50 µg/Nm3
which is withinthe permissible limits for all locations.
• An average concentration of SO2 and NOX is observed to be within the specified limit of
CPCB.
• 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).
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• It is further noted that ambient air quality for PM10 at all stations is not as per the NAAQ 2009
and PP could not satisfactorily addressed the compliance of NAAQ 2009 at these stations.
Committee asked PP to address the said reason in detail and also asked to conduct source
apportionment study to identify PM10 contributors.
• 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.
• Committee deliberated on specific ToR regarding nearby habitation, CPCB directions to
CETP, Baseline data, project specific SOP & Safety measures, CER, EMP etc.
After deliberation, it was unanimously decided to consider the project for further
consideration only after satisfactory submission of the following:
1. Compliance of specific ToR no. 1 regarding provisions of barriers if any proposed towards
residential flats on back side and measures proposed for control of VOCs and noise to
ensure that nearby residents are not affected due to plant operation.
2. Action plan for waste water generation considering 18 (1) (b) directions under the Water Act
1974 imposed by CPCB on CETP. Compliance of the said directions keeping in view quantity
as well as quality of the effluent. Justification regarding how there is no increase in waste
water generation after proposed expansion.
3. Technical details as well as justification regarding higher values of PM10 and other
parameters in baseline study. Mitigation measures for the same shall be incorporated.
4. To address compliance status of NAAQ 2009 at all the AAQM stations detailed source
apportionment study to identify PM10 contributors.
5. Compliance of ToR no. 62 & 64 regarding project specific SOP & Safety measures
respectively.
6. Compliance of MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 regarding Corporate
Environment Responsibility (CER). Fund allocation based on need based analysis for CER
shall be made as per the said OM dated 01/05/2018 for various activities therein.
7. Action plan for handling, storage and processing of Liq. Ammonia to avoid any fugitive
emissions and consequent complaints from the surrounding area.
3. SIA/GJ/IND2/25948/2017 M/s Krishna Chemtech
Plot No. 2213, G.I.D.C., Panoli, Tal: Ankleshwar,
Dist: Bharuch, Gujarat.
Appraisal
Project / Activity No.: 5(f)
Project status: New
• PP has submitted online application vide no. SIA/GJ/IND2/25948/2017 dated 27/09/2018 for
obtaining Environmental Clearance.
• SEIAA has issued TOR to PP vide letter: IA-J-11011/332/2017-IA-II(I) vide dated :
17/08/2017.
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• Project proponent has submitted EIA Report prepared by Aqua-AirEnvironmental
Engineers Pvt.Ltdbased on the TOR issued by SEIAA.
• This is a new unit and proposes for Synthetic Organic Chemicals manufacturing plant as
tabulated below:
Sr. No
Proposed Products CAS No.
Production
Capacity
(MT/Month)
End Use Of All Products
1 1,4-di bromo Butane , 99% 110-52-1
50
Pharma Intermediate
2 1-(4-fluoro phenylepiperazine) , 99% 2252-63-3 Pharma
Intermediate
3 1-benzylepiperazine 2759-28-6 Pharma
Intermediate
4 N,N-Bis 2-chloro ethyle amine 821-48-7 Pharma
Intermediate
5 Cyclo propyl methyl ketone 765-43-5 Pharma
Intermediate
6 Chlorozoxanone 95-25-0 To treat mucular
Pain
7 Aceclofenac 89796-99-6 Anti-inflammatory
Drug
8 Fluconazole 86386-73-4 Antifungal Drug
9 Niclosamide 50-65-7 Anthelmintic Drug
10 1-(4- Methoxyphenyl)-1-(4-nitrophenyl) piperazine
74852-61-2 Pharma
Intermediate
11 1-(4-Methoxyphenyl) piperazine
38212-30-5 Pharma
Intermediate
12 6-Methyl pyridine-3 yl-2,4-Methylsulfonyl phenyl Etanone (Ketosulfone)
221615-75-4
Pharma Intermediate
13 4 Bromo methyl 2 Cyano biphenyl (Bromo OTBN)
114772-54-2 Pharma
Intermediate
Total 50
• 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 28/11/2018.
• Salient features of the project are as under:
Sr.
no
Particulars Details
A Total cost of Proposed Project (Rs. in Crores): 2.0 Crores
(1) Capital cost for EMS (Environmental Management System): 0.371 Crores
(2) Recurring cost towards the environmental protection measures: 0.99 Crores per
Annum.
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B Total Plot area ( sq. meter) 1500 Sq. m.
Green belt area,/Tree Plantation area ( sq. meter) 532 Sq. m.
C Employment generation 12 persons approx.
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
GIDC, Ankleshwar
Status of permission from the concern authority. Yes, granted. GIDC Water Supply letter No/GIDC/DEE/PNL/1611 dated: 02/06/2017
ii Water consumption (KLD)
Category
Water Consumption KLD
(A) Domestic 1.0
(B) Gardening 1.0
(C) Industrial
Process 8.3
Washing 0.5
Boiler 3.5
Cooling 2.0
Scrubbing 0.5
Industrial Total 14.8
Total (A + B + C) 16.8
1) Total water requirement for the project: 16.8 KLD
2) Quantity to be recycle: 0 KLD
3) Total fresh water requirement: 16.8 KLD
iii Waste water generation (KLD)
Category KLD Remarks
(A) Domestic 0.8
(B) Industrial
Process 9.0 Scrubbing media (0.8 KL/day) will be sold to authorized end user registered under Rule-9.
Washing 0.5
Boiler 0.2
Cooling 0.3
Scrubbing 0.8
Total Industrial waste water
10.8
-Worst case scenario for both water consumption & wastewater generation is based on
considering N,N-Bis 2-chloro ethyle amine
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
In-house ETP (Primary treatment): 10 KLD
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v Mode of Disposal & Final meeting point
Domestic: Domestic: Domestic Waste water (0.8 KL/Day) will be disposed by septic tank or soak pit.
Industrial:
Industrial:
�Total 11.6KL/day (10.8KL/day Industrial + 0.8 KL/day domestic) of
effluent shall be generated. 10.0 KL/day will be given primary treatment
in ETP and then sent it to Common MEE of ACPTCL, Ankleshwar for
further treatment and disposal.
�Scrubbing media (0.8 KL/day) will be sold to authorised end user
registered under Rule-9.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. ,
Name of CF
Common MEE of M/s. ACPTCL, Ankleshwar
Membership of Common facility (CF)
Common MEE of M/s. ACPTCL membership- Ref No: ACPTCL/1300000114/2017-18/78,
date of issue: 13/11/2017
vii Simplified water balance diagram with reuse / recycle of waste water
vii Reuse/Recycle details (KLD) Not proposed.
Total reuse??.KLD
Source of waste water for reuse with quantity in KLD
Application area with quantity in KLD
Remarksregarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.)
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-1.5
MT/Hr)
30 m
Agro
Waste
4 MT/Day
PM ≤ 150 mg/Nm3
SO2 ≤ 100 ppm
NOX≤ 50 ppm
Multicyclone Separator, Bag
Filter
2. Thermic Fluid
Heater
(Capacity-2
Lakh Kcal/Hr)
30 m Agro
Waste
2 MT/Day Multicyclone
Separator, Bag Filter
3. D.G. Set
(Capacity-100
KVA) in
emergency
11 m HSD 5 LIT/hr
Adequate stack height
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only
-
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)
1
Process Vent – 1 (N,N-Bis 2-chloro ethyle amine&Chlorination process)
SO2 -40 mg/Nm3 11 m Two Stage Alkali
Scrubber
2
Process Vent – 2 (4 Bromo methyl 2 cyano biphenyl &Bromination process)
HBr-30 mg/Nm3 11 m Two Stage Alkali
Scrubber
-
iii Fugitive emission details with its mitigation measures.
As below:
1. Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures.
2. Care will be taken to store construction material properly to prevent fugitive emissions, if any.
3. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.
4. Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.
5. Periodic monitoring of work area will be carried out to check the fugitive emission. 6. Breather valves will be provided on solvent tanks. 7. Solvent tank vents will be connected to vent chillers. 8. To eliminate chances of leakages from glands of pumps, mechanical seal will be
provided at all solvent pumps. 9. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents
will be connected to vent chillers. 10. Minimum number of flanges, joints and valves in pipelines. 11. Enclosures to chemical storage area, collection of emission from loading of raw
materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
12. Nitrogen blanketing will be provided, besides special care needs to be taken for control in respect of odorous chemicals, if any.
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 asperHW Rules.
Quantity (MT/Annum)
Disposal Method
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1 Discarded Containers/
Bags/ Liners
Storage & handling of
Raw Materials
SchI/
33.1
2400 Nos/ye
ar
Collection,Storage,Transportation, reuse/ sale to authorize vendor.
2 Used oil
Equipment &
Machineries
SchI/
5.1
120
lit/year
Collection,Storage,Transportation, reuse/ sale to authorize vendor.
3
ETP Sludge ETP Sch-I/
35.3
60
MT/year
Collection,Storage,transportation and disposal common TSDF site (BEIL, Ankleshwar).
4
Distillation Residue
Distillation
Sch-I/
20.3
120
MT/yea
r
Collection,Storage,
Transportation and sent for co-processing in cement industries or Disposal at common incineration site
(BEIL, Ankleshwar).
5
Organic Waste
Mfg. Process of N,N-Bis 2-
chloro ethyle amine
Sch-I/
28.1
60
MT/year
6
Spent Carbon
Mfg. Process of
1-(4- Methoxyphe
nyl)-1-(4-nitrophenyl) piperazine
Sch-I/
28.3
15.6 MT/yea
r
7
Inorganic Salt
Mfg. Process of 1-
benzylepiperazine
Sch-I/
28.1
204
MT/year
Collection,Storage,transportation and disposal common TSDF site (BEIL, Ankleshwar).
8 Waste Cake
(KCl)
Mfg. Process of 1-(4
fluoroPhenylePiperazine)
Sch-I/
20.4
744
MT/ year
Collection,storage, transportation and sell to end user registered under Rule-9.
9 Sodium Bisulfite (20%) Scrubber
Sch-I/
28.1
108
MT/ year
Collection, storage, transportation and sell to end user registered under Rule-9.
10 Sodium Bromide sol. (25%)
Scrubber
Sch-II-
Class- B(5)
180
MT/ year
Collection,storage, transportation and sell to end user registered under Rule-9(Dwarkesh Chemical, Ahmedabad).
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11
Spent Solvent Mfg.
Process
Sch-I/
28.6
200
MT/ year
Collection,storage, transportation and sell to end user registered under Rule-9 (Omkar Chemicals, Panoli)or collection, Storage, management & recovery within the premises and will reuse in plant premises.
ii Membership details of TSDF, CHWIF etc.
Membership of TSDF / Common Hazardous Waste Incineration Facility (CHWIF) that is M/s BEIL, Ankleshwar. Ref. No. BEIL/ANK/2018, dated: 05/02/2018
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
There is no generating any non-hazardous waste.
G Solvent management, VOC emissions etc.
I Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
SOLVENT MANAGEMENT PLAN
• All the solvents shall be directly distilled from product mixes and; if required shall be
purified in packed column with the help of reflux.
• The solvent distillation system shall be designed so as to achieve minimum 95.0 %
recovery of solvent.
• Wherever required, the solvents shall be directly pumped into day tanks from the
storage tanks and shall be charged into the reactors without involving any manual
handling.
• All the pumps shall be mechanical seal type to avoid any leakage of solvent.
• All necessary fire fighting systems shall be provided with alarm system. Flame proof
wiring and flame proof electrical accessories shall be provided to avoid any mishap.
• All the storage tank and day tank shall be connected to a vent system through chilled
water condensers to prevent loss of solvents in the atmosphere.
• All the distillation column vents are also connected to cooling water/ chilled brine
condensers for maximum possible recovery of the solvents.
• All the vents will be connected to a common carbon Adsorber for removing traces of
solvent from vent gases.
• Residue generated from the distillation will be sent to BEIL incinerator site.
• Two condenser will install with cooling water and chilled brine to recover the solvent.
• Primary Condenser HE-01:Cooling Tower water or Chilled water (at 10 0C) will be used
to condense the solvents depend on the vapor pressure at its operating conditions and
the non condensed vapors will be condensed in a Secondary Condenser
• VOC Trap Condenser HE-02: Chilled Brine at -05 0C will be used to trap any traces of
Solvent which is slipped from Secondary condenser
SOLVENT RECOVERY PATTERN
Sr. No.
Name of Solvent
Total Solvent
Input (Kg)
Qty of Solvent
Recycled (Kg)
Qty of Losses
(Kg)
% Recovery
% Loss
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1. IPA 20 19.1 0.9 95.5 4.5
2. Toluene 800 760.2 39.8 95.03 4.97
3. DMF 101.5 98.1 3.4 96.6 3.4
4. Methanol 203.3 192.2 11.1 94.5 5.5
5. Acetone 205.7 200.2 5.5 97.3 2.7
6. MDC 3250 3240 10 99 1
7. Ethyl acetate 1240 1185 55 95.6 4.4
ii VOC emission sources and its mitigation measures
Volatile Organic Content Measures: To prevent losses of these solvents in atmosphere, following infrastructure shall be used in addition to LDAR program
• Leak Free Pumps for transfer of solvents • MSW Gaskets in solvent pipelines to prevent leakage from flanges • Minimum number of flanges, joints and valves in pipelines. • To eliminate chances of leakages from glands of pumps, mechanical seal will be
provided at all solvent pumps. • All the rotating equipments like pumps will be installed with Mechanical Seals to
arrest any sort of emissions. • Condenser and scrubber post Reactor with cooling arrangement • Enclosures to chemical storage area, collection of emission from loading of raw
materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.
• In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send to ETP.
• If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark.
• Flanges will be sealed so less losses will be there. • Two condenser will install with cooling water and chilled brine to recover the solvent. • Primary Condenser HE-01: Cooling Tower water or Chilled water (at 50C) will be
used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser
• VOC Trap Condenser HE-02: Chilled Brine at -15 0C will be used to trap any traces of Solvent which is slipped from Secondary condenser
• During the meeting dated 28/11/2018, 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 16.8 KLD. Total wastewater generation will be 10.8 KLD.
• 10.0 KL/day will be given primary treatment in ETP and then sent it to Common MEE of
ACPTCL, Ankleshwar for further treatment and disposal.
• Scrubbing media (0.8 KL/day) will be sold to authorised end user registered under Rule-9.
• Agro waste will be used as fuel for proposed boiler and thermopack.
• Adequate APCM MCS and Bag filter will be provided with boiler and thermopack separately.
• Two stage alkali scrubber will be provided as APCM with each process reactor stack.
• Hazardous waste management will be as per the HW Rules.
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• The baseline environmental quality has been assessed for various components of the
environment viz. air, noise, water, biological and socioeconomic aspect. The baseline
environmental study has been conducted for the study area of 10 km radial distance from
project site for the period March 2017 to May 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 ISCST3. The
resultant concentrations are within the NAAQS. The Value of PM10 is higher in Panoli Region
due to location near GIDC Estate Area. For Kosamdi, the value of PM10 is higher due to
excess vehicle moment. Preventive measures to reduce the PM10 in Kosamdi village will be
covered in CER Activities. 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.
• Committee deliberated on waste water management, area adequacy, BAT, Baseline study,
green belt development, environmental policy, SOP for safety aspects etc.
• Entire quantity of waste water will be sent to M/s: ACPTCL, Ankleshwar.
• Committee suggested to plant local trees with broad leaf and good canopy for green belt
development.
• Compliance of the ToR was found satisfactory.
After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant
of Environmental Clearance.
4. SIA/GJ/IND2/29128/2018 M/s. Shree Chemopharma Ankleshwar Pvt. Ltd. (Unit-3) Plot No. 313/10, 11, G.I.D.C. Estate, Ankleshwar, Dist.: Bharuch, Gujarat – 393 002
Screening and scoping
Project / Activity No.: 5(f)
Project status: New
• This office has received an application vide their online proposal no.
SIA/GJ/IND2/29128/2018dated 05/10/2018regarding 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 manufacturing plant as tabulated
below:
Sr.
No.
Name of the Products CAS no. /CI
no.
Quantity
MT/Month
End-use of products
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Page 24 of 76
GROUP 1
1. PARA CHLORO BENZOIC
ACID
74-11-3 100 Used in manufacturing of bulk
drug – Mebendazole.
2. ORTHO CHLORO
BENZOIC ACID
118-91-2 Used in manufacturing of bulk
drug – Mefenamic Acid and
Mesalamine.
3. META CHLORO BENZOIC
ACID
535-80-8 Active Pharmaceutical
Intermediate.
4. PARA NITRO BENZOIC
ACID
62-23-7 Used in manufacturing of bulk
drug – Folic Acid. Also used in
Manufacturing of high
performance pigments.
5. META NITRO BENZOIC
ACID
121-92-6 Active Pharmaceutical
Intermediate.
6. 2,3 DI CHLORO BENZOIC
ACID
50-45-3 Used in manufacturing of bulk
drug – Lamotrigine.
7. 2,4 DI CHLORO BENZOIC
ACID
50-84-0 Used in manufacturing of bulk
drug – Lasamide.
8. 2,5 DI CHLORO BENZOIC
ACID
50-79-3 Active Pharmaceutical
Intermediate.
9. 2,6 DI CHLORO BENZOIC
ACID
50-30-6 Active Pharmaceutical
Intermediate.
10. 3,4 DI CHLORO BENZOIC
ACID
51-44-5 Active Pharmaceutical
Intermediate.
11. 3,5 DI CHLORO BENZOIC
ACID
51-36-5 Active Pharmaceutical
Intermediate.
12. ORTHO TOLUIC ACID 118-90-1 Application in manufacturing
high performance pigments.
13. DI NITRO TOLUIC ACID 28169-46-2 Application in manufacturing
high performance pigments.
14. 4 CHLORO 3 NITRO
BENZOIC ACID
96-99-1 Used in manufacturing of bulk
drug – Mebendazole.
15. 2 CHLORO 4 NITRO
BENZOIC ACID
99-60-5 Active Pharmaceutical
Intermediate.
16. 2 CHLORO 5 NITRO
BENZOIC ACID
2516-96-3 Used in manufacturing of bulk
drug – Mesalamine.
17. 2 HYDROXY 5 NITRO
BENZOIC ACID
(5 NITRO SALICYLIC ACID)
96-97-9 Used in manufacturing of bulk
drug – Mesalamine.
18. PARA AMINO BENZOIC
ACID
150-13-0 Used in manufacturing of bulk
drug – Benzocaine. Also used in
manufacturing of high
performance pigments.
19. 3 AMINO 4 CHLORO
BENZOIC ACID
2840-28-0 Application in manufacturing
high performance pigments.
20. 3 AMINO BENZOIC ACID 99-05-8 Application in manufacturing
high performance pigments.
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21. 3,5 DIAMINO BENZOIC
ACID
535-87-5 Application in manufacturing
high performance pigments.
22. 4 NITRO BENZAMIDE 619-80-7 Application in manufacturing
high performance pigments.
23. 4 AMINO BENZAMIDE 2835-68-9 Application in manufacturing
high performance pigments.
24. 3 NITRO BENZAMIDE 645-09-0 Application in manufacturing
high performance pigments.
25. 3 AMINO BENZAMIDE 3544-24-9 Application in manufacturing
high performance pigments.
26. 4 CHLORO 3 NITRO
BENZAMIDE
16588-06-0 Application in manufacturing
high performance pigments.
27. 3 AMINO 4 CHLORO
BENZAMIDE
19694-10-1 Application in manufacturing
high performance pigments.
28. META PHENOXY BENZYL
ALCOHOL
13826-35-2 Active Pharmaceutical
Intermediate.
GROUP 2
29. MEFENAMIC ACID 61-68-7 30 Active Pharmaceutical
Intermediate.
30. MESELAMINE 89-57-6 Active Pharmaceutical
Intermediate.
31. LAMOTRIGINE 84057-84-1 Active Pharmaceutical
Intermediate.
32. FOLIC ACID 59-30-3 Active Pharmaceutical
Intermediate.
33. MEBENDAZOLE 31431-39-7 Active Pharmaceutical
Intermediate.
34. 4 CHLORO 3 NITRO
BENZOPHENONE
56107-02-9 Active Pharmaceutical
Intermediate.
35. 4 AMINO 3 NITRO
BENZOPHENONE
31431-19-3 Active Pharmaceutical
Intermediate.
36. 3,4 DIAMINO
BENZOPHENONE
39070-63-8 Active Pharmaceutical
Intermediate.
37. LASAMIDE 2736-23-4 Active Pharmaceutical
Intermediate.
38. FUROSEMIDE 54-31-9 Active Pharmaceutical
Intermediate.
39. BENZOCAINE 94-09-7 Active Pharmaceutical
Intermediate.
40. DABIGATRAN 211915-06-9 Active Pharmaceutical
Intermediate.
41. ALBENDAZOLE 54965-21-8 Active Pharmaceutical
Intermediate.
42. 4 THIOCYNO 2 NITRO
ANILINE
54029-45-7 Active Pharmaceutical
Intermediate.
TOTAL 130
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• PP was called for presentation in the SEAC meeting dated 28/11/2018.
• The project proponent along with their expert /consultant Aqua-Air Environmental
Engineers Pvt. Ltd., Surat attended the meeting and made presentation before the
committee.
• The project falls under the activity 5(f) as per the schedule of EIA Notification 2006.
• The project falls under Category B of project activity5(f) as per the schedule of EIA Notification
2006
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores): 2.0 Crores
B Total Plot area( sq. meter) 1408 Sq. m.
Green belt area ( sq. meter) 444 Sq. m.
C Employment generation 20
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 will be taken after
getting NOC from GPCB
ii Water consumption (KLD)
Category
Quantity
KLD
Remarks
(A) Domestic 4.0
(B) Gardening 2.0
(C) Industrial
Process 33.5
Washing 1.0
Boiler 12.0
Cooling 3.0
Others
Industrial Total 49.5
Total (A + B + C) 55.5
1) Total water requirement for the project: 55.5 KLD
2) Quantity to be recycled: 0.0 KLD
3) Total fresh water requirement: 55.5 KLD
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iii Waste water generation (KLD)
Category Waste water
KLD
Remarks
(A) Domestic 3.7
(B) Industrial
Process 24.0
Washing 1.0
Boiler 2.0
Cooling 0.3
Others 0.0
Total Industrial
waste water
27.3
Total [A + B] 31.0
-
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
In-house ETP consisting of Primary Treatment facility @ 27.3 KL/Day
v Mode of Disposal & Final meeting point
Domestic: Domestic waste water (3.7 KL/Day) will be sent to Septic Tank & Soak Pit.
Industrial:
Treated industrial effluent (27.3 KL/Day) will be sent to Common MEE, M/s.
BEIL, Ankleshwar after primary treatment for further treatment and disposal.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. ,
Name of CF
Common MEE Facility of M/s. ACPTCL, Ankleshwar
Membership of Common facility (CF)
(For waste water treatment)
REF No. : BEIL/ANK/2018 for Common MEE of M/s. BEIL, Ankleshwar
vii Simplified water balance diagram with reuse / recycle of waste water All figures are in KL/ Day.
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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.)
No Reuse/Recycle
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. Boiler (1 TPH)
18 Natural
Gas or
500
M3/day or
SPM SO2 NOx
Multi cyclone + bag filter
Domesti
c
Process
33.5
Water
Consumption
3.7
Boiler
12
Wastewater to
ETP
24
Washing
1
1
Septic
Tank/
Gardeni
ng
2
Common MEE of M/s. BEIL,
Ankleshwar for further
Cooling
3
0.3
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Briquettes 3 MT / day
2. Thermic Fluid Heater (2 Lac
Kcal/ Hr) 18
Natural
Gas or
Briquettes
200
M3/day or
1 MT / day
SPM SO2 NOx
Multi cyclone + bag filter
3. Thermic Fluid Heater (2 Lac
Kcal/ Hr) 18
Natural
Gas or
Briquettes
200
M3/day or
1 MT / day
SPM SO2 NOx
Multi cyclone + bag filter
4. D.G. set (125 KVA)
12 Diesel 10 Liter/ hr SPM SO2 NOx
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)
1
Process Vent- 1* (Product Name:
Ortho Chloro Benzoic Acid)
NOx 11 4 Stage caustic scrubbers in series
2
Process Vent- 2** (Product Name: 4
chloro 3 nitro benzophenone)
SO2 11
2 stage scrubbers in series. 1st column having water and 2nd column having caustic solution.
3 Process Vent- 3***
(Product Name: Mebendazole)
NH3 11
2 stage scrubbers in series having chilled water
* Stack attached to Oxidation & Nitration reactor ** Stack attached to Thionyl Chloride Reaction *** Stack attached to Reaction generating Ammonia
iii Fugitive emission details with its mitigation measures.
As below:
• Enclosed Processed
• Minimum joints/flanges
• Auto handling for charging Raw Materials
• Pumps with double mechanical seals
• Proper Ventilation
• PPEs
F Hazardous wastes
(as per the Hazardous and Other Wastes (Management and Transboundary Movement)
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Rules 2016.
i
Sr.
no.
Type/Name
of Hazardous
waste
Source of
generation
Category
and
Schedule
as per HW
Rules.
Quantity
(MT/Annu
m)
Disposal Method
1 Used/Spent Oil
Equipment and machinery
Sch-I/ 5.1
120 Litres Collection, Storage, Transportation & sent GPCB approved recyclers/reused as lubricant.
2 ETP sludge
ETP Sch-I/ 35.3
600 MT Collection, Storage, Transportation and disposal at TSDF site of M/s BEIL, Ankleshwar.
3 Discarded Drums/ Bags
Raw material and storage
Sch-I/ 33.1
30 MT Collection, Storage, Transportation & sent back to supplier/ approved recycler.
4 Iron Sludge Process (3,5 Diamino
Benzoic Acid)
Sch-I/ 28.1
2000 MT Collection, Storage, Transportation and disposal at TSDF site of M/s BEIL, Ankleshwar.
5 Sodium Nitrite solution
Scrubber Sch-I/ 28.1
800 MT Collection, Storage & Sold to re-processors or end users having permission under Rule-9.
6 Aluminium Hydroxide Solution
Process (Mebendazol
e)
Sch-I/ 28.1
1800 MT
7 Sodium Bromide Solution
Process (Albendazole
)
Sch-II/ B-15
300 MT
8 Ammonium Chloride Solution
Process (Lasamide)
Sch-I/ 28.1
1600 MT
9 Sodium Sulphite Solution
Scrubber Sch-I/ 28.1
800 MT
10 Liq. Ammonia (20 – 25 %)
Scrubber Sch-II/ A-10
675 MT
11 Distillation Residue
Distillation Sch-I/ 36.1
144 MT Collection, Storage, Transportation & sent to cement industries for co-
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processing or common incineration facility of M/s BEIL, Ankleshwar.
12 Spent Catalyst
Process (Folic Acid)
Sch-I/ 28.2
18 MT Collection, Storage, Transportation and sent to registered regenerator
13 Spent Carbon
Process (Mebendazol
e)
Sch-I/
28.3
19 MT Collection, Storage, Transportation & co-processing in cement industries or Send to TSDF of M/s. M/s. BEIL, Ankleshwar
14 Spent Solvent
Process Sch-I/
28.6
3600 MT Collection, Storage, Re-process and Reuse within premises
15 HCl Process (Albendazole)
Sch-II/ B-15
320 MT Collection, Storage and sent to ETP for further treatment.
16 Sulphuric Acid (60%)
Process (Lasamide)
Sch-II/ B-15
2450 MT Collection, Storage & Sold to re-processors or end users having permission under Rule-9.
17 Recovered Nitric Acid
Process (Para Chloro Benzoic
Acid)
Sch-II/ B-15
1200 MT Collection, Storage and Reuse within premises (Reqd. Qty.:- 2400 MT)
-
ii Membership details of TSDF, CHWIF etc.
(For HW management)
TSDF : BEIL- Ankleshwar
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
No such wastes generate.
G Solvent management, VOC emissions etc.
• All the solvents shall be directly distilled from product mixes and; if required shall be
purified in packed column with the help of reflux and therefore there is no generation of
any distillation residue from the solvent distillation.
• The solvent distillation system shall be designed so as to achieve minimum 94.0 %
recovery of solvent.
• Pure solvent, crude solvent and distilled (recovered) solvent shall be stored only in
storage tanks and we shall not be using drums at any stage in the Solvent
Management System.
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• Wherever required, the solvents shall be directly pumped into day tanks from the
storage tanks and shall be charged into the reactors without involving any manual
handling.
• All the pumps shall be mechanical seal type to avoid any leakage of solvent.
• All necessary fire fighting systems shall be provided with alarm system. Flame proof
wiring and flame proof electrical accessories shall be provided to avoid any mishap.
• All the storage tank and day tank shall be connected to a vent system through cooling
water and chilled brine condensers to prevent loss of solvents in the atmosphere.
• All the distillation column vents will be also connected to cooling water/chilled brine
condensers for maximum possible recovery of the solvents.
• All the vents will be connected to a common carbon Adsorber for removing traces of
solvent from vent gases.
• Residue generated from the distillation will be incinerated in-house or sent to BEIL
incinerator site.
• Coolant to be used
Primary Condensers Cooling Water
Secondary Condensers Chilled Brine up to -50C
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
LIST OF SOLVENTS ALONGWITH TOTAL RECOVERY
Name of Solvent Total Input (Kg)
Qty. of Recovered
Solvent (Kg)
Qty. of Losses
(Kg)
% Recovery
% Losses
Acetone 2521.5 2345.3 176.2 93.01 6.99
Benzene 960 912 48 95.00 5.00
Ethanol 175 159.5 15.5 91.14 8.86
Furfuryl Amine 1564 1410 154 90.15 9.85
Iso Propyl Alcohol 5920 5820 100 98.31 1.69
Methanol 15904 15674 230 98.55 1.45
n-Propoanol 1000 990 10 99 1.00
ODCB 10000 9750 250 97.5 2.5
Toluene 4594 4536.6 57.4 98.75 1.25
ii VOC emission sources and its mitigation measures
• Enclosed Processed
• Minimum joints/flanges
• Adequate Condenser
• Brine will be utilised as chilling agent
• Pumps with double mechanical seals
• Proper Ventilation
• PPEs
• During the meeting dated 28/11/2018, technical presentation made by project proponent.
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• This proposal is for a new synthetic organic chemical product. PP has proposed to achieve
ZLD by means of Treated industrial effluent (27.3 KL/Day) will be sent to Common MEE, M/s.
BEIL, Ankleshwar after primary treatment for further treatment and disposal..
• Natural gas or briquette will be used as fuel for boiler and thermic fluid heaters.
• MCS and Bag filter as APCM attached separately with boiler and TFH.
• Four stage alkali scrubber in series will be as APCM with each reactor stack.
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. Details with respect to justification for proposed expansion: (1) To address
proportionate availability of space for production plant. (2) To address proportionate
availability of storage area for raw materials, finished goods, utilities and goods carrier
movement within premises. (3) To address proportionate captive/common
infrastructure available to accommodate additional load due to proposed expansion.
(4) Environment impact and its mitigation measures for common/ captive infrastructure
due to proposed production.
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. Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent
proposed for use in-house with detailed chemical properties including vapor pressure.
LDAR shall endeavor prevention of losses of solvents to the best minimum extent.
5. Qualitative and quantitative analysis of hazardous waste streams generation from the
manufacturing process (Product wise). 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 shall be incorporated in EIA report.
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6. 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 Chlorine gas, Hydrogen gas, Sulphuric acid,
various solvents etc.
7. Complete details regarding project specific safety aspects of Hydrogenation, Nitration
& Chlorination as per the prevailing norms.
8. Submit status of compliance of Environmental norms of M/s: BEIL, Ankleshwar
common MEE.
• 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.
5. SIA/GJ/IND2/29154/2018 M/s. MAKSONS FINE CHEM. PVT LTD
Plot No. 324, 325, 326 & 327, GIDC Industrial Estate, Ankleshwar – 393002, Dist – Bharuch, State: Gujarat.
Screening and scoping
Project / Activity No.: 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no.
SIA/GJ/IND2/29154/2018dated 05/10/2018 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 proposes for Synthetic Organic Chemicals expansion in
manufacturing plant as tabulated below:
Sr. no.
Name of the Products
CAS no. / CI no.
Quantity (MT/Month) End-use of the
products Existing Proposed Total
Group A
1. Ibefone (Phthalide) 87-41-2 3.00
12.00 12.00
Drug Intermediate,
API Industry
2. Bromasil
(Bromophthalide)
6940-49-4 1.00 Drug Intermediate,
API Industry
3. 1 – Bromo-4-Cyano
Acetophenone
20099-89-2 1.00 Drug Intermediate,
API Industry
4. 2,6-Dichloro 24966-39-0 1.00 Drug Intermediate,
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Thiophenol API Industry
5. 2-Phenyl
Thioethanol
699-12-7 1.00 Drug Intermediate,
API Industry
6. 3,4,5-Trimethoxy
Aniline
24313-88-0 2.00 Drug Intermediate,
API Industry
7. 3,5-Dimethoxy
Aniline
10272-07-8 2.00 Drug Intermediate,
API Industry
8. Diethyl Phenyl
Acetamide
2431-96-1 2.00 Pharma Drug, API
Industry
9. Pentoxyphyline 6493-05-6 1.00 Pharma Drug, API
Industry
10. Pyridyl Acetic Acid&
HCl
501-81-5
6419-36-9
2.00 Drug Intermediate,
API Industry
11. 1-(2 – Chloro-
(Chlorophenyl)-
Butyl)-Imidazole HCl
68055-81-2 -- Drug Intermediate,
API Industry
12. 1-Bromo,2,6-
Dimethoxybenzene
16932-45-9 Drug Intermediate,
API Industry
13. 1 – Bromo, 3,4, 5 -
Trimethoxy Benzene
2675-79-8 Drug Intermediate,
API Industry
14. 2 – Amino-(2,5-
Dimethoxy Phenyl)-
Ethanone
784138-79-0 Drug Intermediate,
API Industry
15. 2-
Carboxybenzaldehy
de
119-67-5 Drug Intermediate,
API Industry
16. 3,5-Dimethoxy
Bromo Benzene
20469-65-2 Drug Intermediate,
API Industry
17. 3,5-Dimethyl Bromo
Benzene
576-23-8 Drug Intermediate,
API Industry
18. 3-Bromoaniline 591-19-5 Drug Intermediate,
API Industry
19. 3-Methoxyphenol 150-19-6 Drug Intermediate,
API Industry
20. 4-(Methylthio)-
Phenol
1073-72-9 Drug Intermediate,
API Industry
21. 4-Acetylbenzoic Acid 586-89-0 Drug Intermediate,
API Industry
22. 4-Acetylbenzoic Acid
Methyl Ester
3609-53-8 Drug Intermediate,
API Industry
23. 4-Chloro Phenoxy
Aniline
2770-11-8 Drug Intermediate,
API Industry
24. 4-Nitrophenol MSA
Ester
1158363-70-2 Drug Intermediate,
API Industry
25. 4-Phenoxy Benzoic
Acid
2215-77-2 Drug Intermediate,
API Industry
26. 6 – Bromo – 2- 5773-80-8 Drug Intermediate,
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Naphoic Acid and
Ester
33626-98-1 API Industry
27. 6-Chloro Tetralone 26673-31-4 Drug Intermediate,
API Industry
28. Butoconazole and
Butoconazole Nitrate
64872-77-1 Pharma Drug, API
Industry
29. Methyl Sulfonyl
Acetic Acid
2516-97-4 Drug Intermediate,
API Industry
30. Risedronic Acid and
Sodium Salt
105462-24-6
115436-72-1
Drug Intermediate,
API Industry
Group B
31. 2, 4 - Dimethyl
Thiophenol
13616-82-5 1.00
15.00 15.00
Drug Intermediate,
API Industry
32. 3-Methoxy
Thiophenol
15570-12-4 1.00 Drug Intermediate,
API Industry
33. 4-Chlorophenoxy
Aniline
2770-11-8 2.00 Drug Intermediate,
API Industry
34. 4-Cyano
Acetophenone
1443-80-7 2.00 Drug Intermediate,
API Industry
35. Doxepinone 4504-87-4 2.00 Drug Intermediate,
API Industry
36. 1,3,5-Trimethoxy
Benzene
621-23-8 -- Drug Intermediate,
API Industry
37. 1-Benzyl Imidazole 4238-71-5 Drug Intermediate,
API Industry
38. 2,3-Dimethyl Bromo
Benzene
576-23-8 Drug Intermediate,
API Industry
39. 2-AcetylPyridine 1122-62-9 Drug Intermediate,
API Industry
40. 2-Phenyl
Thioethanol
699-12-7 Drug Intermediate,
API Industry
41. 3,5-Dimethoxy
Benzoic Acid Methyl
Ester
1132-21-4
2150-37-0
Drug Intermediate,
API Industry
42. 3,5-Dimethyl Bromo
Benzene
556-96-7 Drug Intermediate,
API Industry
43. 3-Amino Thioanisole 1783-81-9 Drug Intermediate,
API Industry
44. Doxepin HCl 1668-19-5 Pharma Drug, API
Industry
Group C
45. 2-Bromo Aniline 615-36-1 1.00
20.00 20.00
Drug Intermediate,
API Industry
46. 2-Iodo Aniline 615-43-0 1.00 Drug Intermediate,
API Industry
47. 1 – Bromo – 2- 583-55-1 -- Drug Intermediate,
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Iodobenzene API Industry
48. 3-Acetylpyridine 350-03-8 Drug Intermediate,
API Industry
49. Pyridine – 2-
Aldehyde
1121-60-4 Drug Intermediate,
API Industry
50. Pyridine – 4-
Aldehyde
872-85-5 Drug Intermediate,
API Industry
Group D
51. N,N-Diethyl
Cyanoacetamide
26391-06-0 1.00
25.00 25.00
Drug Intermediate,
API Industry
52. 2 – Bromo – 5-
Chlorotoluene
14495-51-3 -- Drug Intermediate,
API Industry
53. 5 – Bromo – 2-
Chlorotoluene
54932-72-8 Drug Intermediate,
API Industry
54. Ciprofloxacin Lactate 97867-33-9 Pharma Drug, API
Industry
55. Entacapone 130929-57-6 Pharma Drug, API
Industry
Group E
56. Bromoacetaldehyde
Dimethyl Acetal
7252-83-7 -- 25.00 25.00 Drug Intermediate,
API Industry
57. R & D Products -- -- 2.00 2.00 All Chemical
Industries
Total 3.00 99.00 99.00
Note:The unit will manufacture any of the above products as mentioned in group A to E in group wise in either / or basis as per mentioned quantity. But, total production capacity after expansion shall not exceed 99.00 MT/month.
• 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 28/11/2018.
• The project proponent along with their expert /consultant M/s. Earthcare Enviro Solution
Pvt. Ltd 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: Rs. 6.50 Crore
Proposed: Rs. 12.00 Crore
Total: Rs. 18.50 Crore
B Total Plot area
( sq. meter)
Existing: 3615.00 Sq. m.
Proposed: 6920.55 Sq. m.
Total: 10,535.55 Sq. m.
Green belt area
( sq. meter)
Existing: 500.00 Sq. m.
Proposed: 3000.00 Sq. m.
Total: 3500.00 Sq. m.
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C Employment generation Existing: 40 (Male-38, Female 02)
Proposed: 150 (Male-140, Female-10)
Total: 190 (Male-178, Female)
D Water
i
Source of Water Supply(GIDC Bore well,
Surface water, Tanker supply etc...)
GIDC, Ankleshwar
Status of permission from the concern authority.
Unit will get permission from GIDC for
additional water requirement.
ii
Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 1.00 7.10 8.10 --
(B) Gardening 2.00 12.00 14.00 --
(C) Industrial
Process 11.50 60.77 72.27 --
Washing 1.50 3.00 4.50 --
Boiler 2.00 100.00 102.00 --
Cooling 3.00 7.00 10.00 --
Others (Scrubber) -- 5.64 5.64 --
Industrial Total 18.00 176.41 194.41 --
Total (A+B+C) 21.00 195.51 216.51 --
1) Total water requirement for the project: 216.51 KLD
2) Quantity to be recycled: 56.15 KLD
3) Total fresh water requirement: 160.36 KLD
iii Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 1.00 5.68 6.68 --
(B) Industrial
Process 11.00 48.18 59.18 --
Washing 1.50 2.50 4.00 --
Boiler 0.30 5.00 5.30 --
Cooling 0.20 0.35 0.55 --
Others (scrubber) -- 5.64 5.64 --
Total Industrial
waste water 13.00 61.67 74.67 --
iv Treatment facility within premises with capacity [For existing and Proposed]
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
� Proposed in-house ETP (Capacity:80.00 m3/day) having PrimaryTreatment.
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� MEE capacity: 5.0 KL/hr
v Mode of Disposal & Final meeting point
Domestic:
Septic Tank / Soak Pit system.
Industrial:
After expansion, industrial effluent generated from manufacturing process and
other ancillary operation shall be allowed into in-house ETP for primary
treatment. Primary treated water (13.00 KLD) will be sent to CETP of M/s. ETL
for further treatment & final disposal as unit has already valid CTO for
wastewater disposal to CETP (M/s. ETL) and balance quantity (61.67 KLD) will
be sent to Stripper followed by MEE from where water will be concentrated to
recover mixed solvent, salt and condensed water will be reused for washing,
scrubber & process.
Note: At present, unit has planned to install in-house MEE for additional
wastewater. However, in future as & when function of CETP in this area
will improved / installed & if GPCB will grant permission to discharge
effluent into CETP, mode of disposal will be CETP after getting prior
permission.
vi
In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility
--
Membership of Common facility (CF)
--
(For waste water treatment)
vii Simplified water balance diagram with reuse / recycle of waste water
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vii Reuse/Recycle details (KLD)
[Source of reuse & application area]
Total reuse: 56.15 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.)
MEE recovered water
– 56.15 KLD
Process – 48.65 KLD Washing – 4.50 KLD Scrubber – 3.00 KLD
COD : 300 – 400 mg/l
BOD : 100 – 150 mg/l
TDS : 300 – 500 mg/l
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
MT/Day
Type of emissions
i.e. Air Pollutants
Air Pollution Control
Measures
(APCM)
Existing
1
Steam Boiler
(Capacity: 600 kg/hr)
12.00 Natural
Gas 6.250
SCM/Hr
PM
SO2
NOX
Adequate stack height is
provided 2
Thermic Fuel Heater
(Capacity: 1 Lac Kcal/hr)
12.00 Natural
Gas 6.250
SCM/Hr
3 D. G. Set – 01 No. (Capacity: 90 KW)
5.0 HSD 23 Lit/hr
Proposed
4
Steam Boiler
(Capacity: 5 TPH)
12.00 Briquettes
of Bio Coal
600 kg/Hr
PM
SO2
NOX
Multi Cyclone Separator &
Water Scrubber
5
Thermic Fluid Heater
(Capacity: 3 Lac Kcal/hr)
12.00 Natural
Gas 18.75
SCM/Hr
Adequate stack height
will be provided
6
D. G Set – 02 Nos. (Stand By)(Capacity: 500 KW in single / multiple DG Sets)
5.00 HSD 135 Lit/hr
Adequate stack height
will be provided
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
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Existing & Proposed
-
Sr. No.
Specific Sourceof emission(Name of
theProduct &Process)
Type of emission
Stack/Vent
Height (meter)
Air Pollution Control
Measures(APCM)
Existing
1 Ammoniation NH3 12.0 Scrubber
2 Reaction Vessels-1 HBr 10.0 Alkali Scrubber
3 Reaction Vessels-2 HCl 10.0 Alkali Scrubber
Proposed
4 Reaction Vessel-1 HCl
SO2 10.0
Two stage
Alkali Scrubber 5 Reaction Vessel-2 H2S 10.0
6 Reaction Vessel-3 HBr 10.0
7 Reaction Vessel-4 NH3 10.0 Acid Scrubber
-
iii Fugitive emission details with its mitigation measures.
� 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.
Existing & Proposed
i
Sr. no.
Type/ Name of Hazardous waste
Specific Source of generation (Name of the Activity, Product etc.)
Category and Schedule as per HW Rules.
Quantity (MT/Annum)
Management of HW
Existing Proposed Total
1 Process Residue and Wastes
Process
28.1 (Sch. I)
1.20 -- 1.20 Collection, Storage, Transportation & Disposal for incineration in common incinerator of BEIL, Ankleshwar
2 Spent Solvents
Process (many
products)
28.6 (Sch. I)
120.00 30.00 150.00 Collection, Storage, Reuse within
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&Stripper premises OR Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
3 Empty Barrels / Containers / Liners Contami-nated with Hazardous Chemicals / Wastes
Raw Materials &
finished Products packing material
33.1 (Sch. I)
3.00 87.00 90.00 Disposal by send it to authorized decontamination facility / recycler or reuse or send back to supplier
4 Chemical Sludge from Waste Water Treatment
Effluent Treatment
Plant
35.3 (Sch. I)
10.80 56.00 66.80 Collection, Storage, Transportation and Disposal by send it to TSDF – BEIL, Ankleshwar
5 Used or Spent Oil
D G Set &
Thermopack
5.1 (Sch. I)
0.04 0.16 0.20 Reuse in plant & machinery as lubricant OR sell it to authorized re-refiners / recycler
6 Sulphide (as H2S) (Sodium Sulphide / Sodium Hydrogen Sulphide) (55-60%)
Scrubber A13 (Sch. II)
33.76 3.68 37.44 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
7 Oxides and Hydroxides except those of hydrogen, Carbon,
Process (Product No.
01)
B32 (Sch. II)
17.10 322.90 340.00 Collection, Storage, Transportation & Disposal by sell out to
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Silicon, Iron, Aluminum, Titanium, Manganese, Magnesium, Calcium (Zn(OH)2) (90-95%)
authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
8 Bromates (Hypo - Bromites) (Sodium Bromide) (90-95%)
Process (Product No.
45 & 56)
B6 (Sch. II)
30.00 3141.00 3171.00 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
9 Ammonium Sulphate Solution (60-70%)
Scrubber 35.1 (Sch. I)
-- 15.00 15.00 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
10 Sodium Sulphate (92-95%)
Process (Product No. 10, 29, 47)
28.4 (Sch. I)
-- 333.00 333.00 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
11 Copper Solution (95-97%)
Process (Product No. 12, 13, 16,
28.4 (Sch. I)
-- 5820.74 5820.74 Collection, Storage, Transportation
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17, 27, 38, 42, 52, 53)
& Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
12 Sodium Acetate Solution (92-95%)
Process (Product No.
52, 53)
28.4 (Sch. I)
-- 5346.00 5346.00 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste
13 Inorganic Salt
Scrubber 35.1 (Sch. I)
-- 3.00 3.00 Collection, Storage, Transportation and Disposal by send it to TSDF – BEIL, Ankleshwar
14 Spent Carbon
Process (Many
Products)
28.3 (Sch. I)
-- 98.40 98.40 Collection, Storage, Transportation & Disposal for co-processing
15 Spent Catalyst
Process (Product No.
49, 50)
28.2 (Sch. I)
-- 60.00 60.00 Reuse within premises OR Collection, Storage, Transportation and Sell to Registered Recyclers.
16 Iron Sludge Process (Product No.
43)
28.1 (Sch. I)
-- 322.20 322.20 Collection, Storage, Transportation & Disposal at TSDF site for secured landfill
17 Distillation residue
Process (Many
20.3 (Sch. I)
-- 88.32 88.32 Collection, Storage,
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Products) Transportation and Disposal for co-processing
18 MEE salt MEE 35.3 (Sch. I)
-- 548.00 548.00 Collection, Storage, Transportation & Disposal at TSDF site for secured landfill
-
ii Membership details of TSDF, CHWIF etc.
(For HW management)
Unit has got membership of M/s. BEIL for
landfilling and incinerable waste.
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
As below
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
In-house solvent recovery plant will be installed and recovered solvent will be again reused in
process and residue will be disposed for co-processing.
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 28/11/2018, technical presentation made by project proponent.
• This proposal is foran expansion of synthetic organic chemical product. Unit is having valid
CCA for existing products.
• Total water consumption will be 216.51 KLD. Total wastewater generation will be 74.67 KLD.
• Industrial effluent generated from manufacturing process and other ancillary operation will be
allowed into in-house ETP for primary treatment. Primary treated water (13.00 KLD) will be
sent to CETP of M/s. ETL for further treatment & final disposal as unit has already valid CTO
for wastewater disposal to CETP (M/s. ETL) and balance quantity (61.67 KLD) will be sent to
Stripper followed by MEE from where water will be concentrated to recover mixed solvent, salt
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and condensed water will be reused for washing, scrubber & process.
• 56.15 KLD MEE condensate will be reused back in process.
• Committee deliberated on waste water management, Compliance of CPCB directions to
CETP etc. Committee found that management of waste water is not convincing. Upon asking
about feasibility of treated waste water reuse, PP could not replied satisfactorily..
After deliberation, it was unanimously decided to consider the project for further
consideration only after satisfactory submission of the following:
1. Action plan for waste water generation considering 18 (1) (b) directions under the Water Act
1974 imposed by CPCB on CETP. Compliance of the said directions keeping in view quantity
as well as quality of the effluent.
2. Sound management of waste water keeping in view characteristics of waste water in worst
case scenario.
3. Feasibility report for reuse of waste water for industrial purpose.
6. SIA/GJ/IND2/21840/2018 M/s MayurDyechem Intermediates LLP. (Unit-I) Plot No. A1/108,91, A2/92 Phase-2, GIDC Estate, Vatva, Dist: Ahmedabad-382445.
Screening and scoping
Project / Activity No.: 5(f)
Project status:Expansion
• This office has received an application vide their online proposal no.
SIA/GJ/IND2/21840/2018dated 05/10/2018regarding 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 proposes for Synthetic Organic Chemicals expansion in
manufacturing plant as tabulated below:
Sr.
no.
Name of the
Products
CAS no. /
CI no.
Quantity
MT/Month
End-use of
the products
Existing
Proposed Total
1 Vinyl Sulphone
2494-89-5 150 75 225 In Reactive Dyes Manufacturing
2 H-Acid 5460-09-3 0 100 100
Total 150 175 325
• 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 15/11/2018.
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• The project proponent along with their expert /consultant Bhagwati Enviro Care Pvt. Ltd.
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):
Existing: 7.84 Proposed: 10.98 Total: 18.82
B Total Plot area
( sq. meter) Existing –6375
(Plot No 91-1711 Plot No. 92-1887 Plot No. 108-2777) Proposed-0 Total: 6375 Sq. m
Green belt area
( sq. meter)
Existing: 1900 Sq. m. Proposed: 0 Sq. m. Total: 1900 Sq. m.
C Employment generation Existing:80 Proposed: 40 Total:120
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply
etc...)
Bore well
Status of permission from the concern authority.
Under Consideration (Please refer Annexure-IV)
ii
Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(D) Domestic 5 30 35
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(E) Gardening
20 30 50
(F) Industrial
Process 122 112 234
Washing 24.3 22 46.3
Boiler 4.9 20 24.9
Cooling 23.2 20 43.2
Others 2.6 15 17.6
Industrial Total 177 189 366
Grand Total
(A+B+C)
202 249 451
4) Total water requirement for the project: 451 KLD
5) Quantity to be recycled:53 KLD
6) Total fresh water requirement: 398 KLD
iii
Waste water generation (KLD)
Category Existin
g
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(C) Domestic
5 30 35
(D) Industrial
Dilute Stream- V.S. Concentrate Stream –V.S. Process Concentrate Stream –H-Acid
15 2.5 17.5
37 22.2 59.2
0 120 120
Washing 24.3 20 44.3
Boiler 0.2 7 7.2
Cooling 0.5 2 2.5
Total (Industrial) 77 173.7 250.7
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Total Waste Water Generation
(M3/Day)
82 203.7 285.7
iv Treatment facility within premises with capacity [For existing and Proposed]
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP
etc..
� Existing ETP: 150 KL/Day (Tertiary) Followed By spray dryer
v Mode of Disposal & Final meeting point
Domestic:
To soak pit
Industrial:
- In the existing system dilute waste water stream of V.S. of 15 M3/Day is treated in our existing ETP and disposed to the CETP of The Green Environment Services Co operative Society Ltd.
- After expansion Dilute waste water stream of Vinyl Sulphone of 2.5 M3/Day will be disposed to CETP of The Green Environment Services Co operative Society Ltd. after the treatment in our existing ETP.
- In existing system concentrated waste water stream of Vinyl Sulphone of 37 M3/Day is treated in our own Spray Drying System and also disposing through the common MEE and Spray Drying System of The Green Environment Services Cooperative Society Ltd. & Chhatral Environment Management System Pvt. Ltd.
• After expansion Concentrated Waste Water stream of Vinyl Sulphone of 22.2 M3/Day and H-Acid of 120 M3/Day will be treated as per the existing treatment system of Vinyl Sulphone i.e. treated in our own Spray Drying System and will also be dispose through the common MEE and Spray Drying System of The Green Environment Services Cooperative Society Ltd. &Chhatral Environment Management System Pvt. Ltd.
• Concentrated waste water stream of H-Acid will be treated by our own MEE and Spray Drying system and will also be disposed through the common MEE and Spray Drying System of The Green Environment Services Cooperative Society Ltd. &Chhatral Environment Management System Pvt. Ltd And 53 m3/Day will be reuse in H-acid Manufacturing Process.
• Boiler and Cooling Blow Down Will be send to CETP.
• Washing effluent will be evaporate in in-House Spray Dryer.
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vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE,
CHWIF etc.
Name of Common facility
1. CETP, Vatva
2. Novel: Spent Acid, Vatva
3. Common Spray Dryer, Vatva
4. Common Spray Dryer Chhatral
5. CHWIF: Saurastra Enviro Projects Pvt. Ltd
6. TSDF: Eco Care Infrastructure Pvt. Ltd
Membership of Common facility (CF)
(For waste water treatment)
CETP: Green Environment Services Co-Op. Society Ltd
Spray Dryer: Green Environment Services Co-Op. Society Ltd
Spray Dryer: Chhatral Enviro Management System Pvt. Ltd
vii Simplified water balance diagram with reuse / recycle of waste water
Please Refer Annexure-V
vii Reuse/Recycle details (KLD)
[Source of reuse & application area]
Total reuse 53 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.)
53 KLD from H-acid Used in H-Acid
Manufacturing
COD:
BOD:
TDS:
-
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
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-
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 Boiler-1 (Existing) (400 Kg/Hr)
12 Natural
gas 12 m3/hr
Particulate matter SO2 NOX
Not required
due to the utilization of Natural
Gas as Fuel
2 Thermic Fluid Heater (Existing) (150000 Kcal/Hr)
12
Natural gas
12 m3/hr
3 Boiler -2 (1.5 MT/Hr) Boiler-3 (1.5 MT/Hr) (Proposed)
20 Natural gas
600 m3/hr
4 Hot Air Generator (HAG) (Existing) (300000 Kcal/Hr)
12 Natural gas
30 m3/hr
5 Incinerator-1 (For Vinyl Sulphone) (Existing) (1200 Lit/Hr)
30 Natural
gas 300
m3/hr
Particulate matter
SO2
HF Cl
NOX CO
Total Dioxin &
Furan
Water scrubber
followed by Alkali
Scrubber Twin
Cyclones, One Water scrubber
followed by Alkali
Scrubber
6 Spray Dryer (Existing) (3300 Lit/Hr)
30
Natural gas
300 m3/hr
7 DG Set 11
Diesel 10
Lit/Day
Particulate matter SO2 NOX
----
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing & Proposed
-
Sr.
no.
Specific Source of
emission
(Name of the Product
Type of
emission
Stack/Vent
Height
(meter)
Air Pollution
Control
Measures
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&Process) (APCM)
1 CHLOROSULPHONATOR (Acetanilide addition in Vinyl Sulphone)
HCl SO2 Cl2
20
Total four stage scrubbing system Includes Two stage Water Scrubber followed by two stage Alkali Scrubber
2 CHLOROSULPHONATOR (Thionyl Chloride addition in Vinyl Sulphone)
HCl SO2 Cl2
20
Four Stage Alkali Scrubber
3 NEUTRALIZER (H-Acid)
NOX
20
Total four stage scrubbing system includes One stage Water Scrubber followed by three stage Alkali Scrubber
4 ISOLATOR (H-Acid )
SO2 20
Total four stage scrubbing system includesTwo stage Water Scrubber followed by two stage Alkali Scrubber
-
iii Fugitive emission details with its mitigation measures.
Fugitive emission from the proposed project activities shall be mainly the VOCs emissions, which results from uses of solvents. - This emission will be taken place only at storage and handling of solvent. - Storage is in closed area with a facility of condenser which will reduce the emission.
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
Specific
Source of
generation
Category
and
Schedule
Quantity
(MT/Annum)
Management
of HW
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waste (Name of
the
Activity,
Product
etc.)
as per
HW
Rules.
Existing Proposed Total
1 ETP Sludge Effluent Treatment Plant
35.3 12 MT/ Year
900 MT/ Year
912 MT/ Year
Collection, Storage, Transportation, Disposal at TSDF
2 Used Oil Plant Machinery
5.1 1.2 KL/ Year
1.8 KL/ year
3.0 KL/ year
Collection, Storage, Transportation , Disposed by selling to Registered reprocessers /recycler
3 Discarded Carboys/ Barrels/ Bags/Liner
Raw Material Section
33.1 0.60 MT/ Year
30 MT/ Year
30.60
MT/ Year
Collection, Storage, Decontamination, Transportation, Disposal by selling to authorized recycler
4 Gypsum Sludge
From H-Acid Manufacturing Process
26.1 7200 MT/Yea
r
1050 MT/Year
8250 MT/Year
Collection, Storage, Transportation, Sell to Cement Manufacturing Units
5 Process Iron Waste
From H-Acid Manufacturing Process
26.1 NIL 2750 MT/ Year
2750 MT/ Year
Collection, Storage, Transportation, Sell to Cement Manufacturing Units
6 Incinerated Ash
From Incinerator
37.2 720 MT/ Year
NIL 720 MT/ Year
Collection, Storage, Transportation, Disposal at TSDF
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7 Spent Sulphuric Acid
From Vinyl Sulphone Manufacturing Process
26.3 19200 MT/ Year
14400 MT/ Year
33600
MT/ Year
Collection, Storage, Reuse in V.S. and H-Acid Plant. Treatment in ETP
8 Spray Dried Solid
From Spray Dryer
37.2 Nil 5000 MT/ Year
5000 MT/ Year
Collection, Storage, Transportation, Reuse, Sell and Disposal at TSDF
9 Spent Hydrochloric Acid
From Scrubber
26.3 2140 MT/ Year
1630 MT/ Year
3770 MT/ Year
Collection, Storage, and sell to actual users. Treatment in ETP
10 NaHSO3 From Scrubber
26.3 Nil 297
MT/Year
297
MT/
Year
Collection,
Storage, and
sell to actual
users.
Treatment in
ETP
11 Acetic Acid From Vinyl Sulphone
26.3 Nil 3285
MT/Year
3285
MT/
Year
Collection,
Storage, and
sell to actual
users.
Treatment in
ETP
-
ii Membership details of TSDF, CHWIF etc.
(For HW management)
1. CHWIF: Saurastra Enviro Projects Pvt.Ltd
2. TSDF: Eco Care Infrastructure Pvt. Ltd
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
Not be any Non Hazardous Waste Generate.
G
Solvent management, VOC emissions etc.
Name Of Product
Product Quantity
Batch Size in Kg
No. Of Batch/ Month
Solvent to be used
Quantity Used KL/Batch
Quantity Recovered In KL/Batch
Quantity Loss in KL/Batch
H-Acid 100 1500 67 Methanol 1125 1020 105
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i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered
Solvents
� Recovery Of Methanol 91 % and it reuse in process.
ii VOC emission sources and its mitigation measures
� We will assure that measure VOC level in our Manufacturing unit as well as
Raw material storage area. We will also do work place monitoring &
according implementation.
• During the meeting dated 15/11/2018, technical presentation made by project proponent.
• This proposal is for expansion of Dyes Intermediate Vinyl Sulphone and addition of H-Acid.
• While discussing about compliance of the GPCB Circular dated 03/11/2018 regarding specific
products within PCPIR region as well as outside PCPIR region, Project proponent as well as
environmental consultant could not reply satisfactorily.
• Committee found that ratio of V.S and H-acid mentioned in proposed product profile is not as
per the said circular published by GPCB.
In view of the above stated facts, Committee unanimously decided to consider the project for
further consideration only after submission of the following:
1. Compliance of all the conditions stipulated in GPCB circular dated
03/11/2018regarding specific products.
2. Revised proposal considering compliance of GPCB Circular dated 03/11/2018.
7. SIA/GJ/IND2/28777/2018 M/s. Pharmex Healthcare
Plot No. A1-6104/5, GIDC Notified Industrial Estate, Ankleshwar– 393 002, Dist. Bharuch, State- Gujarat, India
Screening and scoping
Project / Activity No.: 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no.
SIA/GJ/IND2/28777/2018dated 21/09/2018 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 existing unit engaged in manufacturing of Synthetic Organic Chemicals and now
proposes for expansion as tabulated below:
Sr. No.
Name of Products CAS No./ Cl no.
Quantity MT/Month
End Use
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Existing Proposed Total
1. Benzoturane 2- Hydroxy Dimethyl Methanol Sulfonate (BHDMS)
-- 30 -30 0 --
2. Hydrazide OR HS code: 28251020
45 -40 5 To cure Lower Blood
Pressure
Ganciclovir Intermediate (G.A.- 11) (Job Work)
-- 1.5 -1.5 0 --
3. 2,3 Dichloro 6 Nitro Aniline (DICONA)
65078-77-5
0 25 25 For the preparation of
Polymers
4. Nitro RF
(O, O, O-Tris (4 -
nitrophenyl) thiophosphate)
64131-85-7
0 5 5 For the preparation of
Amino RF
5. 2-Amino-4-chlorophenol 95-85-2 0 20 20 To manufacture
Chlorzoxazone
6. 4-Amino-2-chlorophenol 3964-52-1
Used for manufacturing 3-Chloro-4-
[(pyridin-2-yl)methyloxy]
aniline
7. 2, 4, 5-Trichloro Aniline 636-30-6 To manufacture
Pigment- Red 112
8. 1,8 Diamino Naphthalene 479-27-6 Used as Pigment
intermediate
9. Para Chloro Aniline Hydrochloride
20265-96-7
0 20 20 Chlor Hexidine
Base
10. 1,5 Dinitro Naphthalene 605-71-0 0 30 30 To manufacture 1,5 Diamino Naphthalene
11. 1,8 Dinitro Naphthalene 602-38-0 To manufacture 1,8 Diamino Naphthalene
TOTAL 75 (Max.) 105
NOTE:
• Total production capacity after proposed EC expansion shall be 105 MT/Month.
• Either individual or total production of products in Sr. No. 5 to 8 shall not exceed 20 MT/Month after proposed expansion.
• This is an expansion unit proposes for Synthetic Organic Chemicals manufacturing plant as
tabulated below:
• PP was called for presentation in the SEAC meeting dated 28/11/2018.
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• The project proponent along with their expert /consultant Siddhi Green Excellence Pvt. Ltd
attended the meeting and made presentation before the committee.
• Salient features of the project including Water, Air and Hazardous waste management:
Sr.
no.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing: 0.8821 Crore
Proposed: 4.499 Crores
Total: 5.3811 Crores
B Total Plot area
( sq. meter)
Existing: 3182 Sq. m.
Proposed: NIL
Total: 3182 Sq. m.
Green belt area
( sq. meter)
Existing: 271.86 Sq. m.
(~8.5%)
Proposed: 110.16 Sq. m.
(~3.5%)
Total: 382.02 Sq. m. (~12%)
Balance greenbelt shall be
developed in the area
specified by GIDC.
C Employment generation Existing: 14 Nos. Company
employees + 6 Nos. on
Contract basis
Proposed: 20 Nos. Company
employees + 6 Nos. on
Contract basis
Total: 34 Nos. Company
employees +12 Nos. on
Contract basis
Locally employed manpower
shall be utilized.
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply
etc...)
GIDC
Status of permission from the concern authority.
Existing Quantity:
Industrial: 7.5 KLD +
Domestic: 0.5 KLD +
Gardening: 0.5 KLD
ii Water consumption (KLD)
Existing KLD
Proposed
KLD
Total after
Expansion
KLD
Remarks Water Consumpti
on*
Water Consumption after
continuing one of the
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existing product*
(G) Domestic 0.5 0 2 2 --
(H) Gardening 0.5 0 1 1 --
(I) Industrial
Process 1 0 8 8
Total fresh water requirement for Proposed Production is 8 KLD.
Washing 1.5 0 NIL NIL
Boiler blowdown of 0.9 KLD & Cooling tower blowdown of 2 KLD shall be reused for Washing purpose. So fresh water requirement for Washing shall be NIL.
Boiler 3 0.2 2.8 3 --
Cooling 2 0.1 6.9 7 --
Others (APCM)
0 0 2 2
Total fresh water requirement for Proposed APCM is 2 KLD.
Industrial Total
7.5 0.3 20 20
Grand Total (A+B+C)
8.5 0.3 23 23
*Production quantity of one of the existing products (i.eHydrazide) shall be reduced from 45 MTM to 5 MTM and rest of the existing products shall be discontinued after proposed expansion.
7) Total water requirement for the project: 25.9 KLD
8) Quantity to be recycled: 2.9 KLD
9) Total fresh water requirement: 23 KLD
iii Waste water generation (KLD)
Cat
Existing KLD
Proposed
Total after
Remarks
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egory
Waste
Water
Generation*
Waste Water
Generationafter
continuing one of
the existing product*
KLD Expansion KLD
(E) Domestic
0.5 0 1.5 1.5
Sewage shall be disposed to soak pit via septic tank.
(F) Industrial
Process
1.2 0 10 10
Low COD effluent stream (4 KLD) & High COD effluent stream (6 KLD) shall be treated separately in ETP. Primary treated effluent shall be sent to CMEE (Common Multi-Effect Evaporator) of M/s. ACPTCL (Ankleshwar Cleaner Process Technology Centre Private Limited), Ankleshwar.
Washing 1.6 0 2.9 2.9
Primary treated effluent shall be sent to CETP (Common Effluent Treatment Plant) of M/s. ETL (Enviro Technology Limited), Ankleshwar after conforming to their inlet norms through tankers for final disposal.
Boiler 0.1 0 Note 1 Note 1
Note 1: Boiler blow down of 0.9 KLD shall be reused for washing purpose and then shall be given Primary treatment in ETP (Effluent Treatment Plant).
Cooling 0 0 Note 2 Note 2
Note 2: Cooling tower blow down of 2 KLD shall be reused for washing purpose and then shall be given Primary treatment in ETP.
Others -- -- -- -- --
Total Industria
l waste water
2.9 0 12.9 12.9
*Production quantity of one of the existing products (i.eHydrazide) shall be reduced from 45 MTM to 5 MTM and rest of the existing products shall be discontinued after proposed expansion.
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Presently, unit is a member of CETP of M/s. ETL, Ankleshwar for 2.9 KLD effluent disposal. Existing CETP load includes both Process & washing effluent. Existing COD load on CETP is between 5000 - 8500 mg/L. After proposed expansion, CETP hydraulic load will include only washing effluent. Therefore, COD load will be 1200 - 1500 mg/L. Because of proposed expansion, Pollution load on CETP will reduce.
iv Treatment facility within premises with capacity [For existing and Proposed]
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
For existing & Proposed expansion:
� ETP Capacity = 15 KLD (Consisting of Primary Treatment)
v Mode of Disposal & Final meeting point
Domestic: Sewage shall be disposed to soak pit via septic tank.
Industrial: Process effluent: Primary treated process effluent shall be sent to CMEE of M/s. ACPTCL (Ankleshwar Cleaner Process Technology Centre Private Limited), Ankleshwar. Washing effluent: Primary treated washing effluent shall be sent to
CETP (Common Effluent Treatment Plant) of M/s. ETL (Enviro
Technology Limited), Ankleshwar after conforming to their inlet
norms through tankers for final disposal.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE,
CHWIF etc.
Name of Common facility
� Name of Common facility:
1. CETP of M/s. ETL (Enviro Technology Limited), Ankleshwar
2. CMEE plant of M/s. ACPTCL (Ankleshwar Cleaner Process Technology Centre
Private Limited), Ankleshwar
Membership of Common facility (CF)
(For waste water treatment)
Unit is member of CETP of M/s. ETL, Ankleshwar.
And for CMEE plant of M/s. ACPTCL, the unit is under process of obtaining
membership.
vii Simplified water balance diagram with reuse / recycle of waste water
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vii Reuse/Recycle details (KLD)
[Source of reuse & application area]
Total reuse: 3 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.)
Boiler blowdown: 0.9
KLD &
Cooling tower blowdown:
2 KLD
Boiler blowdown of 0.9
KLD & Cooling tower
blowdown of 2 KLD shall
be reused for Washing
purpose.
COD: <100
BOD: <30
TDS: <500
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 MT/Day
Type of emissions
i.e. Air Pollutants
Air Pollution Control
Measures (APCM)
Existing
1 Boiler: 600 Kg/hr
11 Natural gas
200 m3/ day
PM
SO2
NOX
Adequate stack height is provided
Proposed
2
Thermic Fluid
Heater: 2 Lakh
Kcal/hr
11 Natural gas
800 m3/ day
PM
SO2
NOX
Adequate stack height
shall be provided
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3
D.G. set (standby): 250 KVA
11 Diese
l 40 L/h
Adequate stack height
shall be provided
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing & Proposed
Sr. no.
Specific Source of emission
(Name of the Product & Process)
Type of emission
Stack/Vent Height (meter)
Air Pollution Control Measures
(APCM)
Existing
There is no process emission from the existing manufacturing process.
Proposed
1
From Two stage water scrubber attached to Reaction vessel of 2,3 Dichloro 6 Nitro Aniline (DICONA)
NH3 15 Two stage Water
Scrubber
Final solution obtained from scrubber and their disposal:
18 – 20 % Ammonia solution generated from scrubbing of NH3 emission emitted from
the production of 2, 3 Dichloro 6 Nitro Aniline (DICONA)shall be sold to authorized
actual end users.
iii Fugitive emission details with its mitigation measures.
� Fugitive emission shall remain within permissible limit as handling of chemicals
will be in closed system.
F Hazardous waste
(as per the Hazardous and Other Wastes (Management and Transboundary
Movement) Rules 2016.
Existing & Proposed
i
Sr. no.
Type/ Name
of Hazardous waste
Specific Source of generation (Name of
the Activity, Product
etc.)
Category and
Schedule as per HW
Rules.
Quantity (MT/Annum)
Management of HW Exis
ting*
Haz. waste
qty after continuing one of the
existing product
s*
Proposed
Total
1 Used Oil
From Machinery
Category: 5.1 &
Sch: I
0.3 KL
0 1.8 KL
1.8 KL
Collection, Storage,
Transportation, Reuse & Disposal by
reusing within plant
and or selling it to
authorized
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agency.
2
Discarded Containers/ Bags and Liners
From Raw material
containers / bags
Category: 33.1
& Sch: I
5.7 MT
(380 nos.) 0.06 MT
(300 nos.)
0
36 MT
(2400 nos.)
12 MT
(60000
nos.)
36 MT
(2400
nos.) 12 MT
(60000
nos.)
Collection, Storage,
Transportation, Reuse,
Decontamination &
Disposal by reuse or selling to
registered re-processor.
3 Tarry Waste
During Production
of: Distillation process of Hydrzide;
2,3 Dichloro 6
Nitro Aniline
(DICONA); Nitro RF (O,O,O-Tris (4 -
nitrophenyl)
thiophosphate); 2, 4,
5-Trichloro Aniline; 1,8
Diamino Naphthalen
e; 1,5 Dinitro
Naphthalene & 1,8 Dinitro
Naphthalene
Category: 36.1
& Sch: I
3.6 0.3 87 87.3
Collection, Storage,
Transportation &Disposal to CHWIF/
Co-processing at
M/s. BEIL, Ankleshwar.
4
Chemical sludge from waste water treatment
From ETP
Category: 35.3
& Sch: I
NIL NIL 60 60
Collection, Storage,
Transportation&Disposal to common
TSDF facility at M/s. BEIL, Ankleshwar.
5 Spent Filter cloth
Filtration Process
Category: 36.2
NIL NIL 3 3 Collection, Stored in Bags in
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& Sch: I
separate place (shed with RCC flooring),
Transportation & sent to CHWIF of M/s. BEIL,
Ankleshwar
6
Off- spec product / raw material OR failed batch
--
Category: 28.4
& Sch: I
NIL NIL 6 6
Collection, Stored in
drums / bags in separate place (shed with RCC flooring),
Transportation and sent
for co-processing
OR to CHWIF of M/s. BEIL,
Ankleshwar.
7
Iron oxide sludge
During Production
of: Through
filtration & Washing step of 2-Amino-4-
chlorophenol & 4-
Amino-2-chlorophen
ol; Distillation step of 2,
4, 5-Trichloro Aniline &
1,8 Diamino
Naphthalene
Category: 26.1
& Sch: I
NIL NIL 1020 1020
Collection, Storage,
Transportation & disposed
to Co-processing
OR TSDF of M/s. BEIL,
Ankleshwar.
8 Spent Solvent
During production
of: Distillation
step of Hydrazide,
2,3 Dichloro 6
Category: 26.4
& Sch: I
NIL 49 1004 1053
Reused continuously in production
through distillation columns having
Primary and
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Nitro Aniline
(DICONA); Nitro RF (O,O,O-Tris (4 -
nitrophenyl)
thiophosphate); 1,5 Dinitro
Naphthalene & 1,8 Dinitro
Naphthalene
secondary condensers inbuilt with reactors
without any storage in
the premises
9
Ammonia Solution (18 – 20 %)
From water Scrubber
attached to Reaction vessel of
2,3 Dichloro 6
Nitro Aniline
(DICONA)
Category: A-10
& Sch: II
NIL NIL 660 660
Collection, Storage,
Transportation & Disposal by selling out to authorized
users who are having
authorization with valid
CCA and rule 9 permission
10
Sulphuric acid (70 - 72%)
During Production of: Nitration step of 1,5
Dinitro Naphthalen
e & 1,8 Dinitro
Naphthalene
Category: B-15
& Sch: II
NIL NIL 546 546
Collection, Storage,
Transportation & Disposal by selling out to authorized
users who are having
authorization with valid
CCA and rule 9 permission
*Production quantity of one of the existing products (i.eHydrazide) shall be reduced from 45 MTM to 5 MTM and rest of the existing products shall be discontinued after proposed expansion.
ii Membership details of TSDF, CHWIF etc.
(For HW management)
For existing Hazardous waste quantity,
unit is having the Membership of
CHWIF & TSDF of M/s. BEIL,
Ankleshwar.
For proposed additional Hazardous
waste, unit is under process of
obtaining membership.
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
Not Applicable
G Solvent management, VOC emissions etc.
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i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered
Solvents
� There shall be a dedicated solvent recovery system consisting of re-boiler
vessels, packed columns and primary and secondary condensers having cooling
water and chilled water as cooling media. Distillation shall be carried out at
atmospheric as well as vacuum conditions to obtain approx. 95-98 % of solvent
recovery and shall be reused.
� Spent Solvent generated from production of Hydrazide, 2,3 Dichloro 6 Nitro
Aniline (DICONA), Nitro RF (O,O,O-Tris (4 -nitrophenyl) thiophosphate), 1,5
Dinitro Naphthalene & 1,8 Dinitro Naphthalene shall be reused continuously in
production through distillation columns having Primary and secondary
condensers inbuilt with reactors without any storage at the premises.
ii VOC emission sources and its mitigation measures
� Handling of chemicals will be in closed system. Primary and secondary
condensers are proposed.
• Unit is having CCA of the Board for existing products. Total water consumption will be 25.90
KLD. Total wastewater generation will be 12.9 KLD.
• Process effluent: Primary treated process effluent shall be sent to CMEE of M/s. ACPTCL
(Ankleshwar Cleaner Process Technology Centre Private Limited), Ankleshwar.
• Washing effluent: Primary treated washing effluent shall be sent to CETP (Common Effluent
Treatment Plant) of M/s. ETL (Enviro Technology Limited), Ankleshwar after conforming to
their inlet norms through tankers for final disposal.
• Committee deliberated on area adequacy, waste water management, storage & handling of
Hazardous chemicals, VOC & LDAR etc.
• While discussing about the product profile in context to expansion of the project, PP requested
to allow them to continue existing product Hydrazine with 5 MTPM with total production
capacity unchanged. PP submitted revised Form-1 with relevant details.
• Committee observed that there is no change in water consumption, waste water generation
etc. due to proposed change in product profile.
• Committee also observed that waste water pollution load on CETP will be reduced due to
proposed expansion.
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.
• Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment
Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall
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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.
• Details with respect to justification for proposed expansion: (1) To address proportionate
availability of space for production plant. (2) To address proportionate availability of storage
area for raw materials finished goods, utilities and goods carrier movement within premises.
(3) To address proportionate captive/common infrastructure available to accommodate
additional load due to proposed expansion. (4) Environment impact and its mitigation
measures for common/ captive infrastructure due to proposed production.
• 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.
• Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent proposed
for use in-house with detailed chemical properties including vapor pressure. LDAR shall
endeavor prevention of losses of solvents to the best minimum extent.
• Feasibility report for reuse of process effluent for industrial purpose without proper treatment.
• Action plan for waste water generation considering 18 (1) (b) directions under the Water Act
1974 imposed by CPCB on CETP. Zero Liquid Discharge for waste water in addition to
consented quantity for discharge into CETP. Keeping in view quantity as well as quality of the
effluent
• Qualitative and quantitative analysis of hazardous waste streams generation from the
manufacturing process (Product wise). 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 shall be incorporated in EIA
report.
• 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 likeSulphuric acid, HCl, various solvents etc.
• Submit status of compliance of Environmental norms of Common Infrastructure.
• 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.
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• The project proponent shall have to apply for Environmental clearance through online portal
http://environmentclearance.nic.in/ along with final EIA report.
8. SIA/GJ/IND2/19749/2017 M/sRemik Chemicals Pvt. Ltd
Plot No. 3109 & 3110, GIDC – Panoli Dist.-Bharuch, Gujarat
Appraisal
Project / Activity No.: 5(f)
Project status: Expansion
• PP has submitted online application vide no. SIA/GJ/IND2/19749/2017dated 06/05/2018 for
obtaining Environmental Clearance.
• SEAC has recommended TOR to SEIAA and SEIAA has issued TOR to PP vide letter dated
06/09/2017.
• Project proponent has submitted EIA Report prepared by M/s: Envisafe Environment
Consultants, based on the TOR issued by SEIAA.
• This is an expansion unit and proposes for Synthetic Organic Chemicals manufacturing plant
as tabulated below:
Sr. No.
Name of Products CAS No. *Capacity (TPM) Use of
Product E P T
1. Aniline 2-4 Disulphonic Acid 137-51-9 Nil 50 – Real
base (71 As is)
50 – Real base
(71 As is)
Dyes Intermediate
2. Aniline 2-5 Disulphonic Acid 98-44-2 Nil 250 – Real
Base (313 As is)
250 – Real Base
(313 As is)
3. Tech. Sulphanilic Acid 121-57-3 100 400 500
4. Pure Sulphanilic Acid 121-57-3 Nil 200 200
5. Metanilic Acid 121-47-1 Nil 200 200
Total 100 1,100 1,200
• The project falls under Category B of project activity 5(f) as per the schedule of EIA
Notification 2006.
• Earlier, PP was called for presentation in the SEAC meeting dated 13/06/2018.
• During the meeting dated 13/06/2018, technical presentation made during the meeting by
project proponent. During the meeting, the project was appraised based on the information
furnished in the EIA Report and details presented during the meeting.
• The proposal is for expansion. This unit is having valid CC&A for existing unit. Copy of CC&A,
its compliance report is submitted. PP ensured that there are no court cases pending and no
public complaints against the project.
• After deliberation, it was unanimously decided to consider the project for further consideration
only after satisfactory submission of the following: (1) Certified Compliance Report (CCR)
from the Member Secretary, GPCB as per the MoEFCC’s Circular no. J-11011/618/2010- IA
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(II) (I) dated 30/05/2012 and Circular no. J-11013/6/2010-IA-II (Part) vide dated 07/09/2017.(2)
Exact source of Hazardous waste and its management as per the HW Rules 2016. (3)
Sources, quantification, APCM and management of bleed liquor for all type of process gas
emissions like SO3, Aniline, CO2 etc. (4) Adequacy of APCM for flue gas emission keeping in
view prevailing guidelines of GPCB. (5) Feasibility to reuse condensate waste water for
cooling purpose. (6) Adequacy of ZLD with quantitative and qualitative analysis of waste
water.
• PP submitted reply for the above mentioned additional details vide their letter dated
19/11/2018
• PP was called for presentation in the SEAC meeting dated 28/11/2018.
• Salient features of the project are as under:
Sr.
no. Particulars Details
A Total cost of Proposed Project(Rs. in Crores):
Existing: 0.86
Proposed: 9.14
Total: 10.00
(1) Capital cost for EMS (Environmental Management System):2.51 Crore
Recurring cost towards the environmental protection measures: 1.18 Crore/Annum.
B Total Plot area (sq. meter) 3,000
Green belt area,/Tree Plantation area (sq.
meter)
Existing: 300
Proposed: 700
Total: 1,000
C Employment Generation Existing: 10
Proposed: 80
Total: 90
D Water[Existing & Proposed]
i
Source of Water Supply
(GIDC Bore well, Surface water etc...)
GIDC
Status of permission from the concern authority: Water is sourced from GIDC water supply
and the same source will be utilized after proposed expansion project.
ii Water consumption (KL/day)
-
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 1.0 6.0 7.0 Fresh
(B) Gardening 0.5 2.5 3.0 Fresh
(C) Industrial
Process & APCM 2.4 24.6 27.0 Fresh
Nil 73.0 73.0 Reuse
Boiler Nil 54.0 54.0 Fresh
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Cooling 1.0 56.0 57.0 Fresh
Nil 23.0 23.0 Reuse
Washing Nil 5.0 5.0 Reuse
Total Industrial Water
Requirement (C)
3.4 235.6 239.0 Fresh + Reuse
3.4 134.6 138.0 Fresh
Total Water
Requirement(A+B+C) 4.9 143.1 148 Fresh
(1) Total Water Requirement for the Project: 249 KLD
(2) Quantity to be recycled/reused: 101 KLD
(3) Total Fresh water requirement: 148 0KLD
-
iii Waste water generation (KL/day)
-
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 1.0 4.0 5.0
(B) Gardening Nil Nil Nil
(C) Industrial
Process & APCM Nil 127 127
Boiler Nil 3.0 3.0
Cooling Nil 20.0 20.0
Washing Nil 5.0 5.0
Total Industrial
Effluent Generation Nil *155 *155 Generation
Total Industrial
Effluent Discharge Nil *Nil *Nil ZLD
*Difference of 54 KLD between Generation and Reuse is accounted as under:
Gypsum Sludge: 34.4 TPD, Sodium Sulphate Sludge: 1.1 TPD, MEE Salt: 0.5 TPD,
Solid Waste (Organic): 12 TPD. Atmospheric Loss: 6
-
iv Treatment facility within premise with capacity
(ETP, CETP, MEE, STP etc).
ETP: 35 KLD (Hy. Load: 28 KLD)
MEE: [3 Nos. x 50 KLD (Hy. Load: 120 KLD)]
ATFD: [3 Nos. x 103 kg/hr (Hy. Load: 248 kg/hr)]
v Mode of Disposal & Final meeting point
Domestic: To soak pit through septic tank
Industrial: • Low COD/TDS stream from Utilities and washing will be treated in existing
ETP. Treated effluent from ETP will be sent to MEE for further treatment.
• High COD/TDS stream from process will be sent to MEE.
• Condensate from MEE will be re-used in manufacturing process, cooling
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and washing. Hence, unit will maintain 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) --
vii Simplified water balance diagram with reuse / recycle of waste water
viii Reuse/Recycle details (KL/day)
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
MEE: 101
Process &
APCM: 96
Washing: 5
400 800 180
E Air (Existing & Proposed)
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i Flue gas emission details (No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz.
TPH, Kcal/hr, MT/hr, KVA etc.)
-
Sr.
No.
Source of
Enission with
Capaity
Stack
Height &
Dia. (m)
Fuel Name
& Qty.
Type of
emission&
Permissible
Limit
Air Pollution Control
Measures
1 Steam Boiler
(6 TPH)
25.0 &
Dia.1.0
Bio-fuel
(Agro waste)
&/OR
Coal
(17.5 TPD)
PM ≤ 150
mg/Nm3
SO2 ≤ 100
ppm
NOx ≤ 50
ppm
Multicyclone
Separator followed by
Bag filter
2
Thermic
Fluid Heater
(3 Lac Kcal/hr)
10.0 &
Dia.0.5
Natural Gas
(595 SCM/Day)
Stack of Adequate
height
3
DG Set
(300 KVA),
Stand-by
7.0&
Dia.0.15
Diesel
(65 Lit/hr)
Adequate stack height
as per CPCB
Guidelines
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
-
Sr.
No
.
Source of
Emission Status
Ht. &
Dia. (m)
Air Pollution Control
Equipment
Type of
Emission
&Permissible
Limit 1st Stage 2nd Stage
1. Ball Mill Existing 9.0 &
Dia. 0.2
Wet/ Acid
Scrubber
(A)
-- PM ≤ 150
SO2 ≤ 40
2. All
Reactors Proposed
9.0 &
Dia. 0.2
Alkali
Scrubber
(B)
Alkali
Scrubber
(C)
SO2 ≤ 40
-
iii Fugitive emission details with its mitigation measures[Existing & Proposed]
There are chances of fugitive emission and odour nuisance during manufacturing process as
well as due to storage & handling of raw materials and products in existing as well as
expansion phase.The unit has taken following precaution for the control of fugitive emission
and same will be adopted 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.
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• Dedicated measuring tanks will be provided to each
reactor.
• Usage of closed handling system for odorous
chemicals /solvents as far as possible.
Emission from bulk storage
tanks during storage, loading,
unloading
• Bulk storage of odorous chemicals will be adopted and
usage of drums/Carboys for such materials are avoided
as far as possible.
• PSVs, Rupture disc, Vapor recovery system will be
installed for process/storage tank vents.
Hazardous chemical storage
area
• Dedicated storage area will be provided
• Adequate ventilation systems will be provided
• All the containers will be kept tightly closed
• Trolley/Forklift will be used for transfer of drums and
containers
• Transfers of odorous waste are carried out preferably
during day time. Transfers during odd hours are
avoided.
Chemical vapor from wet
cake in filtration and drying
area
• Covered transfer systems will be adopted, workers will
be provided with PPE.
• Fume extraction systems will be provided, wherever
required.
Pump and compressor
Emissions
• Mechanical seals will be provided in pumps and
agitators
• Standby arrangement for critical equipment and parts
will be ensured.
• Drip trays will be placed for each pump to collect
leakages and spillages.
Valves, Flanges, plugs and
instrument connections
• Welded pipes will be used wherever feasible.
• Suitable gasket materials will be used.
• Suitable glad packing will used in valves.
• Periodic inspection and maintenance of pipes and pipe
fittings will be carried out.
Release from sampling lines • Closed loop system is used.
F Hazardous waste [Existing & Proposed]
(As per the Hazardous and Other Wastes (Management and Transboundary Movement)
Rules 2016.
i -
Type of
waste
Source of
generation Category
*Quantity per
Annum Method of Disposal
E P T
ETP
Sludge ETP
Sch-1
35.3
- 45
MT
45
MT Collection, Storage,
Transportation, Disposal by
landfilling at TSDF MEE Salt MEE - 155
MT
155
MT
Gypsum ETP - 10,725 10,725 Collection, storage and send to
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Sludge (Prod. 1 &
2)
MT MT cement industry for co-
processing on priority, if not
available Disposal by landfilling
at TSDF
Sodium
Sulphate
Sludge
MEE
(Prod. 5) -
355
MT
355
MT
Collection, Storage,
Transportation, Disposal by Sale
to authorized end-user having
permission under Rule 9 on
priority, if not available Disposal
by landfilling at TSDF
Solid
Waste
(Organic)
MEE/ATFD
(Prod. 1, 2
& 5)
- 3,715
MT
3,715
MT Collection, storage and send to
cement industry for co-
processing on priority, if not
available Disposal by
incineration at CHWIF
Spent
Carbon
Mfg.
(Prod 4)
Sch-1,
26.1 -
265
MT
265
MT
Solid
Waste
(Organic)
Mfg.
(Prod. 2)
Sch-1,
26.1 -
675
MT
675
MT
Iron
Sludge
Mfg.
(Prod. 5)
Sch-1,
26.1 -
1055
MT
1055
MT
Collection, Storage,
Transportation, Disposal by
landfilling at TSDF
Crude
Sulphanilic
Acid
Mfg.
(Prod. 3)
Sch-1,
26.1 -
167
MT
167
MT
Collection, Storage and Captive
Re-use in Manufacturing of
Tech. Sulphanilic Acid
Sodium
Sulphate
[Avg 23%
(20-25%)]
Mfg.
(Prod. 4),
APCE (Prod
1, 2, 5)
Sch-1,
26.1 -
1,935
MT
1,935
MT
Collection, Storage,
Transportation, Disposal by Sale
to authorized end user having
permission under Rule 9 on
priority, if not available Treated
along with effluent in MEE
Process
Waste
(Gypsum)
Mfg.
(Prod. 5)
Sch-1,
26.1 -
1,465
MT
1,465
MT
Collection, storage and send to
cement industry for co-
processing on priority, if not
available Disposal by landfilling
at TSDF
Discarded
Drums /
Bags
RM Storage
& Handling
Sch-1,
33.1
4.50
MT
18.50
MT
23
MT
Collection, Storage,
Decontamination and Disposal
by selling to scrap vendors
Spent Oil /
Used Oil
Plant &
Machineries
Sch-1,
5.1
0.01
KL
0.05
KL
0.06
KL
Collection, Storage,
Transportation, sell to registered
Re-processor / MoEF&CC
approved recyclers on priority, if
not available Reuse as
Lubricant within premises
*E-Existing, P-Proposed, T- Total after Proposed expansion
-
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454th meeting of SEAC-Gujarat, Dated 28.11.2018
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ii Membership details of TSDF, CHWIF etc. Unit will obtain membership from GPCB
approved TSDF / CHWIF
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
-
G Solvent management (If any)
I Details of Solvent recovery (As per respective
ToR)
Not applicable since, there is no solvent
requirement for the proposed expansion
project.
ii VOC emission sources and its mitigation
measures
As mentioned in section E (iii) above.
• During the meeting dated 28/11/2018, technical presentation made by project proponent.
• Committee noted that there is no partially complied or non-complied conditions as per the
Certified Compliance Report (CCR) dated 05/10/2018 received from GPCB on 23/10/2018.
• Revised Hazardous waste management matrix is submitted. However, PP has not explored
environmental friendly method of disposal for Gypsum sludge.
• Complete details regarding APCM for flue gas & process gas emission with adequacy report
is submitted.
• PP now proposes to reuse condensate waste water for Process & APCM in place of cooling
tower. However, PP has not submitted feasibility report for reuse of waste water.
• Adequacy certificate for ZLD prepared by M/s. Darshan Institute of Engineering & Technology
is submitted along with the EIA Report.
• Total water consumption will be 16.8 KLD. Total wastewater generation will be 249 KLD.
• 155 KLD effluent will be given primary treatment in ETP and then sent it to MEE for further
treatment and disposal.
• 101 KLD MEE condensate will be reused back in process.Agro waste and or coal will be
used as fuel for proposed boiler.
• 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 Nov ’17 – Jan ‘18. Ambient Air Quality monitoring was carried out for
PM10, PM2.5, SO2, NOx, HCl, Cl2, HBr, NH3, CO and VOC at six locations, including the
project site. Values conform to the prescribed standards for Ambient Air Quality. The
incremental Ground Level Concentration (GLC) has been computed using ISCST3. The
resultant concentrations are within the NAAQS. Colour, turbidity, dissolved solid, alkalinity,
total hardness; calcium, magnesium, chlorides, Sulphate, and Boron were found above
desirable limits in some of Surface water and ground water samples. Turbidity was found
exceeding the permissible limit in 1 surface water sample whereas dissolved solids, total
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454th meeting of SEAC-Gujarat, Dated 28.11.2018
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hardness, magnesium and chlorides were found exceeding the permissible limit in 3 ground
water samples.
• 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.
• Committee deliberated on reply submitted & presentation made by PP.
After deliberation, it was unanimously decided to consider the project for further appraisal
only after satisfactory submission of the revised EIA report.
1. Unit shall explore the possibilities for environment friendly method for disposal of Gypsum
waste, Land-fillable wastes and Incinerable hazardous wastes.
2. Feasibility to reuse condensate waste water for Process & APCE. Give separate quantity of
water consumption and waste water generation.
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. Shri V. N. Patel, Member, SEAC
4. Shri. R. J. Shah, Member, SEAC
5. Shri A.K.Muley, Member, SEAC
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