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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
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Minutes of the 446th meeting of the State Level Expert Appraisal Committee held on 29/10/2018
at Committee Room, Gujarat Pollution Control Board, Sector 10-A, Gandhinagar.
The 446h meeting of the State Level Expert Appraisal Committee (SEAC) was held on 29th October
2018 at Committee Room, Gujarat Pollution Control Board, Sector 10-A, Gandhinagar. Following
members attended the meeting:
1. Shri S. C. Srivastav, Vice Chairman, SEAC
2. Shri V. N. Patel, Member, SEAC
3. Shri R. J. Shah, Member, SEAC
4. Shri A.K. Muley, Member, SEAC
The additional agenda of TOR/Scoping cases and Appraisal was taken up. The applicants made
presentations on the activities to be carried out along with other details furnished in the Form-1, PFR,
EIA-EMP reports and other reports.
6. IA/GJ/IND2/65259/2017 M/s Indian Oil Corporation Limited. (IOCL)
Kandla Foreshore Terminal Near Booster
Station.
PO – Old Kandla, District –Kutch, Taluka
Gandhidham, Gujarat-370210
Appraisal
Project / Activity No.: 6(b)
Project status: Expansion
• PP has submitted online application vide no. IA/GJ/IND2/65259/2017 of dated 04/10/2018 for
obtaining Environmental Clearance.
• MoEf & CC has issued TOR to PP vide letter No: IA-J-11011/318/2017-IA-II(I) Date: 17/08/2017.
• Project proponent has submitted EIA Report prepared by M/s Engineers India Limited based on the
TOR issued by SEIAA.
• This is an expansion unit and proposes for expansion of isolated storage and handling of Hazardous
chemicals plant as tabulated below:
Sr.
no.
Name of the
Hazardous
chemicals
for storage
Storage details
Quantity
MT/Month End-use
of the
products Existing Proposed Total
1 MS Existing: 6 tanks
Proposed: Nil tank
66080 KL
6 tanks
- 66080 KL
6 tanks
Motor
Spirit
2 HSD Existing: 9 tanks 214386 KL - 214386 KL Diesel
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Proposed: Nil tank 9 tanks 9 tanks
3 SKO Existing: 2 tank
Proposed: Nil
47500 KL
2 tank
- 47500 KL
2 tank
Kerosene
4 ATF Existing: 3 tanks
Proposed: Nil
71298 KL
3 tanks
- 71298 KL
3 tanks
ATF
5 Naphtha Existing: 4 tanks
Proposed: Nil tank
94246 KL
4 tanks
- 94246 KL
4 tanks
Naphtha
5 Ethanol Existing: 3 tanks
Proposed: 3 tanks
110 KL
3 tanks
600 KL
3 tanks
710 KL
6 tanks
Ethanol
• The project falls under Category B of project activity 6(b) as per the schedule of EIA Notification
2006.
• PP was called for presentation in the SEAC meeting dated 29/10/2018.
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing: NA
Proposed: 2.8 crores
Total: 2.8 crores
B Total Plot area
( sq. meter)
Existing: 146 acre (590841sq. m)
Proposed: Nil
Total: 146 acre (590841 sq. m)
Green belt area,/Tree Plantation area
( sq. meter)
Existing: 2.0 acre (8093.71 sq. m)
Proposed: Nil
Total: 2.0 acre (8093.71 sq. m)
C Employment generation Existing: 75
Proposed: Nil
Total: 75
D Water
i
Source of Water Supply (GIDC Bore well,
Surface water, Tanker supply etc...)
Gujarat Water Supply and Sewerage Board
Status of permission from the concern
authority.
Pipeline connection from Gujarat Water Supply and
Sewerage Board
ii
Water consumption (KLD)
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Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 8 Nil 8
(B) Gardening - - -
Industrial
Process - - -
Washing 3 - 3
Boiler - - -
Cooling - - -
Others - - -
Industrial Total 11 - 11
Grand Total (A+B+C) 11 - 11
1) Total water requirement for the project: Nil. The water requirement will be adjusted from
existing water supply i.e. 11 KLD available to Kandla Fore Shore terminal.
2) Quantity to be recycle: 8 KLD
3) Total fresh water requirement: 11 KLD.
iii
Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 6 - 6
Industrial
Process - - -
Washing 2 Intermittent 2
Boiler - - -
Cooling - - -
Others - - -
Total Industrial
waste water
8 - 8
-
iv Treatment facility within premises with
capacity
[ETP (Primary, Secondary, Tertiary), MEE,
ETP of 120 m3/day
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Stripper, Spray Dryer, STP etc].
v Mode of Disposal & Final meeting point
Domestic: Soak pit
Industrial: The treated water is used inside the
terminal for gardening purpose.
vi In case of Common facility (CF) like CETP,
Common Spray dryer, Common MEE etc. ,
name of CF
Not Applicable
Membership of CF Not Applicable
vii Reuse/Recycle details (KLD) 8 KLD
E Air [Existing & Proposed]
i Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
Diesel consumption in the terminal is 65 Litre/Day.
SR.
no.
Source of
emission
With Capacity
Stack
Height
Type
of
Fuel
Quantity
of Fuel
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air Pollution
Control
Measures
(APCM)
1 DG-500 KVA 16 M HSD 5
Litre/Day SO2, NOx
Acoustic
enclosures
2 DG-500 KVA 16 M
HSD 5
Litre/Day SO2, NOx
Acoustic
enclosures
3 DG-500 KVA 16 M
HSD 5
Litre/Day SO2, NOx
Acoustic
enclosures
4 DG-500 KVA 16 M
HSD 5
Litre/Day SO2, NOx
Acoustic
enclosures
5 Fire Engine-1 &
2 (358 KW) 11 M HSD
15
Litre/Day SO2, NOx
Acoustic
enclosures
6
Fire Engine
3,4,5,6,7 (261
KW)
11 M HSD 30
Litre/Day SO2, NOx
Acoustic
enclosures
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
[Existing & Proposed]
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Sr.
no.
Source of
emission
Type of
emission
Stack/Vent
Height
(meter)
Air Pollution Control
Measures
(APCM)
1 DG Stack SO2,
NOx
As per serial
no E (i) As per Serial no E (i)
-
iii Fugitive emission details with its mitigation measures.
[Existing & Proposed]GAs below:
Fugitive emission will be identified through LDAR program and adequate mitigation measures will
be taken.
iv VOC emission sources and its mitigation measures
Proposed Ethanol tanks are above ground horizontal tanks. Only one tank will be operated for
receipt as per present practice. Therefore there will not be any increase in quantity of emission
from present limit.
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
1 Chemical
Sludge from
ETP
ETP 35.3 24 MT/Year Collection, storage,
Transportation and
Disposal by selling out to
authorized recycler
2 Used Oil DG sets 5.1 1.5 MT/Year Collection, storage,
transportation, and
disposal at TSDF
ii Membership details of TSDF, CHWIF etc. Saurashtra Enviro Project Pvt. Ltd.
iii Details of Non-Hazardous waste & its
disposal (MSW and others)
All hazardous waste will be given to Saurashtra
Enviro Project Pvt. Ltd. for safe disposal.
• During the meeting dated 29/10/2018, technical presentation made by project proponent.
• At present unit is engaged in isolated storage and handling of Hazardous chemicals for which they
have obtained CC&A of the Board. The proposal is for expansion of isolated storage and handling of
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Hazardous chemicals.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for expansion of existing unit and for now proposes isolated storage and handling of
Hazardous chemicals. This unit is having valid CC&A for existing unit. Copy of CC&A, CC&A
compliance report is submitted. PP ensured that there are no court cases pending and no public
complaints against the project.
• Total water consumption will be 11 KLD. Total wastewater generation will be 8 KLD. After proposed
expansion, there will be no change in industrial and domestic waste water generation i.e. 8 KLD.
• 8 KLD treated effluent will be used for gardening purpose within premises..
• HSD will be used as fuel for DG set and fire engine..
• 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
xbeen conducted for the study area of 10 km radial distance from project site for the period March -
April, 2018. site will remain within the National Ambient Air Quality Standards (NAAQS).
• Risk assessment including prediction of the worst-case scenario and maximum credible accident
scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site
Emergency Plan has been covered in the RA report.
Discussions & Conclusion:
• Committee noted that proposal is for enhancement of the storage tank capacity for Ethanol. It is
noted that three Above Ground Horizontal tanks of Ethanol each of 200 KL (Total capacity of 600 KL)
are proposed to be installed. PP has obtained TOR from MOEF&CC where in PP is asked to conduct
Public hearing. Asking for details of Public hearing, PP mentioned that they approached MOEF&CC
for amendment in TOR to which MOEF&CC generated EDS on 10/09/2018 vide proposal NO:
IA/GJ/IND2/65259/2017 asking PP “ To refer Ministry’s OM dated 27th April 2018 providing
exemption from public consultation/ Hearing for the projects/Activities located within the industrial
areas/estates/parks and required to submit the proposal for environmental clearance accordingly to
the concerned authority (SEIAA/ MoEF&CC). Referring to this, PP was asked to submit the details of
status of notified area wherein the storage capacity enhancement is proposed. It is also noted that
proposed expansion is within the existing premises and location is within notified area, hence PP
mentioned that applicability of CRZ notification 2011 does not exist.
• Considering the proposed expansion, compliance of CCA conditions, action under various
environmental rules/acts by GPCB, public compliant/litigation pending against the unit were
discussed at length. Committee also deliberated safety measures proposed by the unit for the
additional tanks as well as for the existing facilities.
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• During appraisal, committee noted that air quality is not within the NAAQ 2009 at villages Tuna,
Galpadar, Kund.
Committee deliberated compliance of the TOR issued and asked PP to submit following details so as
to consider the proposal in one of the upcoming SEAC meeting for further consideration.
1. Detailed safety measures including SOP being implemented for existing facilities and also for the
proposed tanks for ethanol to prevent accidents.
2. Need based budgetary outlay of CER as per the OM of MOEF&CC dated 01/05/2018.
3. To address the ambient air quality at the villages Tuna, Galpadar and Kand and associated
mitigation measures to reduce GLC along with the conclusion based on air Model study.
4. Revised environmental management plan (EMP) with budgetary provision of capital cost and recurring
cost after incorporating additional environmental mitigation measures.
7. SIA/GJ/IND2/29117/2018
M/s Indian Oil Corporation Limited
Plot no- Moje Ichhapore – SR No. 270/3 &
Moje Kawas SR No. 32/P, PO – Ichhapore,
Hazira Road, District – Surat Gujarat-394510
Appraisal
Project / Activity No.: 6(b)
Project status: Expansion
• PP has submitted online application vide no. SIA/GJ/IND2/29117/2018 of dated 04/10/2018 for
obtaining Environmental Clearance.
• SEIAA has issued TOR to PP vide letter No: SEIAA/GUJ/TOR/6(b)/893/2018 dated 28/08/2018.
• Project proponent has submitted EIA Report prepared by M/s Engineers India Limited based on the
TOR issued by SEIAA.
• This is an expansion unit and proposes for expansion of isolated storage and handling of Hazardous
chemicals plant as tabulated below:
Sr.
no.
Name of the
Hazardous
chemicals
for storage
Storage details Quantity
MT/Month
End-use
of the
products Existing Proposed Total
1 MS BS-IV Existing: 7 tanks
26771 KL
7 tanks
- 26771
KL
7 tanks
Motor
Spirit
2 HSD BS-IV Existing: 5 tanks
Proposed: 2
23019 KL
5 tanks
16000 KL
2 tanks
39019
KL
Diesel
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tanks 7 tanks
3 SKO Existing: 1 tank
5639 KL
1 tank
- 5639
KL
1 tank
Kerosene
4 LSHFHSD Existing: 2 tanks
1798 KL
2 tanks
- 1798
KL
2 tanks
High
Speed
Diesel
5 Ethanol Existing: 8 tanks
499 KL
8 tanks
- 499 KL
8 tanks
Ethanol
• The project falls under Category B of project activity 6(b) as per the schedule of EIA Notification
2006.
• PP was called for presentation in the SEAC meeting dated 29/10/2018.
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing: Not Applicable
Proposed:12 crores
Total: 12 crores
B Total Plot area
( sq. meter)
Existing: 125 acre (505857 sq. m)
Proposed: Nil
Total: 125 acre (505857 sq. m)
Green belt area,/Tree Plantation area
( sq. meter)
Existing: 13.2 acre (53418.5 sq. m)
Proposed: Nil
Total: 13.2 acre (53418.5 sq. m)
C Employment generation Existing: 41
Proposed: Nil
Total: 41
D Water
i
Source of Water Supply (GIDC Bore well, Surface
water, Tanker supply etc...)
Water thru pipeline from Singapore Weir of
KRBC Division, Surat.
Status of permission from the concern authority.
Permission taken.
ii
Water consumption (KLD)
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Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 21 Nil 21
(B) Gardening - - -
Industrial
Process - - -
Washing 5 - 5
Boiler - - -
Cooling - - -
Others - - -
Industrial Total 26 - 26
Grand Total (A+B+C) 26 - 26
1) Total water requirement for the project: Nil (The water requirement will be adjusted from
existing water supply)
2) Quantity to be recycle: 21 KLD
3) Total fresh water requirement: 21 KLD
iii
Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 17 - 17
Industrial
Process - - -
Washing 3 Intermittent 3
Boiler - - -
Cooling - - -
Others - - -
Total Industrial
waste water
20 - 20
-
iv Treatment facility within premises with capacity
[ETP (Primary, Secondary, Tertiary), MEE, Stripper,
ETP of 10 m3/hr capacity
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Spray Dryer, STP etc].
v Mode of Disposal & Final meeting point Domestic: Soak pit
Industrial: treated effluent will be used
in gardening of the terminal
vi In case of Common facility (CF) like CETP, Common
Spray dryer, Common MEE etc. , name of CF
Not Applicable
Membership of CF Not Applicable
vii Reuse/Recycle details (KLD) 20 KLD
E Air [Existing & Proposed]
i Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
Average Diesel consumption in the terminal is 165 Litre/Day.
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 DG-500 KVA 8 M HSD 85
Litre/Hr SOx, NOx
Acoustic
enclosures
2 DG-500 KVA 8 M
HSD 85
Litre/Hr SOx, NOx
Acoustic
enclosures
3 DG-500 KVA 8 M HSD 85
Litre/Hr
SOx, NOx Acoustic
enclosures
4 DG-380 KVA 8 M HSD 80
Litre/Hr
SOx, NOx Acoustic
enclosures
5 Fire Engine-
480 HP 8 M HSD
80
Litre/Hr SO2, NOx -
6 Fire Engine-
480 HP 8 M HSD
80
Litre/Hr SO2, NOx -
7 Fire Engine-
480 HP 8 M HSD
80
Litre/Hr SO2, NOx -
8 Fire Engine-
480 HP 8 M HSD
80
Litre/Hr SO2, NOx -
9 Fire Engine-
480 HP 8 M HSD
80
Litre/Hr SO2, NOx -
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-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
[Existing & Proposed]
Sr. no. Source of
emission
Type of
emission
Stack/Vent
Height
(meter)
Air Pollution
Control
Measures
(APCM)
1 DG Stack SOx,
NOx
As per serial
no E(i)
As per Serial no
E(i)
-
iii Fugitive emission details with its mitigation measures.
[Existing & Proposed]GAs below:
Fugitive emission will be identified through LDAR program and adequate mitigation measures will
be taken.
iv VOC emission sources and its mitigation measures
Proposed HSD tanks are tanks are Cone Roof Tanks. Only one tank will be operated for receipt
at one time as per present practice. Therefore there will not be any increase in quantity of
emission from present limit.
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
1 ETP Waste ETP 34.3 18 KL/Year TSDF
2 Used Oil DG sets 5.1 0.950 MT/Year Registered
re-processors
3 Oil residue Pumps 3.1 0.750 MT/Year Registered
re-processors
4 Discarded
container
Oil
container
33.3 120 nos./year Authorized
recyclers
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Quantity of discarded containers must be in MT/Annum.
ii Membership details of TSDF, CHWIF etc. GPCB approved TSDF sites.
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
Nil
• During the meeting dated 29/10/2018, technical presentation made by project proponent.
• At present unit is engaged in isolated storage and handling of Hazardous chemicals for which they
have obtained CC&A of the Board. The proposal is for expansion of isolated storage and handling of
Hazardous chemicals.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for expansion of existing unit and for now proposes isolated storage and handling of
Hazardous chemicals. This unit is having valid CC&A for existing unit. Copy of CC&A, CC&A
compliance report is submitted. PP ensured that there are no court cases pending and no public
complaints against the project.
• Total water consumption will be 21 KLD. Total wastewater generation will be 20 KLD. After proposed
expansion, there will be no change in industrial and domestic waste water generation i.e. 20 KLD.
• 20 KLD treated effluent will be used for gardening purpose within premises..
• HSD will be used as fuel for DG set and fire engine..
• 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 January -
March, 2018. Risk assessment including prediction of the worst-case scenario and maximum credible
accident scenarios has been carried out. The detail proposed safeguard measures including On-Site
/ Off-Site Emergency Plan has been covered in the RA report.
Discussions & Conclusion:
• Committee noted that proposal is for enhancement of the storage tank capacity for HSD. It is noted
that two additional tanks of HSD each of 8000 KL (Total capacity of 16000 KL) are proposed to be
installed. Committee noted that TOR was issued by SEIAA vide letter No:
SEIAA/GUJ/TOR/6(b)/893/2018 dated 28/08/2018 including exemption of public hearing.
• Considering the proposed expansion, compliance of CCA conditions, action under various
environmental rules/acts by GPCB, public compliant/litigation pending against the unit were
discussed at length. Committee also deliberated safety measures proposed by the unit for the
additional tanks as well as for the existing facilities.
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Committee deliberated compliance of the TOR issued and asked PP to submit following details so as
to consider the proposal in one of the upcoming SEAC meeting for further consideration.
1. Detailed safety measures including SOP being implemented for existing facilities and also for the
proposed tanks for HSD to prevent accidents.
2. Need based budgetary outlay of CER as per the OM of MOEF&CC dated 01/05/2018.
3. Revised environmental management plan (EMP) with budgetary provision of capital cost and recurring
cost after incorporating additional environmental mitigation measures.
8. SIA/GJ/IND2/19407/2017 M/s. Grasim Industries Ltd
Plot No. -1, GIDC Industrial Estate, P.O.-
Vilayat, Taluka-Vagra, District-Bharuch.
Appraisal
Project / Activity No.: 1(d)
Project status: Expansion
• PP has submitted online application vide no. SIA/GJ/IND2/19407/2017 of dated 11/07/2017 for
obtaining Environmental Clearance.
• SEIAA has issued TOR to PP vide letter No: SEIAA/GUJ/TOR/1(d)/890/2017 vide dated 29-09-2017.
• Project proponent has submitted EIA Report prepared by M/s Anand Environnemental Consultants
Pvt. Ltd based on the TOR issued by SEIAA.
• This is an expansion unit and proposes for expansion of thermal power plant as tabulated below:
Sr.
No.
Name of Product CAS
no.
Quantity
MT/Month
End-use of product
Existing Proposed Total
1. Captive Power Plant
(CPP)
-- 96
MW
45
MW
141
MW
Power Generation
for self use
By-Product
NIL
• The project falls under Category B of project activity 1(d) as per the schedule of EIA Notification
2006.
• PP was called for presentation in the SEAC meeting dated 29/10/2018.
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing: 500 Crores
Proposed: 250 Crores
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Total: 750 Crores
B Total Plot area
( sq. meter)
Existing: 350000 sq. m
Proposed: 69750 sq. m
Total: 419750 sq. m
Green belt area,/Tree Plantation area
( sq. meter)
Existing: 115500 sq. m
Proposed: 23017.5 sq. m
Total: 138517.5sq. m
C Employment generation
Existing:
Proposed:
Total:
Direct
110
30
140
Indirect
--
20
20
D Water
i
Source of Water Supply (GIDC Bore well, Surface
water, Tanker supply etc...)
GIDC
Status of permission from the concern authority. Yes
ii
Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 5.5 2.5 8
(B) Gardening
* * *
* Treated domestic
wastewater will be used
for gardening
(C) Industrial
Process -- -- --
Washing 50 25 75**
Boiler 6450 3100 9550 Boiler make up water
Cooling 4000 1875 5875 Cooling make up water
Others 750 500 1250 DM water regeneration
Industrial Total 11250 5500 16750
Grand Total
(A+B+C) 11255.5 5502.5 16758
**Wash water includes Air pressure preheater/Plant wash down water/floor washing and equipment
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drain/grey water washing /seepage of ash water/bottom ash handling system
1) Total water requirement for the project: 16758KLD
2) Quantity to be recycle: 11642 KLD& 1443 KLD reuse
3) Total fresh water requirement: 5116KLD
iii
Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 4.4 2 6.4
(B) Industrial
Process 0 0 0
Washing 50 25 75
Boiler 2500 1180 3680 Boiler blow down
Cooling 1500 710 2210 Cooling purge
Others 750 500 1250 DM water regeneration
Total Industrial waste
water 4800 2415 7215
Grand Total (A+B) 4804.4 2417 7221.4
-
iv Treatment facility within premises with capacity [For existing and Proposed]
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
• Effluent generated from industry will be treated in our existing effluent treatment plant (capacity-
500 m3/day x2)
Treated effluent will be reused for cooling make-up and RO reject will be used for Dust
suppression in coal handling area, Sprinkling on fly ash, road cleaning.
• Domestic sewage will be treated in STP and treated wastewater will be reused for gardening
within premises.
v Mode of Disposal & Final meeting point
Domestic: GIDC -drainage line ultimately disposal into deep sea.
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Industrial: Zero discharge
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility
Not applicable, since our Effluent generated from industry and domestic will be treated in our
existing effluent treatment plant
Membership of Common facility (CF)
Not applicable, since our Effluent generated from industry and domestic will be treated in our
existing effluent treatment plant
vii Reuse/Recycle details (KLD)
5870 kl/day steam condensate will be recycled back for boiler make-up, 5772 kl/day treated
wastewater will be recycled for cooling make-up and 1443 kl/day RO reject will be reused for Dust
suppression in coal handling area, sprinkling on fly ash and road cleaning.
70% reduction in fresh water consumption by various recycle and reuse of treated wastewater
E Air
i Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
Existing & Proposed
Sr.
no.
Source of
emission
With
Capacity
Stack
Height
(meter)
Name
of the
fuel
Quantity
of Fuel
MT/hr&
MT/Day
Type of
emissions
i.e. Air
Pollutants
Air Pollution
Control
Measures
(APCM)
Existing*
1. Boiler 1 & 2
(2 x 175 TPH)
125 Coal
100
MT/hr
SPM
SO2
NOx
ESP and Low
NOx burners
2. Boiler 3 & 4
(2 x 175 TPH)
125 SPM
SO2
NOx
ESP and Low
NOx burners
Proposed
3. Boiler-5 125 Coal 29.16M SPM ESP and Low
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(175 TPH) T/hr SO2
NOx
NOx burners
-
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
Existing & Proposed
-
Sr.
no.
Source of
emission
Type of
emission
Stack/Vent
Height (meter)
Air Pollution
Control Measures
(APCM)
1 Not Applicable
-
iii Fugitive emission details with its mitigation measures.
All possible preventive measure taken to control / minimize the Fugitive emissions
F Hazardous waste
(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules
2016.
Existing & Proposed
i
Sr.
No.
Type/Name
of
Hazardous
waste
Source of
generation
Category
and
Schedule
as per
HW
Rules.
Quantity
(MT/Annum)
Mode of Disposal**
Existing Proposed Total
1. ETP
Sludge
ETP 35.3 5
MT
2.5
MT
7.5
MT
Collected, stored, transported
& disposed at TSDF site of
BEIL.
2. Spent
Resin
ETP 35.2 0.33
MT
0.09
MT
0.42
MT
Collected, stored, transported
& disposed at TSDF site of
BEIL.
3. Used Manufacturing 33.1 0.54 MT 0.96 MT 1.5 Will be collected, stored and
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Drums process MT reused /sold to authorized
recycler Liners /
PPBags
0.84 MT 1.16 MT 2.0
MT
4. Used Oil From process 5.1 100 kl 28 kl 128 kl Collected, stored and sold to
authorize recycler.
5. Fly Ash/
bed Ash
From Boiler -- 86400
MT
25200
MT
11160
0 MT
Fly ash/ Bed ash sold to M/s.
Anmol&Co. J.K. Lakshmi
Cement, Ambuja.
-
ii Membership details of TSDF, CHWIF etc.
We have membership of BEIL-Dahej for TSDF
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
Waste:Fly Ash/ Bed Ash
Existing- 86400 MT/Annum
Proposed 25200 MT/Annum
Disposal: Fly ash/ Bed ash sold to M/s. Anmol& Co.
J.K. Lakshmi Cement, Ambuja.
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
• Not applicable
ii VOC emission sources and its mitigation measures
• Not applicable
• During the meeting dated 29/10/2018, technical presentation made by project proponent.
• At present unit is engaged in thermal power plant for which they have obtained EC and CC&A of the
Board. The proposal is for expansion of thermal power plant.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for expansion of existing unit and for now proposes thermal power plant. This unit is
having valid EC and CC&A for existing unit. Copy of EC, CC&A, EC compliance and CC&A
compliance report is submitted. PP ensured that there are no court cases pending and no public
complaints against the project.
• Total water consumption will be 16758KLD. Total wastewater generation will be 7215 KLD. After
proposed expansion, waste water will be treated in ETP and RO plant and treated effluent completely
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reused back in plant.
• 5870 kl/day steam condensate will be recycled back for boiler make-up, 5772 kl/day treated
wastewater will be recycled for cooling make-up and 1443 kl/day RO reject will be reused for Dust
suppression in coal handling area, sprinkling on fly ash and road cleaning.
• Coal will be used as fuel for proposed and existing boilers.
• Adequate APCM will be installed with boilers and lime along with coal used as fuel for SO2 emission
control.
• Hazardous waste management will be as per the HW Rules.
• The baseline environmental quality has been assessed for various components of the environment
viz. air, noise, water, biological and socioeconomic aspect. The baseline environmental study has
been conducted for the study area of 5 km/10 km radial distance from project site for the period
October-December 2015. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2,
NOx, 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 AERMOD. The resultant concentrations are within the NAAQS. The modeling study
proved that the air emissions from the proposed plant would not affect the ambient air quality of the
region in any significant manner. The ambient air quality around the proposed project site will remain
within the National Ambient Air Quality Standards (NAAQS).
• Risk assessment including prediction of the worst-case scenario and maximum credible accident
scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site
Emergency Plan has been covered in the RA report.
Discussions & Conclusion:
• It is noted that proposal is for expansion. PP addressed compliance monitoring of environmental
conditions of RO-Bhopal. Referring to the compliance, it is noted that 14 conditions are partially
complied, 4 conditions are not complied and 3 conditions are not responded. Committee deliberated
compliance of EC conditions monitored by the RO-Bhopal, MOEF&CC at length and asked PP to
submit the fresh compliance report of EC conditions with all corrective action in context to the
observation of RO-Bhopal.
• It is further noted that for the foul odor of CS2 and H2S, GPCB has taken action. Committee asked
PP to submit all the measures implemented to curb the foul odor of H2S and CS2 with technical
details.
• Committee noted that PP has not satisfactorily addressed issues raised during the public hearing and
asked PP to identify the issues in detail raised during public hearing and make action plan to redress
the issues. It is further mentioned that activities required for taking mitigation measures for the
redressing public complaints shall be incorporated in the EMP along with its budgetary provision.
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Committee deliberated compliance of the TOR issued and asked PP to submit following details so as
to consider the proposal in one of the upcoming SEAC meeting for further consideration.
1. To explore air cooling technology in place of water cooling system for proposed power plant
expansion that required additional 1875 KLPD of water for cooling tower make up.
2. To address quantity distribution of treated waste water (RO-Reject stream) for its utilization at (1)Dust
Suppression to coal handling area (2) Sprinkling on fly ash (3) Road Cleaning and waste water
management generating from road cleaning.
3. Fugitive emission control action plan due to proposed expansion for coal storage having existing load
of 72000 MTPM and additional load of 21000 MTPM keeping standing coal inventory in view.
4. Detailed EMP with activity and sub component based capital and recurring cost.
5. Need based budgetary outlay of CER as per the OM of MOEF&CC dated 01/05/2018.
6. To re-identify issues raised during public hearing and make action plan to redress the issues.
Address activities required for taking mitigation measures for the redressing public complaints and
submit detailed action plan for its implementation.
7. Submit revised CSR addressing measures taken for issues raised during public hearing and its
implementation plan.
8. Submit revised EMP with additional environmental mitigation measures arising due to redressal of
public complaint/ issues raised during public hearing with details of budgetary provision.
9. SIA/GJ/IND2/28046/2018 M/s. Grasim Industries Ltd. (Chemical
Division)
Plot No.-1, GIDC-Vilayat, Taluka -Vagra,
District-Bharuch, 392 140 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/IND2/28046/2018 dated
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 expansion unit proposes for Synthetic Organic Chemicals manufacturing plant as tabulated
below:
Sr. Name of the CAS no. / Quantity (MT/Month) End-use of the products
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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
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no. Products CI no. Existing Proposed Total
Epichlorohydrin (ECH)
1 Epichlorohydrin 78-93-3 0.0 100000 100000 Epoxy Resins, Synthetic
Glycerine, Water Treatment
Chemicals, Pharmaceuticals
2 Hydrochloric
acid (20%
Technical grade)
as 20%
7647-01-0 0.0 10000 10000 Hydrochloric acid is often
used as a descaling agent.
3 NaCl (20%) 7647-14-5 0.0 172400 172400
4 Refined Glycerin
(75%)
56-81-5 0.0 40000 40000 Glycerine is being used in
pharmaceutical applications,
Chlorinated Poly Vinyl Chloride (CPVC)
5 CPVC 68648-82-8 0.0 100000 100000 Hydronic piping and
distribution (radiators, fan
coils, etc.)
Suitable for many industrial
and process piping
applications
6 Hydrochloric
acid
7647-01-0 0.0 23004 23004 Hydrochloric acid is often
used as a desca ing
agen
poxy Plant
7 Liquid Epoxy
Resin
25068-38-6
101747
100000
201747
� High solids and
solvent free coatings
� Adhesives
� Civil engineering and
construction industry
� Automotive coatings
� Intermediate for can &
coil coatings
� Marine and Industrial
protective coatings
� Tooling, potting,
8 Formulated
Resin
25068-38-6
9 Powder Coating
25036-25-
3
10 Can Coating
Resin
25036-25-3
11 Solution Cut
Resins
1330-20-7
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casting and moulding
compounds
� Composites
Stabilizer in PVC
12 Hardeners 2855-13-2 14000 10000 24000 � High Chemical resistance
flooring/grouting
In adhesive
� Laminations
� Marine Coating
� Patch repair
� Off shore
primers/top
coatings.
� Chemical
resistance mortar.
� Concrete
Impregnation.
Crack injection system
13 Reactive
diluents
2425-79-8 7350 5000 12350 � Filament winding,
laminating,
� Vacuum pressure
impregnation
� Civil engineering
� Electronic
encapsulations
14 Salt 7647-14-5 40000 33677 73677 Dyeing industries
15 Hydrochloric
acid (20%)
7647-01-0 0 1000 1000 --
• 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 29/10/2018.
• The project proponent along with their expert /consultant M/s Anand Environmental Consultants
Pvt. Ltd attended the meeting and made presentation before the committee
• Salient features of the project are as under:
Sr. Particulars Details
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Page 23 of 48
no.
A Total cost of Proposed Project
(Rs. in Crores):
Existing: 453 Cr.
Proposed: 1085 Cr.
Total: 1538 Cr.
B Total Plot area
( sq. meter)
Existing: 141953.58Sq. m.
Proposed: 36557.42Sq. m.
Total: 178511Sq. m.
Green belt area,/Tree Plantation area
( sq. meter)
Existing: GG.Sq. m.
Proposed: GG.Sq. m.
Total: It may be noted that total
area of Grasim Industries Ltd. If
567 acres out of which 33% will be
developed as greenbelt area
C Employment generation Existing:212
Proposed:581
Total:793
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
GIDC
Status of permission from the concern authority.
ii Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 102 25.6 127.6
(B) Gardening 100 30 130
(C) Industrial
Process 656
890 1546 It may be noted that out of
1546 kl/day of total water
consist of 1037 kl/day
recycled water from
caustic & reaction water +
Steam condensate + DM
water and 509 kl/day is
fresh water
Washing 0 220 220
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Boiler 0 0 0
Cooling 800 1235 2035
Others 0 285 2085
Industrial Total 1456 2630 4086
Grand Total (A+B+C) 1658 2685.6 4343.6
1) Total water requirement for the project: 4343.6 KLD
2) Quantity to be recycle: 1841.4KLD
3) Total fresh water requirement: 2502.2KLD
iii Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
(A) Domestic 85 24 109
(B) Industrial
Process 373 335 708
Washing 0 220 220
Boiler 0 0 0
Cooling 384 430 814
Others 0 95 95
Total Industrial waste water 757 1080 1837
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 (Primary, Secondary, Tertiary) –850 M3/day and MEE - 320 M3/day for final
treatment of effluent/sewage generation 842 from existing epoxy plant
Proposed ETP – 500 kl/day capacity for treatment of 350 kl/day effluent/sewage generation from
Proposed Epoxy Plant
Proposed RO plant (750 kl/day) followed by MEE (300 kl/day)for 750 kl/day effluent generation
from proposed ECH and CPVC plant
v Mode of Disposal & Final meeting point
Domestic:
Domestic sewage generated (105 kl/day) from existing and proposed epoxy plant
will be treated in above stated Existing and Proposed effluent treatment plants.
And finally discharged through underground dahej-Vilayat pipeline.
Sewage generated (4.4 kl/day) form CPCV & ECH plant will be treated in STP.
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Treated wastewater will be used for gardening purposes within premises.
Industrial:
Industrial Effluent from epoxy plant (existing & proposed) will be treated in ETP
and treated water will be discharged to Dahej –Vilayat underground pipeline.
Effluent from ECH & CPVC plant will be Zero Discharge.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility
Not applicable
Membership of Common facility (CF)
Not applicable
vii Reuse/Recycle details (KLD)
Not applicable
E Air
i Flue gas emission details
No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.
Existing & Proposed
- Existing
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 D.G. Set
(2000 kVA) 30 HSD
27
Lit/Day
PM
SO2
NOx
Not
Applicable
- 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)
1 Incinerator 36 Hydro
gen
200
Nm3/Hr
PM
SO2
NOx
HCl
Caustic
Scrubber
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ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)
Existing & Proposed
- Existing
Sr.
no. Source of emission
Type of
emission
Stack/Vent
Height
(meter)
Air Pollution Control
Measures
(APCM)
1
ISBL ECH Tank
[Liquid Epoxy Resin Plant
(ECH Vent)]
VOC 30
Guard Condenser,
Scrubber, PRV, Flame
Arrester
2
ISBL Toluene Tank
[Liquid Epoxy Resin Plant
(Toluene Vent)]
VOC 30 Guard Condenser, PVRV,
(Integrated Flame Arrester)
3
OSBL ECH Tank
[Liquid Epoxy Resin tank
(ECH Vent)]
VOC 10 Scrubber, PRV ,Flame
arrestor
4
PESO Toluene Tank
[Liquid EPOXY Resin Tank
(Toluene Vent)]
VOC 10 Underground tank, PVRV
(Integrated flame arrestor)
5
Toluene Tank
[Reactive Diluents Plant
(Toluene) ]
VOC 30 Guard Condenser, PVRV,
(Integrated Flame Arrester)
6 Reactor
[Solution Cut Plant (Xylene) ]
VOC 30 Guard Condenser, PVRV,
(Integrated Flame Arrester)
7
Solution Cut Tank
[Solution Cut Tank Farm
(Xylene)]
VOC 10 PVRV, (Integrated Flame
Arrester)
8
Peso Xylene Tank
[Xylene Tank (PESO Tank
Farm)]
VOC 10 Underground tank, PVRV
(Integrated flame arrestor)
- Proposed
Sr.
no. Source of emission
Type of
emission
Stack/Vent
Height
(meter)
Air Pollution Control
Measures
(APCM)
1 HCl Vent Scrubber HCl 14 Scrubber
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Page 27 of 48
[Emergency vent Scrubber] Cl2
2
HCl synthesis
HCl 30
Absorption Tower using
water as an absorption
media
3 CPVC Reactor and
Degassing Vessel Cl2 12 Alkaline Scrubber
4 PVC Conveying to Silo
Cl2 25 Bag Filter
5 PVC Conveying to Oxygen
PM 10 Bag Filter
6 Degassing
PM 35 Bag Filter
7 Conveying-Degassing
Vessel to Hopper PM 25 Bag Filter
8 Evacuation of air
PM 10 Bag Filter
9 Conveying CPVC from PVC
Reactor PM 25 Bag Filter
iii Fugitive emission details with its mitigation measures.
--
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
Existin
g
Propos
ed
Total
1 Waste
Residues
(Not made
From
Manufactu
ring
I-23.1 560 927 1487 Collection, storage,
transportation ,
disposal at Ambuja
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with animal
or
vegetable
material)
Process Cement Ltd. for
pre-processing, co-
processing/
incineration
2 Chemical
Sludge
from
wastewater
treatment
ETP I-35.3 2025 1200 3225 Collection, storage,
transportation,
disposal of landfill
waste at TSDF and
incinerable waste by
pre-processing, co-
processing/
incineration
3 Discarded
containers/
bags/ liners
contaminat
ed with
hazardous
waste/che
micals
From
Manufactu
ring
I-33.1 850 400 1250 Collection, storage,
transportation,
disposal by selling to
authorized vendors.
4 Used or
Spent Oil
From
Lubricatio
n or
D.G.Set
I-5.1 5 7 12 Collection, storage,
transportation,
disposal by selling to
registered recycler
5 Waste or
residue
containing
oil
I-5.2 1 1 2 Collection, storage,
transportation,
disposal by selling to
registered recycler
6 Incinerator
waste/
residue
I-37.3 0 8000 8000 Collection, storage,
transportation,
disposal of landfill
waste at TSDF
7. MEE
residue
I-37.3 0 2190 2190 Collection, storage,
transportation,
disposal of landfill
waste at TSDF
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-
ii Membership details of TSDF, CHWIF etc. BEIL, SEPPL, RSPL, HELP
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
NaCl (Salt ) from MEE (Epoxy plant)will be
used as product
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
• Toluene - Falling Film Evaporator - 100% recovery, 100% Re-use
• Xylene - Production process - 100% consumption in plant
ii VOC emission sources and its mitigation measures
• Toluene, Xylene and ECH Process - Guard Condensers and Scrubbers
• During the meeting dated 29/10/2018, technical presentation made by project proponent.
• Salient features of the project submitted by PP are as mentioned above.
Observation:
• This proposal is for expansion of existing unit and for now proposes a new synthetic organic chemical
product. This unit is having valid EC and CC&A for existing unit. Copy of EC, CC&A, Ec and CC&A
compliance report is submitted. PP ensured that there are no court cases pending and no public
complaints against the project.
• Total water consumption will be 4343.6 KLD. Total wastewater generation will be 1837 KLD. After
proposed expansion, effluent will be treated in ETP, RO plant and MEE plant. Treated effluent from
Epoxy plant ETP and STP will be discharged in Dahej-Vilayat pipeline.
• Treated effluent from ECH & CPVC plant ETP will be evaporated in MEE after ETP and RO
treatment.
• 1841.4 KLD treated effluent will be reused back in process.
• Hydrogen will be used as fuel for incinerator.
• APCM like caustic scrubber will be provided for proposed incinerator.
• Adequate APCM will be provided with each plant reactors stack.
• Hazardous waste management will be as per the HW Rules.
Discussions & Conclusion:
• Committee noted that proposal is for TOR expansion. Referring to the compliance status of the
existing EC/CCA conditions, action by GPCB, details of public litigation and complaints, project
proponent could explain details with brief summary of compliance. It is also noted that existing
products along with proposed product profile is not addressed with clarity. Committee noted that
proposed production is in increasing in manifold compared to existing with increase in waste water
from 757 KLPD to 1837 KLPD.
• Considering that project proponent could not explain compliance status of EC/CCA with need of
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expansion, fresh water consumption, waste water generation, committee unanimously decided to ask
PP to represent the proposal again to the committee with details of summarized compliance status of
EC/CCA, measures to optimize fresh water consumption and to bring down the waste water
generation for the proposed products along with justification of extent of expansion for the proposed
products.
After deliberation, it was decided to defer the proposal in one of the upcoming SEAC meeting for
presentation considering aforementioned details.
10. SIA/GJ/IND2/28783/2015 M/s. Ami Organics Ltd
Plot No. 440-4/5/6 and 8206/B, Road No. 82,
GIDC Sachin, Ta.: Chorasi,
Sachin-394230, Dist.: Surat, Gujarat
EC-amendment
Project / Activity No.: 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/28783/2015 dated
25/09/2018 regarding grant of amendment in Environmental Clearance.
• This is an existing synthetic Organic Chemical manufacturing unit which was accorded Environmental
Clearance vide letter no. SEIAA/GUJ/EC/5(f)/3078/2015 dated 21/08/2015.
• Details regarding proposed changes in Environmental Clearance vide letter no.
SEIAA/GUJ/EC/5(f)/3078/2015 dated 21/08/2015 as follows :
Sr.
no.
Condition no. in
which changes
proposed.
As per EC As per proposed
amendment
Justification
1 Water: point no.
9 and 10 in EC
(Way of
Disposal)
9. The RO
permeate (44 KL)
shall be reused,
whereas RO
reject (17 KL)
shall be fed to the
MEE (Multiple
Effect
Evaporator).
10. High COD
After treatment through
RO, permeate (44 KLD)
will be Recycled back to
plant and RO reject (17
KLD) will be either sent to
Common Facility of
MEPPL or will be treated
into in-house Evaporator.
4 KLD High COD solvent
bearing stream shall be
The facility is in
operation since
long time and it
requires regular
maintenance.
Also due to regular
maintenance of
evaporation plant,
it is required to
send this 20 KLD
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Solvent Bearing
Stream shall be
stripped by using
steam in steam
stripping column
to recover the
solvent and the
rest shall be sent
to MEE.
treated in stripper and
outlet from stripper will be
either sent to Common
Facility of MEPPL or will
be treated into in-house
Evaporator.
concentrated
stream to common
facility of ‘MEPPL’.
• The project proponent requested for amendment in Environmental Clearance order as above.
• This is an existing unit engaged in Synthetic Organic Chemicals and EC obtained from SEIAA,
Gujarat with the products listed as tabulated below:
Sr.
No. Product Name CAS No. Capacity
1 4-Hydroxy Cumerine 1076-38-6
50 MT/Month
(Total 67 no of
products)
2. Dimethyl Formamide Dimethyl Acetal 4637-24-5
3. 1-(2,3-dichloro phenyl) piperazine HCL 119532-26-2
4. 1-(3-chlorophenyl) piperazine HCL 13078-15-4
5. 1- phenyl piperazine 92-54-6
6. 1-[2-(2-hydroxy ethoxy)ethyl]piperazine 13349-82-1]
7. Trimethyl Ortho Benzoate 707-07-3
8. 1-methyl-3-phenyl piperazine 5271-27-2
9. Trialkyl Ortho Alkolates 53568-66-4
10 1, 2-benzisoxazol-3-yl acetic acid 4865-84-3
11 4-Bromo -1-Methyl-1H-Pyrazole 583-70-0
12 1-methyl-4-piperidone 1445-73-4
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13 2,4-thiazolidinedione 2295-31-0
14 2,6-difluoro benzyl chloride 697-73-4
15 1-(2-hydroxy ethyl) pyrrolidine 2955-88-6
16 3-(Piperazine-1-yl)-1, 2-benzothiazole 87691-87-0
17 3-MORPHOLIN-4-YL-1-(4-NITROPHENYL)-5,6-
DIHYDROPYRIDIN-2(1H)-ONE 503615-03-0
18 4-[1, 2, 4-triazolo-1-yl] methyl phenyl hydrazine 212248-62-9
19 4 – HYDROXY COUMARIN (HC) 1076-38-6
20 5,6- Dimethoxy Indanone (5,6-DMI) 2107-69-9
21 AMINO ACETALDEHYDE DIMETHYL ACETAL
(AADMA)
22483
-09-6
22 1-ALKYL PIPERAZINE
i. 1-Allyl Piperazine
ii. 1-Formyl Piperazine
iii. 1-Carbethoxy Piperazine
iv. 1-Acetyl Piperazine
v. 1 - (3-Chloro propyl)piperazine
vi. 1-Benzyl Piperzaine
vii. 1-(Furoyl)piperazine
viii. 1-(Tetrahydrofuroyl)piperazine
ix. 1-Benzoyl Piperazine
x. 1-Cinnamyl Piperazine
xi. 1-BOC piperazine
xii. 1-CBZ Piperazine
xiii. 1-Isopropyl Piperazine
xiv. 1-Cylco pentyl Piperazine
xv. 1-Cyclo Butyl Piperazine
xvi. 1-Cyclo propyl piperazine
xvii. 1-Cyclo propyl methyl piperazine
xviii. 1-Benzyloxy ethyl piperazine
-
23 1 – Methyl – 3 – Phenyl Piperazine 5271-27-2
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24 1-ARYL PIPERAZINE
i. 1-(3-Chloro Phenyl )Piperazine
ii. 1-(2-Chloro Phenyl)piperazine
iii. 1-(4-Chloro Phenyl )Piperazine
iv. 1-(2,3-DiChloro Phenyl )Piperazine
v. 1-(3,4-DiChloro Phenyl )Piperazine
vi. 1-(2,6-DiChloro Phenyl )Piperazine
vii. 1-(2-Methoxy Phenyl )Piperazine
viii. 1-(3-Methoxy Phenyl )Piperazine
ix. 1-(4-Methoxy Phenyl )Piperazine
x. 1-(2-Hydroxy Phenyl )Piperazine
xi. 1-(3-Hydroxy Phenyl )Piperazine
xii. 1-(4-Hydroxy Phenyl )Piperazine
xiii. 1-(2-Bromo Phenyl )Piperazine
xiv. 1-(3-Bromo Phenyl )Piperazine
xv. 1-(4- Bromo Phenyl )Piperazine
xvi. 1-(2-Nitro Phenyl )Piperazine
xvii. 1-(3-Ntiro Phenyl )Piperazine
xviii. 1-(4-Ntiro Phenyl )Piperazine
xix. 1-Phenyl Piperazine
xx. 1-(3-Trifluoro Phenyl)Piperazine
xxi. N-(3,4-METHYL ENEDIOXY PHENYL)
PIPERAZINE
xxii. N-(2,4-DIMETHOXY PHENYL)
PIPERAZINE
xxiii. 1-(3,4-DIMETHOXY PHENYL)
PIPERAZINE
xxiv. 1-(3-Fluoro Phenyl )Piperazine
xxv. 1-(2-Fluoro Phenyl)pIperazine
xxvi. 1-(4-Fluoro Phenyl )Piperazine
xxvii. 1-(3-Tollyl )Piperazine
xxviii. 1-(2-Tollyl )Piperazine
xxix. 1-(4-Indolyl)piperazine
xxx. 1-Cyclohexyl piperazine
xxxi. 1-(2-Pyridyl)-piperazine
xxxii. 1-Pyridin-4-yl-piperazine
-
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xxxiii. 1-(2-Cyanophenyl)piperazine
xxxiv. 1-(4-Iodo-phenyl)-piperazine
xxxv. 1-(3-nitro-2-pyridyl)piperazine
xxxvi. 1-(2-Pyrimidyl) Piperazine
25 4-hydrzino benzene sulphonamide 17852-52-7
26 4-(methyl amino)-3-nitrobenzoic acid 41263-74-5
27 ethyl 3-(pyridin-2-ylamino)propanoate 103041-38-9
28 dibenzo[b,f][1,4]thiazepin-11(10H)-one 3159-07-7
29 N, N-Dimethyl Formamide Dimethyl Acetal 4637-24-5
30
Ethyl 1-(4-methoxyphenyl)-6-(4-nitrophenyl)-7-oxo-
4,5,6,7-tetra hydro-1H-pyrazolo[3,4-c] pyridine-3-
carboxylate
536759-91-8
31 Ethyl (4-amino-2-nitrophenyl) carbamate 73895-87-1
32 Ethyl (4-aminophenyl) carbamate 57399-97-0
33 Ethyl (4-nitrophenyl) carbamate 2621-73-0
34 Ethyl{4-[4-fluorobenzyl]amino}-2-
nitrophenyl}carbamate 150812-23-0
35 ETHYLCHLORO[(4-METHOXY
PHENYL)HYDRAZONO]ACETATE 27143-07-3
36 1 – (3 – CHLORO PHENYL) – 4 – (3 – CHLORO
PROPYL) PIPERAZINE HCl (ECPH) 52605-52-4
37 1-[2-(2-HYDROXY ETHOXY) ETHYL]
PIPERAZINE 13349-82-1
38 Ibandronic Acid 114084-78-5
39 Methyl Cyclobutane carboxylate 765-85-5
40 S-(2, 3-epoxypropyl) Phthalamide 161596-47-0
41 2H-[1,2,4]-TRIAZOLO-[4,3-a]-Pyridine (124TPO) 6969-71-7
42 ETHYL 5- NITROBENZOFURAN-2-
CARBOXYLATE 69604-00-8
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43 ETHYL-5- AMINOBENZOFURAN-2-
CARBOXYLATE 174775-48-5
44 ETHYL-5- PIPERAZINYL BENZOFURAN-2-
CARBOXYLATE 163521-20-8
45 1-(2, 6-dichlorophenyl) indoline-2-one 15362-40-0
46 1-(4-methylphenyl)-4,4,4-triflurobutane-1,3-dione 720-94-5
47 1-Benzyl-4-piperidone 3612-20-2
48 1-Boc-3-piperidone 98977-36-7
49 1-Boc-4-piperidone 79099-07-3
50 1-Hydroxy benzotriazole 2592-95-2
51 3-CHLORO-1-(4-NITROPHENYL)-5,6-
DIHYDROPYRIDIN-2(1H)-ONE 536760-29-9
52 3-methoxy propiophinone 37951-49-8
53 4-(2-chloroethyl) morpholine 3647-69-6
54 4-(4-aminophenyl) morpholin-3-one 438056-69-0
55 4-chloro butyraldehyde dimethyl acetal 29882-07-3
56 Cyclohexane Carboxaldehyde 2043-61-0
57 1-(4-Rphenyl)-2-piperidone -
58 2-PIPERIDONE(2-PD) 675-20-7
59 N-Boc-2-PIPERIDONE 85908-96-9
60 3, 4 – DIHYDROXY – 5 – NITRO
BENZALDEHYDE (3,4DH5NBZ) 116313-85-0
61 N-Methyl amino Acetaldehyde Dimethyl Acetal 122-07-6
62 2-(chloromethyl)-4- methyl quinzoline
109113-72-6
63 4-cyano-4-(4-fluorophenyl) cyclohexan-1-one. 56326-98-8
64 5-(2-Methoxyphenoxy)-2,2’-bipyrimidine- 150728-12-4
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4,6(1H,5H)-dione
65 Bromo acetaldehyde diethyl acetal 2032-35-1
66 Diethyl (2-methoxy phenoxy) malonate 20730-58-9
67 Methyl di-(2-thienyl)glycolate 26447-85-8
BY PRODUCTS NAME AND CAPACITY
1 1-(2-Hydroxy ethyl) piperazine 103-76-4 14 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 29/10/2018.
• During the meeting dated 29/10/2018, technical presentation made during the meeting by project
proponent.
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores): There will be no increase in project cost.
Capital cost for EMS (Environmental Management System): - No Changes as amendment is only
for way of disposal of effluent
Recurring cost towards the environmental protection measures: No changes.
B Total Plot area ( sq. meter) 8250 sq. m.
Green belt area/Tree Plantation area ( sq. meter) 2500 sq. m.
C Employment generation
Direct No additional manpower will be require as
amendment is only for change in mode of
effluent disposal.
Indirect
Total
D Water
i
Source of Water Supply (GIDC Bore well, Surface
water, Tanker supply etc...)
The water requirement of this project is
69.5 KLD and will be supply by Sachin
Infra Management Ltd.
No change in water consumption due to
proposed EC Amendment.
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Status of permission from the concern authority. Not Applicable as there is no expansion.
ii
Water consumption (KLD)
Existing which will remain same
Sr. No. Purpose Ultimate (KLD)
1 Domestic 10
2 Industrial 59.5
(A) Processing 44.5
(B) Boiler feed
15 (C) Cooling make up
(D) Miscellaneous
TOTAL 69.5
Total water requirement for the project: 132.5KLD
Quantity to be recycle: 63 KLD
Total fresh water requirement: 69.5KLD
When 20 KLD effluent will be sent to Common facility of MEPPL ,
Total water requirement for the project: 113.5KLD
Quantity to be recycle: 44 KLD
Total fresh water requirement: 69.5KLD
iii Waste water generation (KLD)
-
Sr. No. Source Ultimate (KLD)
1 Domestic 10
2 Industrial 65.0
(A) Processing 60.0
(B) Boiler Blow down
5
(C) Cooling bleed off
(D) Miscellaneous
TOTAL of Industrial & Domestic 75
-
iv Treatment facility with capacity
(ETP, CETP, MEE, STP, Spray Dryer etc).
61 KLD shall be send to ETP followed by
RO. RO permeate (44 KLD) will be
Recycled and RO reject (17 KLD) will be
either treated in in-house Evaporator or
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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
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sent to Common Facility of MEPPL
(Mahavir Eco projects Pvt. Ltd.).
4 KLD High COD solvent bearing stream
shall be treated in stripper. Outlet from the
stripper shall be either sent to Common
Facility of MEPPL or will be treated in in-
house Evaporator.
10 KLD domestic effluents will be sent to
soak pit/septic tank as per existing EC.
v Mode of Disposal & Final meeting point
Domestic: 10 KLD Domestic water is being
treated in to Septic Tank / Soak Pit
System/ Packaged STP and will be reused.
Industrial: As mention above and, it is
proposed to sent
17 KLD RO reject and 3 KLD effluent from
stripper to Common facility of MEPPL.
vi In case of Common facility (CF) like CETP, Common
Spray dryer, Common MEE etc. , name of CF
As mentioned in point iv.
Membership of Common facility (CF)
Proponent has obtained NOC letter from
MEPPL for disposal of effluent.
vii Reuse/Recycle details (KLD) 44 KLD effluent will berecycled.
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.
There will be no change in existing APC as mentioned below:
FLUE GAS EMISISON
Sr.
No. Stack Attached to
Stack Height and
Diameter
Fuel
Consumption
Air Pollution Control
System
1. Steam Boiler
Capacity : 1 MT/Hr
Height -. 30 Meters
Dia. - 40 cm Natural Gas
–
1500 m3/day
(Total)
As Natural Gas is used
as a fuel. Adequate
Stack Height is
provided.
2. Steam Boiler
Capacity : 2 MT/Hr
Height -. 30 Meters
Dia. - 40 cm
3. Steam Boiler
Capacity : 2 MT/Hr
Height -. 30 Meters
Dia. - 40 cm
4. Thermopack Unit Height -. 30 Meters
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Capacity : 200 U Dia. - 40 cm
5. Thermopack Unit
Capacity : 400 U
Height -. 30 Meters
Dia. - 40 cm
6. D. G. Set - Stand By
Capacity : 250 KVA
Height -.11 Meters
Dia. - 25 cm
LDO – 40
Liters/Hr
(Total)
As LDO is use as a
fuel. Adequate Stack
Height is provided.
7. D. G. Set - Stand By
Capacity : 250 KVA
Height -.11 Meters
Dia. - 25 cm
As LDO is use as a
fuel. Adequate Stack
Height is provided.
8. D. G. Set - Stand By
Capacity : 250 KVA
Height -.11 Meters
Dia. - 25 cm
As LDO is use as a
fuel. Adequate Stack
Height is provided.
-
ii Process gas i.e. Type of pollutant gases e.g: HCl
There will be no change in existing Process gas emission control system
PROCESS GAS EMISSION
Sr.
No. Vent Attached to
Vent Height and
Diameter Pollutant
Air Pollution
Control System
1. Reaction Vessel Height - 11 Meters
Dia. – 15 cm
HCl Ventury & packed
bed Scrubber
-
iii Fugitive emission details with its mitigation measures.
As below:
There shall be fugitive emissions during handling of raw materials
Mitigation Measures:
Vents of storage tanks are connected to Scrubbers to minimize fugitive emissions of gases.
F Hazardous waste
(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules
2016.
i
Cat. of
waste
Type of
Hazardous
Waste
Source Generated
Quantity Treatment
34.3 ETP Waste From ETP 500 Kg/Day Collection / Storage /
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i. e. 180
MT/Year
Transportation / sent to TSDF
site for secured land filling
36.4 Distillation
residue
From
Distillation
287.7
MT/Month
Collection / Storage /
Transportation / sent to TSDF
site for incineration.
5.1 Used Oil From plant &
machineries
1000
Liters/year
i. e.
0.85 MT/Year
Collection / Storage /
Transportation / sent to TSDF
site / send to registered recycler
33.3 Discarded
Barrels/Liners
/
Containers
From raw
material
packaging
200
Nos/Month
i. e.
19.2 MT/Year
Collection / Storage /
Transportation / sent back to
supplier / sent to registered
recycler
--- Evaporated
Salt *
From
Evaporator
2 MT/Day
i. e.720
MT/Year
Collection / Storage /
Transportation / sent to TSDF
Site
20.2 Spent Solvent
**
From Process 1150
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end
users i. e. M/s. Rhythm
Chemicals Pvt. Ltd. / sent to
TSDF site for incineration
*Salts generated from evaporator will be eliminated when 20 KLD (17 KLD RO Reject + 3 KLD
treated effluent after stripper) effluent is sent to Common facility of MEPPL.
** The generation of detailed solvent list is as per below:
D 3 Sodium
Sulphate
From the
manufacturing
of 4-Bromo -1-
Methyl-1H-
Pyrazole / 2-
PIPERIDONE(
2-PD)
138.90
MT/Month
Collection / Storage / send to
TSDF site
B 11 Thionyl
Chloride
From the
manufacturing
of 2,6-difluoro
benzyl chloride
127.2
MT/Month
Collection / Storage / recycle in to
process
B 6 Raney Nickel From Process 9.5 MT/Month Collection / Storage / recycle in to
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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
Page 41 of 48
process / send to original
Catalyst Manufacturer
From the manufacturing of 4-[1, 2, 4-triazolo-1-yl] methyl phenyl hydrazine / 5,6- Dimethoxy
Indanone (5,6-DMI) / Ethyl (4-aminophenyl) carbamate / ETHYL-5- AMINOBENZOFURAN-2-
CARBOXYLATE
Ammonia From the
manufacturing
of 2H-[1,2,4]-
TRIAZOLO-
[4,3-a]-Pyridine
(124TPO)
13.61
MT/Month
Collection / Storage / recycle in to
manufacturing of 1 – Methyl – 3 –
Phenyl piperazine, Amino
Acetaldehyde Dimethyl Acetal
and 1 – methyl – 3 – Phenyl
Piperazine
28.2 Palladium
Carbon
From the
manufacturing
of 1-Boc-3-
piperidone
14.20
MT/Month
Collection / Storage / recycle in to
process / send to original
Catalyst Manufacturer
26.1 Process
Waste
From the
manufacturing
of 1-[2-(2-
Hydroxy
Ethoxy) Ethyl]
Piperazine
150.8
MT/Month
Collection / Storage /
Transportation / sent to TSDF
site
28.2 Carbon
Residue
From the
manufacturing
of 1-Hydroxy
benzotriazole /
3, 4 –
Dihydroxy – 5
– Nitro
Benzaldehyde
(3,4dh5nbz)
8.57
MT/Month
Collection / Storage /
Transportation / sent to TSDF
site
-
ii Membership details of TSDF, CHWIF etc.
Industry is a member of TSDF site of M/s.
Bharuch Enviro Protection Ltd., Bharuch
for the disposal of Solid / Hazardous
Waste.
ii Details of Non-Hazardous waste & its disposal Not Applicable
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(MSW and others)
G Solvent management& VOC emissions etc.
i Details of Solvent recovery (As per respective ToR)
Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
Sr.
No.
Type of solid
waste Source
Generated
Quantity Treatment
1. Spent
Solvent
(Toluene)
From Process 1150
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 4 Hydroxyl Cumarine, 1-(2,3-dichloro phenyl)
piperazine HCL, 1-(3-chlorophenyl) piperazine HCL, 1- phenyl piperazine, 1-methyl-3-
phenyl piperazine, 1-methyl-4-piperidone, 1-(2-hydroxy ethyl) pyrrolidine, 4 – HYDROXY
COUMARIN (HC), 5,6- Dimethoxy Indanone (5,6-DMI), 1 – Methyl – 3 – Phenyl
Piperazine, 1-(3-Chloro Phenyl ) Piperazine, 1-(2-Chloro Phenyl) piperazine, 1-(4-Chloro
Phenyl ) Piperazine, 1-(2,3-DiChloro Phenyl ) Piperazine, 1-(3,4-DiChloro Phenyl )
Piperazine, 1-(2,6-DiChloro Phenyl ) Piperazine, 1-(2-Methoxy Phenyl ) Piperazine, 1-(3-
Methoxy Phenyl ) Piperazine, 1-(4-Methoxy Phenyl ) Piperazine, 1-(2-Hydroxy Phenyl )
Piperazine, 1-(3-Hydroxy Phenyl ) Piperazine, 1-(4-Hydroxy Phenyl ) Piperazine, 1-(2-
Bromo Phenyl ) Piperazine, 1-(3-Bromo Phenyl ) Piperazine, 1-(4- Bromo Phenyl )
Piperazine, 1-(2-Nitro Phenyl ) Piperazine, 1-(3-Ntiro Phenyl ) Piperazine, 1-(4-Ntiro
Phenyl ) Piperazine, 1-Phenyl Piperazine, 1-(3-Trifluoro Phenyl) Piperazine, N-(3,4-
METHYL ENEDIOXY PHENYL) PIPERAZINE, N-(2,4-DIMETHOXY PHENYL)
PIPERAZINE, 1-(3,4-DIMETHOXY PHENYL) PIPERAZINE, 1-(3-Fluoro Phenyl )
Piperazine, 1-(2-Fluoro Phenyl) piperazine, 1-(4-Fluoro Phenyl ) Piperazine, 1-(3-Tollyl )
Piperazine, 1-(2-Tollyl ) Piperazine, 1-(4-Indolyl) piperazine, 1-(2-Pyridyl)- piperazine, 1-
Pyridin-4-yl-piperazine, 1-(2-Cyanophenyl) piperazine, 1-(4-Iodo-phenyl) - piperazine, 1-
(3-nitro-2-pyridyl) piperazine, 1-(2-Pyrimidyl) Piperazine.
2. Spent
Solvent
(Methanol /
Iso Propyl
Alcohol)
From Process 195
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 1-(2,3-dichloro phenyl) piperazine HCL, 1-(3-
chlorophenyl) piperazine HCL and 1- phenyl piperazine,
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3. Spent
Solvent
(Solvent)
From the
manufacturing
of 1-[2-(2-
hydroxy ethoxy)
ethyl]
piperazine
158.33
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
4. Spent
Solvent
(Piperazine)
From Process 175
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 1-[2-(2-hydroxy ethoxy) ethyl] piperazine, 3-
(Piperazine-1-yl)-1, 2-benzothiazole, 1-(2-hydroxy ethyl) piperazine, 1-Formyl
Piperazine, 1-Carbethoxy Piperazine, 1-Acetyl Piperazine, 1 - (3-Chloro
propyl)piperazine, 1-Benzyl Piperzaine, 1-(Furoyl)piperazine, 1-
(Tetrahydrofuroyl)piperazine, 1-Benzoyl Piperazine, 1-Cinnamyl Piperazine, 1-BOC
piperazine, 1-CBZ Piperazine, 1-Isopropyl Piperazine, 1-Cylco pentyl Piperazine, 1-
Cyclo Butyl Piperazine, 1-Cyclo propyl piperazine, 1-Cyclo propyl methyl piperazine, 1-
Benzyloxy ethyl piperazine, 1 - methyl Piperazine, 1-Hydroxy benzotriazole.
5. Spent
Solvent
(Acetic Acid)
From Process 50
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 1, 2-benzisoxazol-3-yl acetic acid, ethyl 3-(pyridin-
2-ylamino)propanoate,
6. Spent
Solvent
(Methanol)
From Process 555.12
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of Tri Methyl Ortho Benzoate, Tri Alkyl Ortho
Alkonate, 1, 2-benzisoxazol-3-yl acetic acid, 2,6-difluoro benzyl chloride, 4-[1, 2, 4-
triazolo-1-yl] methyl phenyl hydrazine, 1-(2-hydroxy ethyl) piperazine, 1-Formyl
Piperazine, 1-Carbethoxy Piperazine, 1-Acetyl Piperazine, 1 - (3-Chloro
propyl)piperazine, 1-Benzyl Piperzaine, 1-(Furoyl)piperazine, 1-
(Tetrahydrofuroyl)piperazine, 1-Benzoyl Piperazine, 1-Cinnamyl Piperazine, 1-BOC
piperazine, 1-CBZ Piperazine, 1-Isopropyl Piperazine, 1-Cylco pentyl Piperazine, 1-
Cyclo Butyl Piperazine, 1-Cyclo propyl piperazine, 1-Cyclo propyl methyl piperazine, 1-
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Benzyloxy ethyl piperazine, 1 - methyl Piperazine, dibenzo[b,f][1,4]thiazepin-11(10H)-
one, N, N-Dimethyl Formamide Dimethyl Acetal, Ethyl{4-[4-fluorobenzyl]amino}-2-
nitrophenyl}carbamate, 1-[2-(2-HYDROXY ETHOXY) ETHYL] PIPERAZINE, Methyl
Cyclobutane carboxylate, 2H-[1,2,4]-TRIAZOLO-[4,3-a]-Pyridine (124TPO), 1-Boc-3-
piperidone, 4-chloro butyraldehyde dimethyl acetal, Cyclohexane Carboxaldehyde, 4-
cyano-4-(4-fluorophenyl) cyclohexan-1-one., 5-(2-Methoxyphenoxy)-2,2’-bipyrimidine-
4,6(1H,5H)-dione, Methyl di-(2-thienyl)glycolate.
7. Spent
Solvent
(IPE)
From Process 1125
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 4-Bromo -1-Methyl-1H-Pyrazole, ethyl 3-(pyridin-2-
ylamino)propanoate, 1-Boc-3-piperidone, Cyclohexane Carboxaldehyde, N-Methyl
amino Acetaldehyde Dimethyl Acetal,
8. Spent
Solvent
(MDC)
From Process 1550
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 2,6-difluoro benzyl chloride, 3-(Piperazine-1-yl)-1,
2-benzothiazole, 5,6- Dimethoxy Indanone (5,6-DMI), Methyl Cyclobutane carboxylate,
ETHYL 5- NITROBENZOFURAN-2-CARBOXYLATE, ETHYL-5- PIPERAZINYL
BENZOFURAN-2-CARBOXYLATE, 4-(2-chloroethyl) morpholine, 4-chloro
butyraldehyde dimethyl acetal, Cyclohexane Carboxaldehyde, 4-cyano-4-(4-
fluorophenyl) cyclohexan-1-one.
9. Spent
Solvent
(IPA)
From Process 190
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 5,6- Dimethoxy Indanone (5,6-DMI), Ethyl 1-(4-
methoxyphenyl)-6-(4-nitrophenyl)-7-oxo-4,5,6,7-tetra hydro-1H-pyrazolo[3,4-c] pyridine-
3-carboxylate, S-(2, 3-epoxypropyl) Phthalamide, 4-(4-aminophenyl) morpholin-3-one.
10 Spent
Solvent
(Ethyl
Acetate)
From Process 200
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of 1 – Methyl – 3 – Phenyl Piperazine, 1 - Methyl - 3 -
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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
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Phenyl Piperazine, Ethyl (4-nitrophenyl) carbamate, S-(2, 3-epoxypropyl) Phthalamide.
11 Spent
Solvent
(Phenol)
From the
manufacturing
of
dibenzo[b,f][1,4]
thiazepin-
11(10H)-one
9.41
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
12 Spent
Solvent
(DMF)
From Process 260
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of dibenzo[b,f][1,4]thiazepin-11(10H)-one, ETHYL 5-
NITROBENZOFURAN-2-CARBOXYLATE, 3-CHLORO-1-(4-NITROPHENYL)-5,6-
DIHYDROPYRIDIN-2(1H)-ONE. .
13 Spent
Solvent
(Ethanol)
From Process 935.20
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of Ethyl (4-aminophenyl) carbamate, Ibandronic Acid,
Methyl Cyclobutane carboxylate, ETHYL 5- NITROBENZOFURAN-2-CARBOXYLATE,
ETHYL-5- AMINOBENZOFURAN-2-CARBOXYLATE, 5-(2-Methoxyphenoxy)-2,2’-
bipyrimidine-4,6(1H,5H)-dione.
14 Spent
Solvent
(Acetone)
From Process 1040
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
Generated from the manufacturing of ETHYLCHLORO[(4-METHOXY
PHENYL)HYDRAZONO]ACETATE and Ibandronic Acid.
15 Spent
Solvent
(Mono
Ethylene
Glycol)
From the
manufacturing
of 2H-[1,2,4]-
Triazolo-[4,3-a]-
Pyridine
(124TPO)
100
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
16 Spent
Solvent (Di
From the
manufacturing
105
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
Page 46 of 48
Chloro
Methane)
of ETHYL 5-
NITROBENZOF
URAN-2-
CARBOXYLAT
E
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
17 Spent
Solvent
(THF)
From Process 180
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
From the manufacturing of 1-Boc-3-piperidone / 3-methoxy propiophinone / 4-(4-
aminophenyl) morpholin-3-one
18 Spent
Solvent (t -
Butanol)
From the
manufacturing
of 1-Boc-3-
piperidone / 1-
Boc-4-
piperidone
28.76
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
19 Spent
Solvent
(Hexane)
From the
manufacturing
of 1-Boc-4-
piperidone
35
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
20 Spent
Solvent
(Chloro
Benzene)
From the
manufacturing
of 1-(4-
Rphenyl)-2-
piperidone
194
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
21 Spent
Solvent
(Methylene
DiChloride)
From the
manufacturing
of 3, 4 –
Dihydroxy – 5 –
Nitro
Benzaldehyde
(3,4DH5NBZ)
301.93
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
22 Spent
Solvent
(1, 4
From the
manufacturing
of 2-
130
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
Page 47 of 48
-
Dioxane) (chloromethyl)-
4- methyl
quinzoline
sent to TSDF site for incineration
23 Spent
Solvent
(o-xylene)
From the
manufacturing
of 4-cyano-4-(4-
fluorophenyl)
cyclohexan-1-
one
166.40
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
24 Morpholine From the
manufacturing
of 3-morpholin-
4-YL-1-(4-
nitrophenyl)-
5,6-
dihydropyridin-
2(1H)-one
67.50
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
25 Salicyladehy
de
From the
manufacturing
of ethyl 5-
nitrobenzofuran
-2-carboxylate
20
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
26 Propionic
Acid
From the
manufacturing
of 3-methoxy
propiophinone
22.55
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
27 N-heptane From the
manufacturing
of Methyl di-(2-
thienyl)glycolate
392
MT/Month
Collection / Storage / recycle in to
process / sent to authorized end users i.
e. M/s. Rhythm Chemicals Pvt. Ltd. /
sent to TSDF site for incineration
ii VOC emission sources and its mitigation measures NIL
• During the meeting dated 29/10/2018, Committee observed that unit has proposed to amend in
condition no-9 and 10 of EC order. Committee deliberated on the possible impacts on surrounding
environment due to proposed amendments.
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446thmeeting of SEAC-Gujarat, Dated 29.10.2018
Page 48 of 48
Discussions & Conclusion:
• Committee deliberated on EC-amendment proposal as above.
• Committee noted that PP has requested amendment in EC condition for allowing them to send
treated waste water of 20 KLPD after treatment to common facility of MAHAVIR ECO for pursuing
zero liquid discharge. It is noted that quality of treated waste water will be COD: 10,000 mg/litre to
12,000 mg/litre, TDS: 12000 mg/litre to 15000 mg/litre. Further PP mentioned that during failure of
operation of in-house MEE, alternative source of disposal of treated waste water for pursuing ZLD is
needed. Committee asked PP to submit details of overhauling hours of existing MEE since
commissioning and to justify how frequent the operation of in-house MEE gets overhauled and also
to submit compliance status of common infrastructure of MAHAVIR ECO that pursues zero liquid
discharge (ZLD).
After deliberation, committee asked PP to submit aforementioned details and after submission, it
was decided to consider the proposal in one of the upcoming SEAC meeting.
Meeting ended with thanks to the Chair and the Members.
Minutes approved by:
1. Shri S. C. Srivastav, Vice Chairman, SEAC 2. Shri V. N. Patel, Member, SEAC
3. Shri. R. J. Shah, Member, SEAC
4. Shri A.K. Muley, Member, SEAC