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1
550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 1 of 106
Minutes of the 550thmeeting ofthe State Level Expert Appraisal Committee held on 19/09/2019 at
Committee Room, Gujarat Pollution Control Board, Sector 10A,Gandhinagar.
The 550thmeeting of the State Level Expert Appraisal Committee (SEAC) was held on 19thSeptember
2019 at Committee Room, Gujarat Pollution Control Board, Sector 10A, Gandhinagar. Following
members attended the meeting:
1. Dr. Dinesh Misra, Chairman, SEAC
2. Shri S. C. Srivastav, Vice Chairman, SEAC
3. Shri Rajesh. I. Shah, Member, SEAC
4. Shri V. N. Patel, Member, SEAC
5. Shri. R. J. Shah, Member, SEAC
The regular agenda of Appraisal, Reconsideration&ToR cases were taken up. The Committee considered
the applications made by project proponents, additional details submitted as required by the SEAC/SEIAA
and details furnished in the Form-1, PFR, EIA-EMP reports.
Proposal No. Name and Address of the Unit Remarks
1 SIA/GJ/IND2/38454/2018 M/s. Ven Petrochem & Pharma India
Pvt Ltd
Plot No.2903,05,07,09,10,& 2704 to
2708, GIDC, Sarigam, Taluka :
Umbergaon, District : Valsad.- 396155
Appraisal
Category of the unit : 5(f)
Project status: Expansion
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/38454/2018dated
30/08/2019 for obtaining Environmental Clearance.
• SEIAA issued TOR to PP vide their letter dated 10/01/2019.
• Project proponent has submitted EIA Report prepared by Anand Environmental Consultants Pvt Ltd,
Ahmedabadbased on the TOR issued by SEIAA.
• This is an expansion project for manufacturing of synthetic organic chemical as tabulated below.
Sr.
no.
Name of the Products CAS no. /
CI no.
Quantity (MT/Month) End-use of the
products Existing Proposed Total
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550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 2 of 106
1 Acebrophylline
179118-73-
1
0.0
1.0 1.0 Anti-mucolytic
(for cough)
2 Ambroxol Hydrochloride 23828-92-4 0.0 6.6 6.6 Anti-mucolytic
(for cough)
3 Bromhexine Base
3572-43-8 0.0 1.0 1.0 For manufacture
of Bromohexine
Hydrochloride
4 Bromhexine
Hydrochloride
611-75-6 3.0 3.0 6.0 Anti-mucolytic
(for cough)
5 Timolol Maleate 26921-17-5 0.0 1.2 1.2 Anti –
Glaucoma
(for eye drops)
6 2-Amino-N-Methyl-N-
Cyclohexyl
Benzenemethanamine
57365-08-9 0.0 1.2 1.2 For manufacture
of Bromohexine
Hydrochloride
7. Sodium Bromide* 7647-15-6 10.7 93.2 103.9 Photographic
Chemical
8. Dimethyl Hydantoin* 77-71-4 0.5 1.1 1.6 For manufacture
of Dibromo
Dimethyl
Hydantoin
Total
14.2 108.3 122.5
• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006.
• PP was called for presentation in the SEAC meeting dated 19/08/2019.
• Salient features of the project are as under:
Sr.
No.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing : INR 4.50 Crores
Proposed : 20 Crores
Total : INR 24.50 Crores
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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B Total Plot area
( sq. meter)
Existing: 9690 .Sq. m.
Proposed: 2300 Sq. m. (from 9690 sqm)
Total: 9690 Sq. m.
Green belt area
( sq. meter)
Existing: 970.67. Sq. m.
Proposed: 240 Sq. m.
Total: 1210.67 Sq. m.i.e. 1211 Sq. m
C Employment generation Existing:83
Proposed:62
Total:145
D Water
i Source of Water Supply
(GIDC Bore well, Surface water, Tanker
supply etc...)
G.I.D.C
Status of permission from the concern authority. Permission from GIDC is
Obtained.
ii Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 4 4 8 --
(B) Gardening 1 1 2 --
(C) Industrial
Process 2.0 3.4 5.4 --
Washing 1.1 0.9 2.0 --
Boiler 12 12 24 --
Cooling 6 2 8 --
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Others 0.1 0.2 0.3 --
Industrial Total 21.2 18.5 39.7 --
Grand Total
(A+B+C)
26.2 23.5 49.7 --
1) Total water requirement for the project: 49.7KLD
2) Quantity to be recycled: 12KLD
3) Total fresh water requirement: 37.7KLD
iii Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 2.4 2.4 4.8 --
(B) Industrial
Process 1.55 1.75 3.30 --
Washing 1.1 0.9 2.0 --
Boiler 4.5 3.5 8 Will be recycled
Cooling 3.0 1.0 4 Will be recycled
Others 0.1 0.2 0.3 --
Total Industrial waste
water
10.25 7.35 17.6 --
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STPetc..
� Existing : Capacity of Incinerator – 250 kg/hour , 2.75 KLD incinerated within premises,
7.5 KLD recycled back
� Proposed: Capacity of Incinerator –500 kg/hour
� 2.85 KLD will be incinerated within premises / co processing, 4.5 KLD will be recycled back
after treatment.
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Treatment scheme including segregation at source.
� 4.8 KL / day domestic waste water generated will be disposed into septic tank /soak pit
system.
� 17.6 KL/day industrial waste water generated out of which 5.60 KL / day (3.30 KLDfrom
Process + 2.0 KLD from Washing + 0.3 KLD from Scrubber) will be incinerated in an
incinerator within premises or will be collected, stored, transported and disposed to cement
industries for co-processing AND 12 KL / day (8 KLD from boiler + 4 KLD from cooling) will
be recycled / reused back.
� Details are given in EIA report, Chapter – 2.
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the
Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding
compliance of CETP.
� Not Applicable.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
� Unit maintains ZLD by incinerating industrial waste water in an incinerator within premises
and the same practice will be continued after expansion or will be sent to cement
industries for co-processing.
v Mode of Disposal & Final meeting point
Domestic: 4.8 KL / day (existing + proposed) domestic waste water generated will be
disposed into septic tank /soak pit system.
Industrial: 5.60 KL / day (3.30 KLD from Process + 2.0 KLD from Washing + 0.3 KLD from
Scrubber) (existing + proposed) will be incinerated in an incinerator within
premises or will be collected, stored, transported and disposed to cement
industries for co-processing.
12 KL / day (8 KLD from boiler + 4 KLD from cooling) (existing + proposed) will
be recycled back.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.
Name of Common facility (CF)(For waste water treatment)
� Not Applicable
Membership of Common facility (CF) - Not Applicable
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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(For waste water treatment)
� Not Applicable
vii Simplified water balance diagram with reuse / recycle of waste water
vii Reuse/Recycle details (KLD)
[Source of reuse & application area]
Total reuse 12 KLD
Source of waste water
for reuse with quantity in
KLD (From where it is
coming)
Application area
with quantity in
KLD (Where it is
used)
Characteristics of
waste water to be
reused (COD,
BOD,TDS etc.)
Remarks
regarding
feasibility
to reuse i.e.
Boiler condensate and
cooling water purge will be
the source of waste water
generated which is planned
to be used.
Approximately 8 KLD
of boiler condensate
and 4 KLD of cooling
purge water will be
reused back into the
boiler as well as back
for cooling makeup
� pH : 7- 8.5
� Suspended Solids : 150
– 200 mg/l
� TDS :1500 – 2000 mg/l
� Oil & Grease : 5 -10 mg/l
� COD : 80-100 mg/l
BOD : 10-20 mg/l
It is
completely
feasible to
use for
Boiler &
cooling
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.
4 recycle
Total water
consumption 37.7 (2nd day onwards)
(49.7-12)
Gardening
2
Domestic 8
Industrial 39.7
(27.7 +12)
Boiler 24
Process
5.40
Cooling make-up
8
To Incinerator / disposed to cement
industries for co-processing
5.60
Other (scrubbing)
0.3
Water from GIDC
Septic tank/soak pit
4.8
Washing
2
4 8 3.30 0.3 2
Recycle back
12
8 recycle 4 fresh 16 fresh
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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. Boiler
1000 kg / hour
11 PNG 25 scm/hr PM
SO2
NOX
--
2.
D.G. Set
(250 KVA)
5 Diesel 25 lit/hr PM
SO2
NOX
--
3. Incinerator
(250 kg/hr)
30* PNG
25 scm/hr PM
SO2
HCl
Dust Collector
followed by
scrubber
- 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. Boiler
1000 kg /
hour
12 PNG 25 scm/hr PM
SO2
NOX
--
2.
D.G. Set
(250 KVA)
5 Diesel 25 lit/hr PM
SO2
NOX
--
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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3. Incinerator
(500 kg/hr)
30* PNG
50 scm/hr
PM
SO2
HCl
Dust
Collector
followed by
scrubber
**This will be a common stack for existing as well as proposed expanded incinerator
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing & Proposed
- Existing
Sr.
no.
Specific Source of emission
(Name of the Product &
Process)
Type of
emissi
on
Stack/Vent
Height
(meter)
Air Pollution
Control
Measures
(APCM)
1 Bromination Vessels (2 Nos).
(Bromohexine Hydrochloride &
During bromination reaction )
HBr
Br2
12 Two separate
two Stage Alkali
Scrubber
- Proposed
Sr.
no.
Specific Source of emission
(Name of the Product &
Process)
Type of
emissio
n
Stack/Ven
t
Height
(meter)
Air Pollution
Control
Measures
(APCM)
1 Bromination Vessels (2 Nos).
(Ambroxol Hydrochloride/
Acebrophylline & During
Bromination reaction,
Bromhexine base & During
Bromination reaction)
HBr
Br2
10 Two separate
two Stage Alkali
Scrubber
iii Fugitive emission details with its mitigation measures.
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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� Concrete road is/will developed within plot premises to avoid fugitive dust due to vehicle
movement.
� Manufacturing activity will be carried out in closed reactors / vessels and regular checking and
maintenance of the same will be carried out to avoid any leakage and relative fugitive
emissions.
� All the raw materials will be stored in closed containers and in sealed bags and will be handled
through closed system to avoid the handling losses and relative fugitive emissions.
Water sprinkling will be done to avoid dust emission.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary Movement Rules
2016).
Existing & Proposed
i Sr.
no
.
Typ
e/N
am
e o
f
hazard
ou
s
waste
Sp
ecif
ic
So
urc
e o
f
gen
era
tio
n
(Nam
e o
f th
e
Cate
go
ry a
nd
Sch
ed
ule
as Quantity (MT/Annum)
Man
ag
em
en
t
of
HW
Exis
tin
g
Pro
po
sed
To
tal
1. (a) ETP
Sludge
From Wet
Scrubbers
35.3 14.4 28.8 43.2 Collection,
Storage,
Transportat
ion and
Disposal at
TSDF –
BEAIL
Ankleshwar
/ VWEMCL
– Vapi.
(b) ETP
Sludge
From
treatment of
water to be
recycled
-- 24 24
Total (a+b) 14.4 52.8 67.2
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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2.
Process
waste water
*
From
manufacturing
process of
Acebrophyllin
e, Ambroxol
hydrochloride,
Bromhexine
Base,
Bromhexine
Hydrochlorid,
Timolol
Maleate,
2-Amino-n-
methyl-n-
cyclohexyl
benzenemeth
anamine
28.1 -- 1680 168
0
Collection,
Storage,
Transportat
ion and
disposed to
cement
industries
for co-
processing
or
Incineration
.
Distillation
Residue
From
manufacturing
process
28.1 0.36 35.64 36 Collection,
Storage,
Transportat
ion and
disposed to
cement
industries /
RSPL –
Panoli for
co -
processing.
3. Used Spent
Oil
From
lubrication or
D.G. Set
5.1 0.08 11.92 12 Collection,
Storage,
Transportat
ion and
Disposal by
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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selling to
registered
reprocesso
rs.
4. Empty
barrels /
containers /
liners
contaminate
d with
hazardous
chemicals /
wastes
From raw
materials
33.1 2.7 27.3 30 Collection,
Storage,
Decontami
nation,
Transportat
ion and
Disposal by
selling to
authorized
recycler.
5. Spent
Carbon
From
manufacturing
process of
Acebrophyllin
eAmbroxol
hydrochloride,
Bromhexine
Base,
Bromhexine
Hydrochloride
, Timolol
Maleate,2-
Amino-n-
methyl-n-
cyclohexyl
benzenemeth
anamine
28.3 1.2 13.2 14.4 Collection,
Storage,
Transportat
ion and
Disposed
to cement
industries /
RSPL -
Panoli.
6. Incineration
Ash*
From
Incinerator
37.2 35 51.4 86.4 Collection,
Storage,
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Transportat
ion and
Disposal at
TSDF site
of M/s.
BEAIL/
Ankleshwar
/ VWEMCL,
Vapi
7. Date expired
–off
specification
process
Expired
Products
28.4 0.005 0.115 0.12 Collection,
Storage,
Incineration
within unit.
8. Sodium
Bromide
Solution**
From
manufacturing
process
- 128.4 1118.4 124
7
Will be
collected,
stored,
transported
and sold to
authorized
end users
registered
under Rule
-9 and
users
having
PCB
Approvals.
9. Dimethyl
Hydantoin**
From
manufacturing
process
- 6 13.2 19.2 Will be
collected,
stored,
transported
and sold to
authorized
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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end users
registered
under Rule
-9 and
users
having
PCB
Approvals.
10
.
Bleed Liquor From
Scrubbing
1.2 2.4 3.6 Will be
incinerated
in an
incinerator
within
premises.
Note* - generated if process waste is not disposed for co – processing and is incinerated within
premises.
**- By-Products
ii Membership details of TSDF, CHWIF etc.
(For HW management)
BEAIL,VWEMCL, RSPL
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
-
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered
Solvents etc. (Details in Table Format)
Sr.
No.
Name of Product Name of Raw
Materials
/ Solvent
Raw Materials/
Solvent to be
Used
Raw Materials /
Solvent to be
Recovered
(MT/Month) (MT/Month) (%)
1. Bromhexine
hydrochloride
Industrial spirit 51200 49150 96
Methanol 18720 17800 95
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Mono
chlorobenzene 18000 17640 98
Toluene 76080 73110 96
2. 2-amino-n-methyl-n-
cyclohexyl
benzenemethanamine
Methanol 7488 7120 95
Mono
chlorobenzene 7200 7056 98
Toluene 16512 15860 96
3. Bromhexine base Industrial spirit 3036 2916 96
Methanol 3276 3115 95
Mono
chlorobenzene 3150 3087 98
Toluene 12964 12444.3 96
4. Ambroxol hydrochloride Acetone 3360 3180 95
Industrial spirit 11700 11220 96
Methanol 56160 53400 95
N-butanol 15840 15240 96
Toluene 103200 99060 96
5. Acebrophylline Acetone 970 922 95
Industrial spirit 1287 1235 96
Methanol 6180 5870 95
N-butanol 4840 4650 96
Toluene 17181 16459 96
6. Timolol maleate Acetone 7680 7220 94
Tert-butanol 5520 5280 96
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Toluene 12672 12048 95
Recovered solvents will be reused in process.
ii VOC emission sources and its mitigation measures
Closed loop systems, double mechanical seal pumps will be provided to reduce VOC emission
as much as possible.
H � Details regarding storage of Hazardouschemicals
Storage details Name of major Hazardous Chemicals Remarks
Storage tanks Hydrochloric acid
Drum/Barrel storage
Acetic acid, Acetone, Benzaldehyde, Benzoic
acid, Hydrazine hydrate, Industrial spirit,
Liquor ammonia, Maleic acid, Methanol,
Mono chlorobenzene, N-butanol, N-
methylcyclohexylamine, Ortho nitro
benzaldehyde, Ortho nitro toluene, Sodium
hydride, Sodium hydrosulphite, Soidum
borohydride, Tert-butanol, Theophylline,
Toluene, Trans-4-amino cyclohexanol
--
� Applicability of PESO : --
• During the meeting dated 19/08/2019, technical presentation made by the 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 baseline environmental quality has been assessed for various components of the environment
viz. air, noise, water, biological and socioeconomic aspect for the study area of 10 km radial distance
from project site for the period January 2019 to March2019. Ambient Air Quality monitoring was
carried out for PM10, PM2.5, SO2, NOx, HCl, HBr, & VOC as Benzene, Toluene & Xylene at eight
locations, including the project site. Values conform to the prescribed standards for Ambient Air
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Quality. The incremental Ground Level Concentration (GLC) has been computed using AERMOD.
The resultant concentrations are within the NAAQS. The modelling study proved that the air emissions
from the proposed plant would not affect the ambient air quality of the region in any significant
manner. The ambient air quality around the proposed project site will remain within the National
Ambient Air Quality Standards (NAAQS).
• Risk assessment including prediction of the worst-case scenario and maximum credible accident
scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site
Emergency Plan has been covered in the RA report.
• During SEAC meeting on 19/08/2019, committee noted that the proposal is for expansion. This unit
has 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. Source of water is
GIDC.PP mentioned that entire effluent generated after expansion from process, washing & scrubber
will be incinerated in in-house incinerator or will be sent to co-processing in cement industries. PP
mentioned that effluent generated from boiler blow down & cooling tower blow down will be recycled
back in the same process. Unit will maintain complete ZLD. PP has proposed one boiler & one
incinerator. Fuel used will be PNG. Committee noted that PP has not addressed LDAR (Solvent
Recovery) product wise and committee asked PP to submit revised LDAR product wise. Committee
also noted that PP has not addressed Hazardous Waste as per HWR – 2016 and was asked the
submit the revised table eliminating the by-product and incorporating the same in Hazardous Waste
Matrix. Committee also noted that PP has not satisfactorily address the likely impacts of project and
its mitigation measures along with technical details pertaining to best available technologies (BAT) for
the proposed project considering the expansion of existing products.
• After detailed discussion, it was decided to consider the proposal only after submission of the
following documents:
1. 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. Address all the solvents product wise
separately.
2. Technical Justification for direct recycle/reuse of utility effluent along with its treatability &
feasibility.
3. Technical details of the plant/s along with details on best available technologies (BAT), proposed
technology and reasons for selecting the same.
4. Anticipated environmental impacts due to the proposed project/production may be evaluated for
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significance and based on corresponding likely impacts VECs (Valued Environmental
Components) may be identified. Baseline studies may be conducted within the study area for all
the concerned/identified VECs and likely impacts will have to be assessed for their magnitude in
order to identify mitigation measures.
5. Revised Hazardous Waste Matrix addressing the by-product in Hazardous Waste as per HWR –
2016.
2 SIA/GJ/IND2/39992/2018 M/s. Altis Fine Chem Pvt. Ltd.
Survey No. 192, Near Katwad Patiya,
Dalpur, Prantij, Sabarkantha.
Appraisal
Category of the unit : 5(f)
Project status: Expansion
• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/39992/2018dated
30/08/2019 for obtaining Environmental Clearance.
• SEIAA issued TOR to PP vide their letter dated 28/01/2018.
• Public Hearing of the Project was Carried Out at Project Site of M/s.Altis Fine Chem Pvt Ltd,
Located at Survey No. 192, Near Katwad Patiya, Dalpur, Prantij, Sabarkantha. by Gujarat Pollution
Control Board dated 18/06/2019.
• Project proponent has submitted EIA Report prepared by Bhagwati Enviro Care Pvt. Ltd,
Ahmedabadbased on the TOR issued by SEIAA.
• This is an expansion project for manufacturing of synthetic organic chemical 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 Quinine
Sulphate
207671-44-
1 1 0 1
Pharmace
uticals
Drugs &
Drugs
Intermedia
tes
2 Ethyl-5
(piperazine-
yl-
benzafuran 2
carboxylate
765935-67-
9 1 0 1
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HCL)
3 3(4-
chlorobutyl)-
1H-Indole-5-
carbonitrile
143612-79-
7 1 0 1
4 Alanyl-L-
Glutamine 39537-23-0
0 8 8 5 2,3
Dihydroxy
Phthalazine-
1,4-Dione
1445-69-8
6 Alpha Keto
Isoleucine
Calcium Salt
66872-75-1 0 3 3
7 Alpha Keto
Leucine
Calcium Salt
51828-95-6 0 3 3
8 Alpha Keto
Phenyl
Alamine
Calcium Salt
54865-40-6 0 3 3
9 Alpha Keto
Valine
Calcium Salt
51828-94-5 0 3 3
10 Alpha
Hydroxy
Methionine
Calcium Salt
135236-72-
5 0 3 3
11 Aripiprazole 129722-12-
9 0 24 24
Total 3 47 50
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006.
• The unit is located outside GIDC, Complying the three conditions as per the amendment with EIA
Notification, 2006 vide SO 1599 (E) dated 25/06/2014. [The Water consumption less than 25 m3/day
(22.4 KLD); Fuel consumption is less than 25 TPD (0.92 MT/day); and not covered in the category of
MAH units as per the Management, Storage Import of Hazardous Chemical Rules (MSIHC Rules),
1989]
• PP was called for presentation in the SEAC meeting dated 19/09/2019.
• Salient features of the project are as under:
Sr.
no.
Particulars Details
A Total cost of Proposed Project
(Rs. in Crores):
Existing: 3.57 Crore
Proposed: 5.9 Crore
Total: 9.47 Crore
Details of EMP
Sr.
No
System Approximate
recurring
cost per
annum
(in Lacs)
Approximate
capital cost
(Rs. In Lacs)
Basis for cost estimates
1
Air pollution
control
2.0 8.0
The capital cost would include
cost of providing adequate height
of the stack, ladder and platform,
Air Pollution Control Systems and
recurring cost would include cost
of monitoring of air environment.
2
Water
pollution
control
160.0 10.0
Capital cost would include cost of
ETP, Evaporation cost of Spray
Drying etc. In capital cost civil
work, mechanical work, Electrical
20
550th meeting of SEAC-Gujarat, dated 19.09.2019
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work and piping work is included.
Recurring cost is for operational
phase.
3
Noise
pollution
monitoring
0.25 0.0
The recurring cost would include
cost of noise monitoring.
4
Solid and
hazardous
waste
management
3.0 10.0
Capital cost would include cost of
providing storage space for
hazardous waste and
membership of TSDF Fee.
Recurring cost would include cost
of land filling and transportation.
5
Environment
monitoring
and
management
1.0 1.0
The recurring cost would be
incurred on hiring of consultants
and payment of various statutory
fees to regulatory agencies.
6 Green belt 1.0 0.0
Development of Greenbelt
including Gardening and
Plantation.
7 Occupational
health (OHC) 1.5 1.0
Occupational health check up of
Employees and workers
Total 168.75 30
Details of CER as per OM dated 01/05/2018
9.6 Lacs for Three Year
(1.0 % of Total Project
Cost) For Brownfield
Project
M/s. Altis Fine Chem Pvt. Ltd. CER Budget:
9.6 Lacs (For Three Year)
Propose Planning for CER Activity (2019-2021)
21
550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 21 of 106
Cost in Lacs/Yr
2019 2020 2021
− 1.5 Lacs for Education
at Primary School of
Dalpur village.
i.e. will be provided
stationary, Books,
UniformO
− 1.0 Lacs for drinking
water facility provided in
Vajapur.
_Providing drink.ing water
station
− 1.0 Lacs for drinking
water facility.
_Provide Drinking Water
Stand at Katwad Patiya
for local people (near
our industries).
− 1.0 Lacs for Drinking
Water facility provided
in Dalpur village.
_Provided Drinking
Water Station
in Dalpur village.
− 1.5 Lacs for Education at
Vajapur village.
(Aganwadi Center &
primary school -Vajapur)
− 2.2 Lacs for Trees
Plantation at Vajapur
village. (with help of
local people)
Trees Plantation at
nearHathmati Canal.
Greenbelt area develop
inMehsana Highway
with help oflocal NGO.
− 0.7 Lacs for Green belt
area develop at near
Katwad Patiya with
help of local people
− 0.7 Lacs for trees
Plantation in Dalpur
village.
_with help of local people &
local
NGO.
Total: 3.2 Lacs Total: 3.2 Lacs Total: 3.2 Lacs
B Total Plot area
( sq. meter)
Existing: 17806 Sq. m.
Proposed: 0
Total: 17806 Sq. m.
Green belt area
( sq. meter)
Existing: 800 Sq. m.
Proposed: 5200 Sq. m.
Total: 6000 Sq. m.
C Employment generation Existing: 22
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Proposed: 50
Total: 72
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
Borewell
Status of permission from the concern authority.
Applied to CGWA
ii
Water consumption (KLD)
Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic 0.8
1.2 2.0
(B) Gardening
0 2.0 2.0
(C) Industrial
Process 1.4
14 15.4
Washing 0.5
0.5 1.0
Boiler 0.5
1.5 2.0
Industrial Total
2.4 16 18.4
Grand Total
(A+B+C)
3.2 19.2 22.4
1) Total water requirement for the project: 22.4 KLD
23
550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 23 of 106
2) Quantity to be recycled: 0
3) Total fresh water requirement: 22.4 KLD
(Total water requirement = Fresh water + Recycled water)
iii
Waste water generation (KLD)
Category Existing
KLD
Proposed
(Additional)
KLD
Total after
Expansion
KLD
Remarks
(A) Domestic
0.8 1.2 2.0
(B) Industrial
Process 1.2
14 15.2
Washing 0.5
0.5 1.0
Boiler 0.05
0.15 0.2
Total Industrial
waste water
1.75 14.65 16.4
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP
etc..
� ETP (Cap-40 KLD Primary & Tertiary Treatment Unit)
Treatment scheme including segregation at source. (Give Characteristics of
each stream i.e. COD, BOD, TDS etc.)
� Industrial Effluent Generation: 16.4 KLD _ goes to ETP (Cap-40 KLD,
having Primary & Tertiary Treatment Unit) then send to Common Spray
Drying Facility at Chhatral Environment Management System Pvt. Ltd. -
Dhanot for Spray Drying.
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550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 24 of 106
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b)
of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB
regarding compliance of CETP.
� Not Applicable
� Industrial Effluent Generation: 16.4 KLD _ goes to ETP (Cap-40 KLD,
having Primary & Tertiary Treatment Unit) then send to Common Spray
Drying Facility at Chhatral Environment Management System Pvt. Ltd. -
Dhanot for Spray Drying.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
� Industrial Effluent Generation: 16.4 KLD _ goes to ETP (Cap-40 KLD,
having Primary & Tertiary Treatment Unit) then send to Common Spray
Drying Facility at Chhatral Environment Management System Pvt. Ltd. -
Dhanot for Spray Drying.
v Mode of Disposal & Final meeting point
Domestic:
2.0 KLD discharge to Soak pit via septic
tank.
Industrial:
Industrial Effluent Generation: 16.4 KLD _
goes to ETP (Cap-40 KLD, having
Primary & Tertiary Treatment Unit) then
send to Common Spray Drying Facility at
Chhatral Environment Management
System Pvt. Ltd. - Dhanot for Spray
Drying.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE,
CHWIF etc.
Name of Common facility (CF)(For waste water treatment)
� Common Spray Drying Facility at Chhatral Environment System Pvt. Ltd. –
Dhanot
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Membership of Common facility (CF)
(For waste water treatment)
Common Spray Drying Facility at Chhatral Environment System Pvt. Ltd. - Dhanot
vii Simplified water balance diagram with reuse / recycle of waste water
vii Reuse/Recycle details (KLD)
[Source of reuse & application area]
Total reuse: 0
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)
26
550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 26 of 106
1
Boiler
(800
kg/hr)
(Existing)
12
Extra
cted
Bark
Wast
e
0.4
Particulate
Matter
SOx
NOx
Dust
Collector
2
Boiler
(3 MT)
(Propose
d)
30
White
Coal
OR
Briqu
ettes
0.92
Particulate
Matter
SOx
NOx
Multi
Cyclone
Dust
Collector
followed by
Bag Filter
- We will dismantle our existing Boiler (800 kg/hr) after obtaining Environment
Clearance.
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing & Proposed
- There will be no process gas emission in existing as well as proposed activity.
iii Fugitive emission details with its mitigation measures.
Fugitive emission will due to the leakages in pump, storage container, material
transferring, and packing.
Mitigation measures:
• Proper storage of raw materials, products and fuels
• Ensuring closed feeding and sampling.
• Establishing SOPs for start-up, shut down and maintenance operational
procedure
• Regular work place and ambient air quality monitoring will be done.
F Hazardous waste
(As per the Hazardous and Other Wastes (Management and Transboundary
Movement) Rules 2016.
Existing & Proposed
i
Sr
.
Type/Na
me of
Specific
Source
Categor
y and
Quantity
(MT/Annum)
Manageme
nt of HW
27
550th meeting of SEAC-Gujarat, dated 19.09.2019
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no
.
Hazardou
s waste
of
generati
on
(Name of
the
Activity,
Product
etc.)
Schedu
le as
per HW
Rules.
Existin
g
Propose
d
Tot
al
1
ETP
Waste
Effluent
treatment
plant
35.3 12 3 15 Collection,
Storage,
Transportat
ion &
Disposed at
TSDF
2
Spent
Oil/Used
Oil
Lubricatio
n of plant
machineri
es
5.1 8 4 12 Collection,
Storage,
Transportat
ion &
Disposed
by reuse as
lubricant in
the plant
3
Discarded
Container
s (Bag,
Barrel,
Drum)
Raw
material
section
33.1 2 3 5 Collection,
Storage,
Transportat
ion &
Disposed
by return
back to
supplier.
4 Process
Waste
(Bark)
From
Quinine
-- 310.5
6
0 310
.56
Collection,
Storage,
Transportat
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Sulphate
mfg.
process
ion & sale
to Rule 9
authorized
industries.
5
Distillation
Residue
Generate
d from
distillation
process
of
Toluene,
Methanol,
MTBE,
MDC,
Ethyl
Acetate,
Acetone,
Di ethyl
ether, IPA
36.1 0 19.32 19.
32
Collection,
Storage,
Transportat
ion and
disposal to
CHWIF.
6
Spent
Solvent
Generate
d from
distillation
process
of
Toluene,
Methanol,
MTBE,
MDC,
Ethyl
Acetate,
Acetone,
Di ethyl
ether,
-- 0 1798.32 179
8.3
2
Collection,
Storage,
recover &
reuse in
manufacturi
ng process
at our
premises.
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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IPA.
-
ii Membership details of TSDF, CHWIF etc.
(For HW management)
TSDF – Eco Care Infrastcture
Limited
iii Details of Non-Hazardous waste & its
disposal(MSW and others)
No
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered
Solvents etc. (Details in Table Format)
MT/MT (Batch Size 1 MT)
S
r.
N
o.
Product
Name
Solve
nt
Name
Prod
uct
Qty.
(MT/
M)
Solv
ent
use
Spent
Solve
nt
Lo
ss
Reco
ver
Solve
nt
Distilla
tion
Residu
e
Recov
ery %
1 Quinine
Sulphate
Tolue
ne 1 2 1.99
0.0
1 1.98 0.01 99.49
2
Ethyl-5
(piperazin
e-yl-
benzafura
n 2
carboxylat
e HCL)
Ethyl
Aceta
te
1 6.52 6.5 0.0
2 6.47 0.03 99.54
3
3(4-
chlorobutyl
)-1H-
Indole-5-
carbonitrile
MDC 1 8 7.98 0.0
2 7.93 0.05 99.37
4 Alanyl-L-
Glutamine
Metha
nol 8 6.51 6.5
0.0
1 6.46 0.04 99.38
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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5
Alpha Keto
Isoleucine
Calcium
Salt
MTBE 3 2.07 2.05 0.0
2 2.02 0.03 98.54
6
Alpha Keto
Leucine
Calcium
Salt
MTBE 3 2.1 2.07 0.0
3 2.04 0.03 98.55
7
Alpha Keto
Phenyl
Alamine
Calcium
Salt
MTBE 3 1.72 1.7 0.0
2 1.67 0.03 98.24
8
Alpha Keto
Valine
Calcium
Salt
Aceto
ne 3 0.97 0.94
0.0
3 0.92 0.02 97.87
Di
ethyl
ether
3 2.31 2.3 0.0
1 2.28 0.02 99.13
9
Alpha
Hydroxy
Methionine
Calcium
Salt
Metha
nol 3 1.85 1.83
0.0
2 1.8 0.03 98.36
1
0
Aripiprazol
e
Iso
Propy
l
Alcoh
ol
24 2.05 2.03 0.0
2 2 0.03 98.52
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
H � Details regarding storage of Hazardous chemicals
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Storage details Name of major
Hazardous chemicals
Remarks
Storage tanks
Toluene Tank Size: –
10 MT
Drum/Barrel storage
− Acetone
− Ethyl Acetate
− Hydrazine Hydrate
− Hydrochloric Acid
− Iso Propyl Alcohol
− Sodium Hydroxide
− Sulphuric Acid
− Titanium Tetra
Chloride
Drum – 50
kg, 100 kg,
150 kg, 200
kg
� Applicability of PESO :
� PESO Permission obtained for Storage of 15 KL Raw Material
• During the meeting dated 19/09/2019, technical presentation made by the 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 baseline environmental quality has been assessed for various components of the environment
viz. air, noise, water, biological and socioeconomic aspect for the study area of 10 km radial distance
from project site for the period October 2018 to December2018. Ambient Air Quality monitoring was
carried out for PM10, PM2.5, (SO2), (NOx), HC, CO and VOCsat 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. 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
32
550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 32 of 106
scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site
Emergency Plan has been covered in the RA report.
• During SEAC meeting on 19/09/2019, committee noted that the proposal is for expansion. This unit
has 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. Source of water is
Bore well.PP mentioned that entire effluent generated after expansion from process, boiler blow down
& washing shall be treated in in-house primary & tertiary ETP and treated effluent will be sent to
Common Spray Drying Facility at Chhatral Environment System Pvt. Ltd. – Dhanot. PP mentioned
that they will dismantle the existing boiler. PP has proposed one new steam boiler. Fuel used will be
White Coal. PP has addressed Hazardous Waste as per HWR – 2016.
• After detailed discussion, it was decided to forward the proposal to SEIAA, Gujarat for grant of
Environment Clearance.
3 SIA/GJ/IND2/37351/2018 M/s. Transworld Furtichem Pvt Ltd
Plot No. 353 to 367, Sector-4, KSEZ,
Gandhidham, Kutchh.
Appraisal
• PP remained absent in the EC – Appraisal presentation held on 19/09/2019.
• After detailed discussion, Committee decided to defer the proposal and consider the same in
one of the upcoming meeting of SEAC.
4 SIA/GJ/IND2/38556/2019 M/s. Anju Life Science
Plot No. C-261, G.I.D.C. Industrial
Estate, Saykha, Tal: Vagra, Dist.:
Bharuch, Gujarat – 391340.
Screening &
Scoping
• PP remained absent in the Screening & Scoping presentation held on 19/09/2019.
• After detailed discussion, Committee decided to defer the proposal and consider the same in
one of the upcoming meeting of SEAC.
5 SIA/GJ/IND2/40809/2019 M/s. Ooxylic Solutions
Plot No.33 & 36 GIDC Estate, Sojitra,
Anand.
Screening &
Scoping
Category of the unit: 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/40809/2019 dated
33
550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 33 of 106
29/08/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for
preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is a new unit proposes for manufacturing of synthetic organic chemicals as tabulated as below:
Sr.
No.
Name Of Product
CAS NO. Production
Capacity
MT/Month
End use of the product
as
1 Equilibrium Peracetic acid
(35%)
79-21-0 500 Cleaning agent in addition
to a cold disinfectant,
Synthesis of Alkenes &
Organic Compound
2 Distilled Peracetic acid (65
%)
79-21-0 100 Cleaning agent in addition
to a cold disinfectant,
Synthesis of Alkenes &
Organic Compound
3 2-Phenyl Propionic acid 492-37-5 20 2-Phenylpropionate is an
intermediate in alpha-
Methyl styrene (2-
phenylpropylene)
metabolism
4 Alpha Pinene Oxide
OR
Alpha Campholenic Aldehyde
1686-14-2
OR
110 Food additive, flavor
5 Sodium Acetate Powder 127-09-3 127 Sodium acetate is added
to food to help prevent
bacterial growth
6 Different Epoxides
1) Styrene oxide 96-09-3 50 Fragrance, Electronics,
Automotive
2) Limonene oxide 203719-54-4 Air fresheners, fragrance,
Cleaning, Washing, Food
Additive
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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3) Isopulegol epoxide 13834-13-4 Active compounds and
pharmaceuticals
4) Linalool oxide 1365-19-1 Fragrance
TOTAL 907 -
• 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 19/09/2019.
• Salient features of the project including Water, Air and Hazardous waste management:
Sr.
no.
Particulars Details
A
A Total cost of Proposed Project
(Rs. in Crores):
3.5Crore.
B Total Plot area ( sq. meter)
2107Sq. m.
Green belt area
( sq. meter)
710.11 Sq. m.
C Employment generation
12
D Water
i
Source of Water Supply
(GIDC Bore well, Surface water, Tanker supply etc...)
GIDC Estate, Sojitra
Status of permission from the concern authority. GIDC, Sojitra. has allotted the plot
with commitment to provide
infrastructure facility and water
requirement
Ii
Water consumption (KLD)
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550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 35 of 106
Sr. No. Water required for Quantity
(KLD)
Remark
1. Domestic 1.0 1.0 KLD Fresh Water
2. Gardening 1.0 1.0 KLD Fresh Water
3. Industrial
a. Process 0.0 DM water will be used.
b. Cooling 3.0 3.0 KLD Recycle Distillate
c. Washing 0.2 0.2 KLD Fresh Water
Total (a+b+c) 3.2 0.2 KLD Fresh Water
3.0 KLD Recycled Water
Total (1+2+3) 5.2 2.2 KLD Fresh Water
3.0 KLD Recycled Water
Note: Total Fresh Water Consumption: 5.2 KLD
Reuse: 3.0 KLD
After Reuse Fresh Water Consumption: 2.2 KLD
Iii
Waste water generation (KLD)
Sr. No.
Waste Water
Generation
Quantity (KLD) Remark
1. Domestic 0.8 Discharge to Soak pit
2. Gardening - -
3. Industrial
a. Process 10.6 7.6 KLD will be Reused
as DM water in to
Process & 3.0 KLD
Cooling as make up
b. Cooling 0.3 0.3 KLD will be treated
in To ETP
c. Washing 0.2 0.2 KLD will be treated
in To ETP
Total (Industrial to
ETP)
11.1 10.6 KLD will be
Recovered & reused in
36
550th meeting of SEAC-Gujarat, dated 19.09.2019
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Processand cooling
make up
+
0.5 KLD will be treated
in To ETP
� 0.8 KLD Domestic Effluent will be Discharge to be soak pit.
� 0.5 KLD Industrial Effluent will be treated in the ETP & evaporated by steam jacketed
evaporator.
� 10.6 KLD distillate water will generate during manufacturing of Sodium Acetate
Solution, 7.6 KLD will be recovered and reused in process and 3.0 KLD will be as
cooling tower makeup.
Iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.
� ETP (Primary) + Evaporator
Treatment scheme including segregation at source.
� ETP (Primary) + Evaporator
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1) (b) of the
Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding
compliance of CETP.
� No
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
� Treated effluent will be treated in ETP and evaporated by steam jacketed evaporator.
V Mode of Disposal & Final meeting point
Domestic: Soak pit
Industrial: ZLD
Vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. Name
of CF
� NA
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Membership of Common facility (CF)
(For waste water treatment)
� NA
Vii Simplified water balance diagram with reuse / recycle of waste water
viii Reuse/Recycle details (KLD)
Total reuse : 10.6KLD
Source of waste
water for reuse
with quantity in
KLD (From where
it is coming)
Application
area with
quantity in
KLD (Where it
is used)
Characteristics of
waste water to be
reused (COD, BOD,
TDS etc.)
Remarks
regarding
feasibility to
reuse i.e.
Condensate from
distillation process
of manufacturing
Sodium Acetate
7.6 KLD in
Process
pH: 7.51
COD:9
BOD:3
TDS:100
It is distillate
can be used
as DM water
38
550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 38 of 106
water- - - -
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
.
Stack
Attached
to
Stack
Heig
ht
(m)
Fuel
Used
Quantity
of Fuel
Pollutants
Permissible
Limit
APCM
1.
TFH
5 Lac
Kcal
15 Natural
gas/
Agro
Waste
300
SCM/
0.8 TPD
PM/NOx-
/SO2
PM<150
mg/Nm3
SO2<100
PPM/
NOx<50 PPM
Adequate
Stack
Height/
Dust
Collector
ii Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
� No Process gas emission
iii Fugitive emission details with its mitigation measures:
As below:
Proposed project is of manufacturing of S. O. Chemicals. Followings Measures will take for
existing & proposed project.
� Maintaining the house keeping regularly
� Transferring the liquid materials by pump
� To carry out regular leak detection and repair activities
� Proper routine maintenance of equipment reduces the likelihood of leaks
F Hazardous wastes
(as per the Hazardous and Other Wastes (Management and Transboundary Movement)
Rules 2016.
i
Sr.
No. Waste
Category
as HWM
Rules 2016
Source
Quantity
(MT/
Year)
Management Facility
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550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 39 of 106
1 ETP sludge
34.3
ETP 2
Collection, storage,
transportation, disposal at
the approved TSDF site
2 Distillation
Residue SCH-I/ 20.3
Solvent
Recovery
1
Collection, storage,
transportation, disposal at
the approved CHWIF site
3 Spent
Solvent SCH-I/ 28.6
Manufacturi
ng process
of
Campholeni
c Aldehyde,
2-Phenyl
Propionic
acid, Alpha
Pinene
Oxide
Alpha
Campholeni
c Aldehyde,
Different
Epoxides
464 Collection, storage,
transportation & reusing in
next batch.
4 Discarded
Containers 33.1
Materials
container
0.5
Collection, storage,
transportation, disposal by
selling to Registered
recycler.
5 Used Oil 34.3 Machinery
0.01
Collection, storage,
transportation, disposal by
selling to Registered
recycler.
ii Membership details of TSDF, CHWIF etc.
(For HW management)
Membership of TSDF/CHWIF site
will be carried out before starting
the production activity.
iii Details of Non-Hazardous waste & its disposal Non Hazardous recycling waste
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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(MSW and others) will be sold to the registered
recycler.
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.
(Details in Table Format)
Type of Solvent Details of Solvent
Recovery
% of Recovery Reuse of
Solvent
Toluene Distillation 99.97 Recycle in next
batch
Dichloroethane Distillation 99.80 Recycle in next
batch
ii VOC emission sources and its mitigation measures
� VOC will be observing due to the use of solvent. To minimize the VOC level below
the CPCB norms we will be taken action as follows.
� Pump and pipes will be provided for transferring of solvent.
� Raw materials will be kept in closed container.
� Regular monitoring of the storage container and transferring system.
H � Details regarding storage of Hazardous chemicals
Storage details Name of major Hazardous
chemicals
Remarks
Storage tanks
Alpha Piene,
Toluene
Ethylene Dichloride
� 24 tanks X 2000 liters
� 9 tanks X 10000 liters
� 4 tanks X 1000 liters
Drum/Barrel storage
Peracetic Acid,
Isopulegol,
Styrene Monomer,
Sulfuric Acid
HDPE container
� Applicability of PESO : Not Applicable
• During the meeting dated 19/09/2019, technical presentation made by the Project proponent.
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550th meeting of SEAC-Gujarat, dated 19.09.2019
Page 41 of 106
• Committee noted that this proposal is new in GIDC Sojitra. Source of Water is GIDC. PP mentioned
that condensate effluent will be generated from process which will be reused back in process and
cooling tower make up, while effluent generated from washing & cooling tower blow down will be
treated in proposed in-house primary ETP followed by steam jacketed evaporator. Unit will maintain
complete ZLD. PP has proposed one thermic fluid heater. Fuel used will be Natural Gas/Agro Waste.
PP has addressed Hazardous Waste as per HWR – 2016.
• After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant
of Terms of Reference.
• 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. Explore the use of renewable energy to the maximum extent possible. Details of provisions
to make the project energy-efficient through 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.
3. 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.
4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard
during unloading, storage, transportation, handling and processing of Solvents.
5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form.
6. Technical Justification for no waste water generation from process and use of condensate
in process and cooling tower make up along with its treatability & feasibility.
• 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
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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information as per the generic structure of EIA given in Appendix III in the EIA Notification, 2006.
• Further Project Proponent may be advised to submit final EIA Report with EC application within 100
days from the date of issuance of this ToR to expedite processing of Environment Clearance
application.
• The project proponent shall have to apply for Environmental clearance through online portal
http://environmentclearance.nic.in/ along with final EIA report.
6 SIA/GJ/IND2/40919/2019 M/s. Perivinc Pharmaceuticals Pvt
Ltd.
Plot No.: 257, GIDC Estate, Hansalpur,
Viramgam, Dist.: Ahmedabad.
Screening &
Scoping
Category of the unit: 5(f)
Project status: Expansion
• This office has received an application vide their online proposal no. SIA/GJ/IND2/40919/2019 dated
29/08/2019 made by project proponent (PP) 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 for chemical manufacturing and now proposes for expansion in manufacturing
of new synthetic organic chemicals as tabulated as below:
Sr.
No.
Name of the
Products CAS.NO
Existing Proposed Total after
Expansion Uses
MT/Month MT/Month MT/Month
1 Herbal Extract
(Vinea Alkaloids) - 0.5 -0.5 0.0 -
2 Trihexy Phenidyl-
HCl 52-49-3 0.0 0.70 0.70
Healthcare 3 Procyclidine-HCl 1508-76-5 0.0 0.40 0.40
4 Pantoprazole
Sodium 164579-32-2 0.0 2.8 2.8
5 Levosulpride 23672-07-3 0.0 1.834 1.834
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6 Bromhexine-HCl 611-75-6 0.0 1.5 1.5
Total 0.5 7.234 7.234
• 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 19/09/2019.
• 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):
Proposed: Approx Rs. 300 Lacs
B Total Plot area (sq. meter)
2248.5 Sq.m
Green belt area
( sq. meter)
744 Sq. m
C Employment generation
Proposed: 25 people
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. Required permission obtained
ii
Water consumption (KLD)
Sr.
No.
Source
Water Consumption (KL/Day)
Existing
Quantity
Proposed
Quantity
Total
Quantity
1. Domestic 3 0 3
2. Gardening - 2.5 2.5
3. Industrial
A. Process 14.0 -13.4 0.6
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B. Boiler 5.0 -3.0 2.0
C. Washing 3.0 -1.0 2.0
D. Cooling - +2.0 2.0
Total Industrial 22.0 -15.4 6.6
Total
(Domestic + Industrial) 25.0 -12.9 12.1
Total water requirement for the project: 12.1 KLD
Quantity to be recycled: 0 KLD
Total fresh water requirement: 12.1 KLD
iii
Waste water generation (KLD)
Sr.
No.
Source
Waste Water Generation (KL/Day)
Existing
Quantity
Proposed
Quantity
Total
Quantity
1. Domestic 2.5 0 2.5
2. Gardening - - -
3. Industrial
A. Process 3.0 -1.7 1.3
B. Boiler 0.5 -0.2 0.3
C. Washing 3.0 -1.0 2.0
D. Cooling - 0.3 0.3
Total Industrial 6.5 -2.6 3.9
Total
(Domestic + Industrial) 9.0 --2.6 6.4
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..
ETP: 10 KLD, Stripper: 0.5 KL/hr
v Mode of Disposal & Final meeting point
Domestic: Septic Tank/soak pit system
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Industrial:
Treated effluent will be sent to Common Spray
Drying Facility developed by M/s. Chhatral
Environmental Management System Pvt. Ltd.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , Name
of CF
Unit has already obtained membership for disposal of treated effluent at Common Spray
Drying Facility developed by M/s. Chhatral Environmental Management System Pvt. Ltd.
Membership of Common facility (CF)
(For waste water treatment)
Obtained
vii Simplified water balance diagram with reuse / recycle of waste water
Fresh Water (12.1) (First Day)
Domestic
0.30
Septic Tank
2.0
Process
(0.6)
0.3
Washing(2
.0)
Boiler(2.0) Cooling
(2.0)
ETP (3.9)
Gardening Industrial (6.6)
Treated Effluent will be sent to Spraying Drying Facility Developed by M/s.
Chhatral Common Environment Management Facility
1.3
Stripper
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viii Reuse/Recycle details (KLD)
Total reuse: 0 KLD of water
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
.
N
o.
Stack
Attached
to
Type of Fuel &
Rate of Consumption Stack
Heigh
t (m)
APC
M
Parameter &
Permissible
Limit
Existing Proposed
after
expansion
1
Steam
Boiler
(1 No.)
Wood –
200
Kg/day
Agro waste
Briquettes –
800 Kg/day
32 Bag
Filter
PM < 150
mg/Nm3
SO2< 100 ppm
NOx< 50 ppm
Proposed
Sr.
No
.
Stack
Attached to
Type of Fuel
&
Rate of
Consumption
Stack
Height
(m)
APCM
Parameter &
Permissible
Limit
2
D.G Set -
1 Cap.
250 KVA
HSD: 10
lit/hr 12
Acousti
c
Enclos
ure
PM < 150
mg/Nm3
SO2< 100
ppm
NOx< 50 ppm
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
Existing: There is no process emission from the production of existing product.
Proposed: For Fugitive emission
Sr.
No. Stack Attached to
Stack
Height
(m)
APCM Parameter &
Permissible Limit
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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1 Solvent Storage Area & Process
Area 8 meter
Packed
Carbon
Column
-
iii Fugitive emission details with its mitigation measures.
As below:
� Regular sprinkling of water is carried out & green belt is provided within premises to
prevent fugitive emissions due to vehicular movement. Regular maintenance of vehicles.
� Management to ensure proper handling of the spillages during transfer, charging operation
and provision of a Dust Collection System for collection of the air borne material wherever
applicable.
� Preventive maintenance of flange connections and glands of pumps.
� Management will also ensure proper usage of the Personnel Protective Equipment by the
workers.
� Closed handling system shall be provided for chemicals.
� Reflux condenser to be provided over the reactor.
� The raw materials shall be taken from storage tanks to reactor through closed pipeline.
Storage tanks shall be vented through trap receiver
� Fugitive emissions in the work zone environment, product raw material storage area will be
monitored regularly.
-
F Hazardous wastes
(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules
2016.
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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i Sr
.
No
.
Type of
Waste
Categ
ory
Existin
g
Quanti
ty
Propose
d
Quantity
Total after
expansio
n
Mode of Disposal
1. Used Oil 5.1 -- 0.5
MT/YEAR
0.5
MT/year
Collection, Storage ,
Transportation , Reuse and/or
Disposal by selling to Registered
Re-refiners
2.
Empty Barrels
Glass Bottle
Liners,
Containers
33.1
2.28
MT/YE
AR
3.72
MT/Year
6.0
MT/Year
Collection, Storage,
Decontamination, transportation,
disposal by selling to authorized
recycler.
3.
Process
Wastes,
Residues &
Wastes
21.1
29.5
MT/Ye
ar
-29.5
MT/Year Nil
Collection, Storage,
Transportation, Disposal at
Registered TSDF or Disposal by
co-processing or Incineration
4. Spent Solvent 26.4
540
MT/Ye
ar
195.84
MT/Year
735.84
MT/Year
Collection and
Distillation in-house/recovery &
reused
5. Distillation
residue 26.3 --
6.0
MT/Year
6.0
MT/Year
Collection, Storage,
Transportation, Disposal by co-
processing or Incineration
6.
Chemical
Sludge from
wastewater
treatment
35.3
9.36
MT/Ye
ar
-4.36
MT/Year
5.0
MT/ Year
Collection, Storage,
transportation and disposal at
any registered TSDF site.
ii Membership details of TSDF, CHWIF etc.
(For HW management)
Will be obtained before
going for production
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
--
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Name of
Product
Reacti
on
Stage
Name of
Solvent
Input Recovery
%
Recovery
Machiner
y End
Use Kg/
Mont
h
Kg/
Month Used
Trihexy
Phenidyl-HCl
I & II Methanol 2870 2660 92.68% Separate
distillation
Col. With
Reactor
Re
used
in
next
batch
II Toluene& THF 3500 1645 94.00%
Procyclidine-
HCL
I & II Methanol 2050 1900 92.68%
II Toluene& THF 2500 2350 94.00%
Pantoprazol
e Sodium
I Methanol 8800 8160 92.73%
II Acetone 9600 8920 92.92%
III Acetone 1120
0 10560 94.29%
Levosulpride I
Ethylene
Glycol 3850 3696 96.00%
Methanol 1155
0 10850 93.94%
Bromhexine-
HCL I Methanol 5400 5040 93.33%
ii VOC emission sources and its mitigation measures
� Breather valves will be provided on solvent tanks.
� To eliminate chances of leakages from glands of pumps, mechanical seal will be provided
at all solvent pumps.
� Entire process will be carried out in the closed reactors with proper maintenance of
pressure and temperature.
� Periodic monitoring of work area will be carried out to check the VOC emission.
Solvent recovery system will be provided with chilled water condenser system
• During the meeting dated 19/09/2019, technical presentation made by the Project proponent.
• Committee noted that the name of the Project is “SELF REGISTRATION” and asked PP to clarify
about the same. PP mentioned that they have made an error while applying the application and they
will submit the required documents for the name change/correction of the same.
• Committee noted that this proposal is for expansion. Unit is located at GIDC, Hansalpur. Unit has
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valid CC&A. Unit has submitted Compliance of CC&A. PP ensured that there is no court case and
public complaint against this unit. Source of water is GIDC. PP mentioned that they will surrender
existing products hence all the effluent coming out from existing plant will be NIL. PP mentioned that
effluent generated after expansion from process, washing, cooling tower blow down & boiler blow
down will be treated in in-house primary ETP and treated effluent will be sent to Common Spray
Drying Facility developed by M/s. Chhatral Environmental Management System Pvt. Ltd for final
treatment and disposal. Committee noted that PP has not satisfactorily addressed water balance
diagram and water consumption and generation table. PP has proposed one standby D.G. Sets. Fuel
used will be HSD. Committee noted that PP has not addressed process stack considering the mass
balance of product profile and have not incorporated any APCM for the same. Committee also noted
that PP has not addressed Bleed Liquor in Hazardous Waste which will be coming out of process
stack.
• After detailed discussion, it was decided to consider the proposal only after satisfactory
submission of the following details.
1. Revised Water Balance Diagram Considering Expansion scenario and addressing the Water
Consumption & Generation Table Considering the Same.
2. Addressing the Process Stack Considerig the Expansion in Product Profile along with its APCM.
3. Revised Hazardous Waste Matrix Considering Bleed Liquor from APCM of Process Stack and
Sound Management of the Same.
4. Authenticated Documents for change of name of Project from “Self Registration” to “Perivinc
Pharmaceuticals Pvt Ltd”.
7 SIA/GJ/IND2/40968/2019 M/s. Paras Pharma Chem
Plot No. C-235, GIDC Indu. Estate,
Saykha, Vagra, Bharuch.
Screening &
Scoping
Category of the unit: 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/40968/2019 dated
29/08/2019 made by project proponent (PP) 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.
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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• This is a new unit proposes for manufacturing of synthetic organic chemicals as tabulated as below:
Sr.
No
Product Name CAS No. Proposed
Quantity
(MT/Month)
End Use Of Product
1. 1,3 DICHLORO DIMETHYL
HYDANTOIN
112-36-7
750
Pharma & Water Treatment
2. 1,3 Dibromo-5,5- Dimethyl
Hydantion
77-48-5 Pharma Industries
3. 5,5 Dimethyl Hydantion 77-71-4 Pharma Industries
4. 2,2-Azobisisobutyronitrile 78-67-1 Pharma, Polymer,Paint And
Pesticides Industries
5. Benzoyl Peroxide 94-36-0 Paint & Polymer Industries
6. MEK Peroxide 1338-23-4 Paint & Polymer Industries
7. LABSA 27176-87-0 Use In Detergents Industries
8. Methyl Methacrylate (MMA) 80-62-6 Acrylic Resin, Paint & Plastic
Industries
9. Acrylic Emulsion 25067-01-0 Textile , Paper & Leather
Industries,
10. VAM Emulsion 108-05-4 Textile, Paint Industries
11. Sodium Hypochlorite 7681-52-9
350
Textile & Paper Bleaching
12 Calcium Chloride 7440-70-2 Paint & Dyes Industries
13 Benzalkonium Chloride (BKC-50) 8001-54-5 Clinical Products
14 Benzalkonium Chloride (BKC-80) 8001-54-5 Clinical Products
15 Amine Oxides 1643-20-5 Clinical Products
16 Pearl Essence 8039-79-0 Used in Paint and Plastic
Industries
17 Cobalt Octate 13586-82-8 Paint & FRP Plastic
Industries
18 TRO Turky Red Oil 8002-33-3 Antifoaming Agent & Textile
Industries
19 Coco Diethanolamide 68603-42-9 Cosmetic & Toiletries
20 Solvent Based Paints ---- Use in Wooden,Metal,
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Household & Industrial Use
TOTAL: 1100
• 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 19/09/2019.
• Salient features of the project including Water, Air and Hazardous waste management:
Sr.
no.
Particulars Details
A
A Total cost of Proposed Project
(Rs. in Crores):
9.50 Crores
B Total Plot area ( sq. meter) 8304.338 Sq. m.
Green belt area ( sq. meter) 2689.11 Sq. m.
C Employment generation 80
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 the
permission letter from
GIDC.
Ref
No:GIDC/EE(W/D)/BRH/
585
ii Water consumption (KLD)
Category
Quantity
KLD
Remarks
(D) Domestic 3.0
(E) Gardening 10.0
(F) Industrial
Process 37.0
Washing 30.0
Boiler 9.5
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Cooling 8.5
Scrubber 2.0
Industrial Total 87.0
Total (A + B + C) 100.0
7) Total water requirement for the project: 100 KLD
8) Quantity to be recycled: 68 KLD
9) Total fresh water requirement: 32 KLD
iii Waste water generation (KLD)
Category Waste water
KLD
Remarks
(C) Domestic 2.0
(D) Industrial
Process 40.0 Stream-I: Low COD &
TDS: 69 KLD
Stream-II:Utilites: 2 KLD
Washing 29.0
Boiler 1.0
Cooling 1.0
Scrubber 2.795 Reuse and sell end users
having permission under
rule-9
Total Industrial waste
water
73.795
Total [A + B + C] 75.795
-
Iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP
etc.
� ETP (Primary,Secondary& Tertiary): 69 KLD
Treatment scheme including segregation at source.
Stream I (RAW EFFLUENT Stream) (69 KLD)
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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First all non-toxic and biodegradable (streams I) of wastewater shall pass through
Oil & Grease Removal Tank (OGRT-01) where floating O & G shall be removed
manual from top and collected in O & G Collection Tank (OGCT-01).
Then 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 Tanks (LDT-01-A/B) as per
requirement with help of Lime Dosing Pumps. Then after, neutralized wastewater
shall go to Flash Mixer (FM-01) by gravity. Alum shall be dosed from Alum Dosing
Tanks (ADT-01-A/B) with help of Dosing Pumps. Then after, coagulated
wastewater shall be settled in Primary Settling Tank-1 (PST-01).
Clear supernatant from PST-01 shall be passed in Aeration Tank (AT-01). Here,
biodegradation of organic matter of the wastewater shall be carried out by bacteria
(suspended growth) in the AT-01 and for that oxygen shall be supplied by 2 nos.
of air blowers (B-02) through diffusers. Air blowers also keep MLSS in
suspension.
Then after, wastewater shall go to Secondary Settling Tank (SST-01). Here, the
suspended solids shall be settled at bottom. Sludge shall be removed from bottom
of SST-01 and pumped to AT-1 to maintain MLSS and excess activated sludge
shall be sent to Sludge Sump (SS-01). Clear supernatant from SST-01 shall be
collected in Intermediate Sump (IS-01) by gravity.
Thereafter, the wastewater shall be passed through Pressure Sand Filter (PSF-
01) to remove left out TSS and Activated Carbon Filter (ACF-01) for final effluent
polishing. After tertiary treatment, effluent shall be collected in Treated Effluent
Sump (TES-01) before sent to RO-01 for further treatment. RO-01 permeate
water shall be collected in RO Treated Water Tank (ROTWT-01) before reuse in
plant. RO-01 reject shall be sent to Single Stage Evaporator (SSE-01).
Condensate water from SSE-01 shall be reuse/recycle in boiler or cooling for
future treatment.
Sludge settled in PST-01 and excess sludge from SST-01 shall be collected in
Sludge Sumps (SS-01) then sludge shall be pumped to Centrifuge (CF-01) where
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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poly shall be mixed from poly Dosing Tank-2 (PDT-02) with sludge to increase
efficiency of centrifuge sludge dewatering. Then, dewatered sludge shall be
stored in in HWSA and then ultimate disposal to TSDF. Leachate from CF-01 and
backwash from PSF-01 and ACF-01 shall be collected in Drain Pit and pumped
back to ENT-01 for further treatment.
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1)
(b) of the Water (Prevention and Control of Pollution) act, 1974 issued by
CPCB regarding compliance of CETP.
� Not Applicable
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
� Source of water will be met through Saykha GIDC Water Supply.Total water
requirement will be 100 KL/Day (Fresh Water: 32 KL/Day +RO Permeate: 60
KL/Day +Condensate Water:8 KL/Day).
� Total 75.795 KL/Day (73.795 KL/Day: Industrial + 2.0 KL/Day: Domestic) of
effluent shall be generated.
� Stream-I: 69 KL/day low COD & TDS stream (from process & Washing) will
be treated in ETP giving primary, secondary & Tertiary treatment then sent to
RO for further process.
� Stream-II: 2 KL/day utilities stream (from Boiler, cooling) will be send to RO.
Total 71 KL/day (from Boiler, cooling & Treated effluent from ETP ) will be
treated in RO & 60 KL/day RO permeate will be reused in Industrial Water
requirement & RO reject will be sent to Inhouse Single Stage Evaporator and
than pass through condense. Condensate water shall be reuse/recycle in
boiler or cooling.
� 2.795 KL/Day Scrubber wastewater Will be reused or sold to end users having
permission under Rule-9.
� 2 KL/Day Domestic waste water will be sent to Septic Tank & Soak Pit.
v Mode of Disposal & Final meeting point
Domestic: Domestic waste water (2.0 KL/day) will be disposed by septic tank
or soak pit system
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Industrial: � Stream-I: 69 KL/day low COD & TDS stream (from process
&Washing) will be treated in ETP giving primary, secondary &
Tertiary treatment then sent to RO for further process.
� Stream-II: 2 KL/day utilities stream (from Boiler, cooling) will
be send to RO.
Total 71 KL/day (from Boiler, cooling & Treated effluent from
ETP ) will be treated in RO & 60 KL/day RO permeate will be
reused in Industrial Water requirement & RO reject will be sent
to Inhouse Single Stage Evaporator and than pass through
condense. Condensate water shall be reuse/recycle in boiler or
cooling.
� 2.795 KL/Day Scrubber wastewater Will be reused or sold to end
users having permission under Rule-9.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE
etc. Name of CF
� Not Applicable, Unit has Zero Liquid Discharge.
vii Simplified water balance diagram with reuse / recycle of waste water
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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Note:
When CETP, Saykha will be operational then after unit will discharge effluent to CETP,
Saykha for further treatment after primary, secondary & Tertiary treatment in ETP.
viii Reuse/Recycle details (KLD)
Total reuse: 34.0 KLD
Source of waste
water for reuse
with quantity in
Application
area with
quantity in
Characteristics of
waste water to be
reused (COD, BOD,
Remarks
regarding
feasibility
Raw Water: 100
Dom: 3.0
Process Boiler Cooling
Septic Tank & Soak
Pit: 2
Ind: 87 Gardening: 10
1 40 2.795
Washing
29
Other : 2
1
Will be reused or
sold to end users
having permission
under Rule-9.
RO Reject : 11
ETP (69)
(Primary, Secondary, Tertiary)
RO:71 RO Permeate :60
Reuse/recycle
Single Stage Evaporator
Condenser Condensate water: 8
Reuse/Recycle in
Salt to sludge drying
Steam: II 2
KLD Utilities
Steam-I 69 KLD Low
COD & TDS Steam
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KLD (From
where it is
coming)
KLD (Where it
is used)
TDS etc.) to reuse i.e.
RO Permeate: 60
KLD
Condensate
Reuse Water:8
KLD
Industrial
Water: 60 KLD
Boiler &
Cooling:8 KLD
COD: 70 mg/l
BOD: 30 mg/l
TDS: 2000 mg/l
COD: 50 mg/l
BOD: 20 mg/l
TDS: 150 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.
-
Sr.
no
.
Source
of
emissio
n
With
Capacity
Stack
Height
(meter
)
Type of
Fuel
Quantit
y of
Fuel
MT/Day
Type of
emission
s i.e. Air
Pollutant
s
Air Pollution
Control
Measures
(APCM)
1
Boiler
(Capacit
y: 500
KG/PH)
18 Briquette
s of Bio-
Coal/
Coal
1
MT/Day
/ 0.8
MT/Day
SPM
SO2
NOx
Multi-cyclone
Separator with
Bag Filter
2
Boiler
(Capacit
y: 1
TPH)
18 Briquette
s of Bio-
Coal/
Coal
5
MT/Day
/ 4
MT/Day
SPM
SO2
NOx
Multi-cyclone
separator with
bag filter
3 Thermic
fluid
18 Briquette
s of Bio-
4
MT/Day
SPM Multi-cyclone
separator with
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heater
(Capacit
y: 1 Lakh
Kcal/ Hr)
Coal/
Coal
/ 3
MT/Day
SO2
NOx
bag filter
4
D. G. Set
(125
KVA)
11 HSD 300
Lit/Day
SPM
SO2
NOx
Adequate Stack
Height
5
D. G. Set
(125
KVA)
11 HSD 300
Lit/Day
SPM
SO2
NOx
Adequate Stack
Height
-
ii Process gas emission details 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
emissio
n
Stack/Ven
t
Height
(meter)
Air Pollution Control
Measures
(APCM)
1
Process Vent
(Chlorination)
(Product Name:
AIBN, DDH,
DCDH)
Cl2
HCl
11 Two Stage Water +
Caustic Scrubber
2
Process Vent
(Sulphonation)
(Product Name:
MMA and LABSA)
SO2 11 Two Stage Caustic
scrubber
3 Process Vent
(Ammoniation)
NH3 11 Two Stage Acid scrubber
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(Product Name:
DMH)
-
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. Adequate ventilation will be provided.
3. Regular maintenance of valves, pumps, flanges, joints and other equipment will
be done to prevent leakages and thus minimizing the fugitive emissions.
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. Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be
equipped with on-line pH meter with hooter system for better operational
control.
7. Close feeding system will be provided for centrifuges. Centrifuge and filtrate
tank vents will be connected to vent chillers.
8. Minimum number of flanges, joints and valves in pipelines.
9. Regular inspection of floating roof seals and proper preventive maintenance of
roofs and seals for tanks.
10. Fugitive emission over reactors, formulation areas, centrifuges, chemical
loading, transfer area will be collected through hoods and ducts by induced
draft and controlled by scrubber/ dust collector.
11. Dedicated scrubber will be provided are used for fugitive emissions to
control.
12. For dust emissions bag filter will be provided.
13. 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.
F Hazardous wastes
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(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.)
Categor
y &
Schedul
e as per
HW
Rules.
Quantit
y
(MT/
Annum)
Management of HW
1 Discarded
Drums/Bags
Raw
Material
and
Storage
Sch-I/
33.1
45 Collection, Storage,
Transportation and
sell to Register Re-
processors after
decontamination.
2 Used / Spent
Oil
Equipment
&
Machinery
Sch-I/
5.1
200 Lit/
Year
Collection, Storage,
Transportation and
sell to registered
recycler.
3 ETP Sludge ETP Sch-I/
35.3
216 Collection, Storage,
Transportation and
sent to common
TSDF of M/s. BEIL.
4 Distillation
Residue
Distillation Sch-I/
20.3
100.68 Collection, Storage,
Transportation and
sent for co-
processing in cement
industries or sent to
common incineration
of M/s. BEIL.
5 Spent Catalyst Process
(Product
Sch-I/
28.3
5 Collection, Storage,
Transportation and
sent to registered
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No:9,10) regenerator under
Rule-9 permission.
6 HCl (10%) Scrubber SCH-
1/26.1
263 Collection, Storage &
210 MT/Month (2520
MT/year)will be
reused within
premises in the
manufacturing of
Calcium Chloride.
7 NaOCl (12%) Scrubber SCH-
1/26.1
270 Collection, Storage &
convert to product
and than sell as main
product.
8 Sodium
Sulphite (25%)
Scrubber Sch-II/
B36
316.8
Collection, Storage,
Transportation and
sold to end user
having permission
under rule-9.
9 Spent Sulphuric
Acid (50%)
Process
(Product
No:7,8)
Sch-I/
26.3
2529
10 Ammonium
sulphate (15%)
Scrubber
Sch-II/
B15
1350
11 Ammonium
bisulphate
(50%)
Process
(Product
No:8)
Sch-I/
26.3
1350
12 Spent Solvent Process
(Product
No;17)
Sch-I/
28.6
3045
Collection, Storage,
Distillation and Reuse
within premises.
13
.
Off
Specification
Products
From mfg.
Process
(Batch
Sch-I/
28.4
20
Collection, Storage,
Transportation and
sent for co-
processing in cement
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failure) industries or Disposal
at common
incineration site.
14
.
Evaporator
Salt
Condeser SCH-
1/26.1
1080 Collection, Storage,
Transportation and
sent to common
TSDF of M/s. BEIL.
-
ii Membership details of TSDF, CHWIF etc.
(For HW management)
Unit has membership of
CETP,Dahej.
Ref. No: BEIL/ANK/2019
dated13/09/2019
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
There will be no
generation of Non-
Hazardous waste.
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered
Solvents etc. (Details in Table Format)
Only one solvent is Used in process. Other Solvent is to be used as reactant.
Solvent
Boiling
Point
(0C)
Vapor
Pressure
Inpu
t
(MT/
mon
th)
Outpu
t
(MT/m
onth)
Loss %
Recovery
%
Loss
Toluene 110.6°C
3.8 kPa
(@
25°C)
420 400 39 95.25 1.85
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.
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• Entire process will be carried out in the closed reactors with proper
maintenance of pressure and temperature.
• Close feeding system will be provided for centrifuges. Centrifuge and
filtrate tank vents will be connected to vent chillers.
• Fugitive emission over reactors, formulation areas, centrifuges, chemical
loading, transfer area, will be collected through hoods and ducts by
induced draft and controlled by scrubber/dust collector.
• Emphasis will be given to solvent management/solvent loss prevention.
• Control by having proper scrubbing system.
• Condenser to trap VOC.
• 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.
• 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.
• All the raw materials will be pneumatically transfer to the reactor.
• All rotating equipments like pumps will be installed with mechanical seals
to arrest any sort of emissions.
• 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.
H � Details regarding storage of Hazardous chemicals
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Storage details Name of major Hazardous chemicals Remarks
Storage tanks
Acetone cynohydrin, Benzoyl
Chloride,Hydrochloric Acid,Sulphuric
Acid , Methanol or Toluene
Drum/Barrel storage
Liquid Ammonia, Hydrazine Hydrate,
Hydrogen peroxide, Dibuthyl Phthalate,
Acetone,IPA, Diethylamine, 2-
Ethylhexanoic acid
Cylinder,Bottle or
Tonner
Bromine and Chlorine
� Applicability of PESO : If Applicable, company will take permission.
• During the meeting dated 19/09/2019, technical presentation made by the Project proponent.
• Committee noted that this proposal is new in GIDC Saykha. Source of Water is GIDC. Committee
noted that PP has addressed product profile considering end-use of some products in pesticides
industry and asked PP to clarify the same, PP mentioned that they will submit revised product profile
considering the same. PP mentioned that effluent generated from process, washing will be treated in
in-house ETP consisting of Primary, Secondary & Tertiary treatment followed by RO, while effluent
generated boiler blow down, cooling tower blow down will be directly treated in RO. PP mentioned that
RO – Permeate will be mixed with fresh water and reused/recycled back while RO – Reject will be fed
to Single Stage Evaporator, Condensate from Evaporator will be reused back in utility while
residue/salt will be disposed at approved TSDF.Committee noted that treatment characteristic
proposed by PP is not satisfactory. PP has proposed two Steam Boiler & one Thermic Fluid Heater.
Fuel used will be Briquette of Bio-Coal/Coal. PP has addressed Hazardous Waste as per HWR –
2016.
• After detailed discussion, it was decided to consider the proposal only after satisfactory
submission of the following documents:
1. Revised Product Profile eliminating the end-use of Products pertaining to Pesticides & Pesticides
Specific Intermediates (Address Water Balance Diagram, Consumption & Generation Details
along with Flue Gas Stack & Process Stack, Hazardous Waste Details).
2. Properly Addressing Characteristic of Waste Water Based on Treatment Technology with
Technical Justification for % Reduction of Load (pH, COD, BOD, SS).
3. Technical Justification for use of Single Stage Evaporator Instead of Multiple Effect Evaporator
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Considering the Product Profile and Characteristic of Waste Water to be generated.
8 SIA/GJ/IND2/38383/2019 M/s. Ketul Chem Pvt Ltd
Plot No. D2/CH/132, GIDC-Dahej-II,
Bharuch.
ToR –
Reconsideration
Category of the unit: 5(f)
Project status: New
• This office has received an application vide their online proposal no. SIA/GJ/IND2/38383/2019 dated
29/07/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for
preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is a new unit proposes for manufacturing of synthetic organic chemicals as tabulated as below:
SR.N
O NAME OF PRODUCTS CAS NO.
Quantity
(MT/Month) END USE
Pharma Intermediate Group-1
1 1, 1-Cyclohexane diacetic
acid monomide 99189-60-3
70
Pharma Intermediate/Gabapentin
2 1,1- Cyclohexane diacetic
acid (Di-Acid) 11/7/4355 Pharma Intermediate/Gabapentin
3 2-Cyanoacetamide 107-91-5 Pharma Intermediate/pregablin
4 Ethyl cyanoacetate 105-56-6 Pharma Intermediate/pregablin
5 Methyl cyanoacetate 105-34-0 Pharma Intermediate/pregablin
6
± 3-(Carbamoyl methyl)-5-
methyl hexanoic acid
(CMMHA)
181289-15-6 Pharma Intermediate/pregablin
7
3R-(-)-3-(Carbamoyl
methyl)-5-methyl hexanoic
acid
181289-33-8 Pharma Intermediate/pregablin
8 2-Cyano pyrazine 19847-12-2 Pharma Intermediate/pyrazinamide
9 2-Cyano pyridine 100-70-9 Pharma Intermediate/bromazepine
10 4-Cyano pyridine 100-48-1 Pharma Intermediate/bromazepine
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11 Cyanoacetic acid 372-09-8 Pharma Intermediate/pregablin
Pharma Intermediate Group-2
12 4-hydroxy Acetophenone 99-93-4
75
Pharma Intermediate/atenolol
13 4-Hydroxy phenyl
acetamide 17194-82-0 Pharma Intermediate/atenolol
14 2-(4-Hydroxyethyl)phenol 56718-71-9 Pharma Intermediate/Metoprolol
15 2-{4-(2-Methoxy ethyl)
phenoxy} methyl oxirane 56718-70-8 Pharma Intermediate/Metoprolol
16 4-(2-Methoxy ethyl Phenol)
OR MEP 501-94-0 Pharma Intermediate/Metoprolol
17 2-Chloro ethanol 107-07-3 pharma intermediate/ thiodiglycol
18 4'-Methyl-2-cyanobiphenyl 114772-53-1 pharma intermediate/ losartan
19 4'-(bromomethyl)-[1,1'-
biphenyl]-2-carbonitrile 114772-54-2 Pharma Intermediate/losartan
20
4'-methyl-2-biphenyl
carboxylic acid methyl
ester
114772-34-8 pharma intermediate/ valsartan
21 2-(Thiophen-2yl) ethanol 5402-55-1 Pharma Intermediate/clopidogrel
22 4-Hydroxy benzaldehyde 123-08-0 pharma intermediate/ Pioglitazone
23 2,4-Dichloro-5-fluoro
acetophenone 704-10-9 Pharma Intermediate/ketaconazole
24 2',4'-dichloroacetophenone 2234-16-4 Pharma Intermediate/ketaconazole
25 Ethyl ethoxy methylene
malonate 87-13-8
Pharma
Intermediate/glibenclamide
26 N-Acetyl thiazolidine-4-
caboxylic acid 5025-82-1
Pharma Intermediate/ Folcisteine
27 Methyl Isobutyryl acetate 42558-54-3 Pharma Intermediate/ atorvastatin
28 D (-) P-Hydroxyphenyl
glycine methyl ester 57591-61-4 Pharma Intermediate/amoxicillin
29 5-Methyl-2-pyrazine
carboxylic acid 5521-55-1 Pharma Intermediate/glipizide
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30 Iminostilbene carbonyl
chloride 33948-22-0
Pharma
Intermediate/carbamazepine
31 10-Methoxy Iminostilbene 4698-11.7 Pharma
Intermediate/oxcarbamezepine
32 2-Chloro-4-(4-chloro
phenoxy) acetophenone. 119851-28-4
Pharma
Intermediate/difenoconazole
33 2-Amino-4-Hydroxy
Acetophenone 90033-64-0 Pharma Intermediate/ractopamine
34 2-Bromo-4’-hydroxy
Acetophenone 2491-38-5 Pharma Intermediate/ractopamine
35 2-Chloro-4’-hydroxy
Acetophenone 6305-04-0 Pharma Intermediate/ractopamine
Bulk Drugs Group-1
36 Pregabalin 148553-50-8
30
api/anti covulsant
37 Albendazole 54965-21-8 api/anti worm
38 Atenolol 29122-68-7 api/beta bocker
39 Atorvastatin Calcium 134523-00-5 api/cardiovascular
40 Carbamazepine 298-46-4 api/anti epileptic
41 Gabapentin 60142-96-3 api/anti covulsant
42 Ketoconazole 65277-42-1 api/anti fungal
43 Losartan potassium 124750-99-8 api/hypertension
44 Metoprolol Succinate 98418-47-4 api/hypertension
45 Metoprolol Tartrate 37350-58-6 api/hypertension
46 Oxcabazepine 28721-07-5 api/anti epileptic
47 Pantaprazol Sodium 138786-67-1 api/anti ulcer
48 Ractopamine hydrochloride 90274-24-1 api/beta agonist
49 Ritonavir 155213-67-5 api/antiretroviral
50 Rivaroxaban 366789-02-8 api/anticoagulant
51 Salmeterol xinafoate 94749-08-3 api/anti asthamatic
52 Saxagliptin Monohydrate 945667-22-1 api/anti diabetic
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53 Soterenol 13642-52-9 api/anti asthamatic
54 Sitagliptin 486460-32-6 api/anti diabetic
55 Valsartan 137862-53-4 api/hypertension
56 Glipizide 29094-61-9 api/anti diabetic
57 Rosuvastatin Calcium 147098-20-2 api/cardiovascular
58 Sofosbuvir 1190307-88-
0 api/anti viral
59 Telmisartan 144701-48-4 api/hypertension
60 Mirtazapine 61337-67-5 api/anti histamine
61 Nevirapine 129618-40-2 api/HIV/AIDS curing
62 Octopamine 104-14-3 api/veternary
63 Tranexamic acid IP 1197-18-8 api/antifibrinolytics
Specialty Chemicals
64 p-Chloro phenol 106-48-9
120
Raw material for
4,2(Methoxyethyl)phenol
65 o-Chloro phenol 95-57-8 Raw material for 2-
Chlorobenzaldehyde
66 2,6-Dichloro toluene 118-69-4 Raw material for 2 methyl 3
biphenyl methanol
67 Hydrazine hydrate 10217-52-4 Raw material for 1,2,4-Triazole
68 1,2,4-Triazole 288-88-0 Raw material for 1-Methyl-1,2,4-
Triazole
69 3-Cyano pyridine 100-54-9 Raw material for nictonic
acid/nictonamide
70 Phenyl Ethyl Alcohol (PEA) 60-12-8 Raw material for Phenyl Methyl
Alcohol
71 Phenyl ethyl methyl ether
(PEME) 3558-60-9
Raw material for Phenyl ethyl
methyl ether
72 Triclosan 3380 -34-5 Raw material for Irgasan
73 2–Amino–4, 4’ – Dichloro
Diphenyl Ether 121-27-7 Raw material for Yellow acid
74 2–Hydroxy–4, 4’–Dichloro 3380-44-7 Raw material for Tinosan
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Diphenyl Ether
75 Decabromo diphenyl oxide 1163-19-5 Raw material for Saytex
76 Alpha phenyl ethyl amine dl 618-36-0 Raw material for R+ 1
phenylethylamine
77 (R)-(+)-1-Phenylethylamine 3886-69-9 Raw material for R- carbommoyl
methyl 5 methyl hexanoic acid
78 (S)-(-)-1-Phenylethylamine 2627-86-3 Raw material for (S)-3-Cyano-5-
methylhexanoic acid
79 L-(+)-Mendelic acid 17199-29-0 Raw material for Dulexotine
Hydrochloride
80 Malononitrile 109-77-3 Rawmaterial for 2
chlorobenzaldehyde malononitrile
81 2,4-Difluoro aniline 367-25-9 Raw material for 2,4-difluoro-5-
chloronitrobenzene
82 2,2-Dibromo-2-
Cyanoacetamide 10222-01-2 Raw material for Bioban (dbnpa)
83 2-(4-tert-butyl)phenyl)
ethanol 5406-86-0
Raw material for 2-Benzoxazol-2-
yl-1-(4-tert-butylphenyl)ethanol
Total 295
• 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 19/09/2019.
• Technical presentation was made by the project proponent with consultant/expert Aqua Air
Environmental Engineers Pvt. Ltd during SEAC meeting dated 13/08/2019.
• Committee noted that this proposal is for new unit located at GIDC Dahej-II.
• Committee deliberated on size of group products in product profile and end use of each group
products are not adequate and hence committee insisted to PP for submit adequate revised product
profile proposal. Committee asked about compliance of Ozone Depleting Substances Rules for
proposed Page 82 of 82 539thmeeting of SEAC-Gujarat, Dated 13.08.2019 Page 82 of 82 product
namely 1,1,1,2-Tetrafluoroehtane etc. Committee asked for clarification regarding 2,4-Difluoro aniline ,
2,6-Dichloro toluene, 2,-3-Dichloro pyridine etc as pesticide inter mediate, PP could not explain
regarding it. Committee asked about waste water management, PP informed low COD effluent after
ETP treatment will be sent to CETP and high COD effluent after primary treatment will be sent to
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common MEE of M/s SEPPL, Dahej. Committee asked about readdressed worst case scenario as per
revised product profile for water consumption and waste water management.
• After deliberation, SEAC unanimously decided to defer the project and consider the proposal
after submission of the following details.
1. Revised product profile with respect to production capacity, size of group products and its end use
in agro chemicals.
2. Readdressed water consumption and waste water generation considering worst case scenario for
revised product profile.
3. Technical justification for compliance of ODS (Ozone Depleting Substances) Rules 2000 and its
amendments time to time for proposed product 1,1,1,2-Tetrafluoroehtane etc.
• Project proponent presented for the following points in SEAC meeting dated 19/09/2019 for the above
mentioned points.
• PP has replied as below:
1. PP presented revised product profile eliminating the production capacity, size of group products
and also eliminating the products pertaining to agro chemicals.
2. PP presented water consumption and waste water generation considering worst case scenario for
revised product profile.
3. PP mentioned that they have eliminated the products pertaining to ODS (Ozone Depleting
Substance) Rules, 2000.
• The case was reconsidered in the SEAC meeting dated 19/09/2019. During the said
meetingCommittee observed that reply submitted by PP is satisfactory.
• Salient features of the project including Water, Air and Hazardous waste management (Revised):
Sr.
no.
Particulars Details
A
A Total cost of Proposed Project
(Rs. in Crores):
22.0 Crores
B Total Plot area ( sq. meter) 13,923 Sq. m.
Green belt area ( sq. meter) 4,177 Sq. m.
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C Employment generation 150
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. GIDC/DEE(WS)/BRH/235
ii Water consumption (KLD)
Category
Quantity
KLD
Remarks
(G) Domestic 10.0
(H) Gardening 2.0
(I) Industrial
Process 136.4
Washing 20.0
Boiler 40.0
Cooling 10.0
Scrubber 4.0
Industrial Total 210.4
Total (A + B + C) 222.4
10) Total water requirement for the project:222.4 KLD
11) Quantity to be recycled: 9.6 KLD
12) Total fresh water requirement: 212.8 KLD
iii Waste water generation (KLD)
Category Waste Remarks
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water
KLD
(E) Domestic 8.0
(F) Industrial
Process 114.2 Low COD & TDS: 103.8 KLD (ETP-1)
High COD & TDS: 10.4 KLD (ETP-2)
Washing 20.0 Low COD & TDS: 20.0 KLD (ETP-1)
Boiler 10.0 RO: 12 KLD, RO Reject of 2.4 KLD will
be treated with ETP-1. Cooling 2.0
Scrubber 5.33 Reuse and sell under rule-9
permission
Total Industrial waste
water
151.5
Total [A + B] 159.5
-
iv Treatment facility within premises with capacity
[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP
etc.
� ETP-1 (Primary, Secondary, Tertiary) : 126.2 KLD
� ETP-2 (Primary) : 10.4 KLD
� ETP-3 (RO) : 12.0 KLD
Treatment scheme including segregation at source.
� Stream I (Low COD & TDS Stream) (123.8 KLD + 2.4 RO Reject)
� First all non-toxic and biodegradable streams (low & medium COD & TDS)
of wastewater shall pass through oil & grease removal tank (ogrt-01) where
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floating o & g shall be removed manual from top and collected in o & g
collection tank (ogct-01). Then effluent shall be collected in collection cum
equalization tanks-01 (cets-01). Pipe grid is provided at bottom of the cets-
01 to keep all suspended solids in suspension and to provide proper mixing.
2 nos. Of air blowers (1w+1 stand-by) shall supply air through to pipe grid.
� Then after, equalized wastewater shall be pumped to neutralization tank-1
(nt-01-b) where the continuous addition and stirring of lime solution is done
to maintain neutral ph of wastewater from lime dosing tanks (ldt-01-a/b) as
per requirement with help of lime dosing pumps. Then after, neutralized
wastewater shall go to flash mixer (fm-01) by gravity. Alum shall be dosed
from alum dosing tanks (adt-01-a/b) with help of dosing pumps. Then
coagulated effluent shall be collected in flocculator (fl-01) where
polyelectrolyte shall be dosed from polyelectrolyte dosing tank-1 (pedt-01)
with help of pumps to carry out flocculation with help of flocculator
mechanism. Then after, coagulated wastewater shall be settled in primary
clarifier-1 (pcl-01).
� Clear supernatant from pcl-01 shall be passed in aeration tank-1 (at-01).
Here, condensate from MEE and ATFT through condensate storage tank
(cst-01) mix with effluent. Here, biodegradation of organic matter of the
wastewater shall be carried out by bacteria (suspended growth) in the at-01
and for that oxygen shall be supplied by 2 nos. of air blowers (b-02) through
diffusers. Air blowers also keep MLSS in suspension.
� Then after, wastewater shall go to secondary clarifier-1 (scl-01). Here, the
suspended solids shall be settled. Sludge shall be removed from bottom of
scl-01 and pumped to at-1 to maintain MLSS and excess activated sludge
shall be sent to sludge sump (ss-01).
� Clear supernatant from scl-01 shall go to aeration tank-2 (at-02). Here
biodegradation of left out organic matter of the wastewater shall be carried
out by bacteria (suspended growth) and for that oxygen shall be supplied by
two nos. Of blowers (b-03) with help of diffusers. Then after, wastewater
shall go to secondary clarifier-2 (scl-02) from at-2. Here, the suspended
solids shall be settled. Activated sludge shall be removed from bottom of scl-
02 and pumped to at-02 to maintain MLSS and remaining will be sent to ss.
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Nutrients will be added from nutrient dosing tanks (ndts-01) to aeration tank-
1 & 2 for growth of bacteria. Clear shall be collected in intermediate sump
(is-01) by gravity.
� Thereafter, the wastewater shall be passed through multi grade filter (mgf-
01) to remove left out TSS and activated carbon filter (acf-01) for final
effluent polishing. After tertiary treatment, effluent shall be collected in
treated effluent sump-01 (tes-01) before sent to CETP Dahej for further
treatment.
� Sludge settled in pcl-01, pcl-02 and excess sludge from scl-01-b/02-b shall
be collected in sludge sumps (sss-01-a/b) then sludge shall be pumped to
centrifuge (cf-01) where poly shall be mixed from poly dosing tank-2 (pdt-02)
with sludge to increase efficiency of centrifuge sludge dewatering. Then,
dewatered sludge shall be stored in in HWSA and then ultimate disposal to
TSDF. Leachate from cfs-01 and backwash from mgf-01 and acf-01 shall be
collected in drain pit and pumped back to cet-01-a/b for further treatment.
� Stream II (High TDS stream) (10.4 KLD Process)
� All high TDS streams of wastewater shall be collected in equalization cum
neutralization tank-01 (ent-01). Here caustic shall be added from ldt-01 by
gravity. Mixer is provided at bottom of the ent-01 to keep all suspended
solids in suspension and for proper mixing.
� Then, neutralized wastewater shall be pump to flash mixer-02 (fm-02) where
alum and polyelectrolyte shall be dosed from alum dosing tank (adt-01) and
polyelectrolyte dosing tank (pedt-01) respectively by gravity. Then it will go
into pst-01 where solids are allowed to settle and clear supernatant from pst-
01 shall be collected in treated effluent sump (tes-01) before sent to
common MEE M/s. BEIL for further treatment.
� Stream-III (12 KL)
� All utilities streams of wastewater shall be passed through duel media filter
(dmf-01) to remove left out TSS. After treatment, effluent shall be collected
in RO feed tank (roft-01) before sent to RO-01 for further treatment. RO-01
permeate water shall be collected in RO permeate tank (ropt-01) before
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reuse in process & RO-01 reject shall be sent to ETP for further treatment.
Note: (In case of CETP discharge) :
Management of waste water keeping in view direction under section 18 (1)
(b) of the Water (Prevention and Control of Pollution) act, 1974 issued by
CPCB regarding compliance of CETP.
� Unit has proposed ETP to achieve CETP norms, and then after unit will
discharge the effluent to CETP, Dahej through Pipeline.
Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):
� Low COD & TDS effluent will be discharge into CETP, Dahej after treated
in Primary, Secondary and tertiary treatment. High COD & TDS effluent
will be treated in primary treatment and then sent to CMEE of BEIL, Dahej
and waste water from Cooling and boiler will be treated in RO and reuse
within premises.
v Mode of Disposal & Final meeting point
Domestic: Septic tank/Soak Pit System
Industrial: Low COD & TDS: Effluent will be treated in Primary, Secondary and
tertiary treatment, after that sent to CETP, Dahej.
High COD & TDS: Effluent will be treated in in primary treatment
and then sent to CMEE of BEIL, Dahej.
Waste water from Cooling and boiler will be treated in RO and reuse
within premises.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE
etc. Name of CF
� CETP, Dahej, CMEE of BEIL,Dahej
Membership of Common facility (CF)
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(For waste water treatment)
GIDC/BRH/DEE (DRG)/362
vii Simplified water balance diagram with reuse / recycle of waste water
viii Reuse/Recycle details (KLD)
Total reuse: 9.6 KLD
Source of waste
water for reuse
with quantity in
KLD (From
where it is
coming)
Application
area with
quantity in
KLD (Where it
is used)
Characteristics of
waste water to be
reused (COD, BOD,
TDS etc.)
Remark
s
regardin
g
feasibilit
y to
reuse
i.e.
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RO Permeate: 9.6
KLD
Boiler: 9.6 KLD COD: 120 mg/l
BOD: 30 mg/l
TDS: 300 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.
-
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 (4
TPH) 30 Coal 4
SPM <
150
mg/Nm3
SO2 < 100
ppm
NOx < 50
ppm
Multi
Cyclone
Separator
with Bag
Filter &
Water
Scrubber
4
D. G Set
(750
KVA)
11 HSD 2
SPM <
150
mg/Nm3
SO2 < 100
ppm
NOx < 50
ppm
Adequate
stack
Height
-
ii Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx
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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
(Ketoconazole) HCl 11
Two stage
Water
scrubber
2 Process Vent
(Valsartan) SO2 11
Two stage
Alkali
scrubber
3 Process Vent
(Ketoconazole) HBr 11
Two stage
Water
scrubber
4
Process Vent
(4-Hydroxy Phenyl
Acetamide)
NH3 11
Two stage
Water
scrubber
-
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. Adequate ventilation will be provided.
3. Regular maintenance of valves, pumps, flanges, joints and other
equipment will be done to prevent leakages and thus minimizing the
fugitive emissions.
4. Entire process will be carried out in the closed reactors with proper
maintenance of pressure and temperature.
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5. Periodic monitoring of work area will be carried out to check the fugitive
emission.
6. Stand by pumps will be provided on all scrubbers. Besides, scrubbers
will be equipped with on-line pH meter with hooter system for better
operational control.
7. Close feeding system will be provided for centrifuges. Centrifuge and
filtrate tank vents will be connected to vent chillers.
8. Minimum number of flanges, joints and valves in pipelines.
9. Regular inspection of floating roof seals and proper preventive
maintenance of roofs and seals for tanks.
10. Fugitive emission over reactors, formulation areas, centrifuges, chemical
loading, transfer area will be collected through hoods and ducts by
induced draft and controlled by scrubber/ dust collector.
11. Dedicated scrubber will be provided are used for fugitive emissions to
control.
12. For dust emissions bag filter will be provided.
13. 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.
F Hazardous wastes
(as per the Hazardous and Other Wastes (Management and Transboundary
Movement) Rules 2016.
i Sr.
No
.
Type Of Waste Source Of Generation Category Quantity
(MT/Annu
m)
Mode Of
Treatment
And Disposal
1 Spent carbon ± 3-(Carbamoyl
methyl)-5-methyl
hexanoic acid
(CMMHA),
4-Hydroxy phenyl
acetamide, Triclosan,
Schedule
-(I)-(28.3)
504 Collection,
Storage,
Transportation
and sent for
co-processing
in cement
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Sitagliptin, Nevirapine industries or
sent to
Incineration
site of M/s.
SEPPL.
2 Sulphuric Acid
(50-65%)
1,1- Cyclohexane
diacetic acid (Di-Acid),
2–Hydroxy–4, 4’–
Dichloro Diphenyl
Ether, Triclosan,
Schedule
-(I)-(28.1)
13,629 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
3 HCl (30%) 4-hydroxy
Acetophenone,
2,6-Dichloro toluene,
Saxagliptin
Monohydrate
& Scrubber
Schedule
-(I)-(28.1)
1,402 Collection,
Storage and
Reuse in 3R-(-
)-3-(Carbamoyl
methyl)-5-
methyl
hexanoic acid
(Reqd Qty.
5712
MT/Annum)
4 Dil. Formic Acid 1,2,4-Triazole Schedule
-(I)-(28.1)
2,706 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
5 NaCl Salt Cyanoacetic acid, 2–
Amino–4, 4’ –
Schedule
-(I)-(28.1)
1,872 Collection,
Storage,
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Dichloro Diphenyl
Ether, Malononitrile,
Pregabalin
Transportation
and sell to end
users Having
Rule-9
permission.
6 Discarded
Drums/Bags/Lin
ers
Raw Material and
Storage
Schedule
-(I)-(33.1)
1,500 Nos. Collection,
Storage,
Decontaminati
on, Reuse,
Transportation
and sale to
authorized
vendor.
7 Spent Catalyst 4-(2-Methoxy ethyl
Phenol) OR MEP,
Phenyl Ethyl Alcohol
(PEA), Ritonavir
Schedule
-(I)-(28.2)
72 Collection,
Storage,
Transportation
and Sell to
Regenerator
Having Rule-9
permission.
8 Organic Waste Saxagliptin
Monohydrate,
Rosuvastatin Calcium
Schedule
-(I)-(28.1)
1,020 Collection,
Storage,
Transportation
and sent for
co-processing
in cement
industries or
sent to
common
incineration
site of M/s.
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SEPPL.
9 Iron Sludge 2–Amino–4, 4’ –
Dichloro Diphenyl
Ether
Schedule
-(I)-(28.1)
756 Collection,
Storage,
Transportation
and Disposal to
co-processing
in cement
industries or
sent to TSDF
site.
10 Inorganic Waste 2',4'-
dichloroacetophenon
e, Soterenol,
Triclosan,
Octopamine
Schedule
-(I)-(28.1)
3,372 Collection,
Storage,
Transportation
and Disposal to
co-processing
in cement
industries or
sent to TSDF
site.
11 Spent Solvent Manufacturing
Process
Schedule
-(I)-(28.6)
31,500 Collection,
Storage and
reuse within
premises after
distillation.
12 Distillation
Residue
Distillation plant Schedule
-(I)-(20.3)
948 Collection,
Storage,
Transportation
and sent for
co-processing
in cement
industries or
sent to
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common
incineration
siteof M/s.
SEPPL.
13 Off Specification
Products
Failure of Batch Schedule
-(I)-(28.4)
24 Collection,
Storage,
Transportation
and sent for
co-processing
in cement
industries or
sent to
common
incineration
siteof M/s.
SEPPL.
14 Used Oil From Moving
Machineries
Schedule
-(I)-(5.1)
12 Collection,
Storage,
Transportation,
Reuse and
sale to
authorized
recycles.
15 Sodium Acetate
(25%)
Atorvastatin Calcium Schedule
-(I)-(28.1)
18 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
16 Sodium Sulphate
(95%)
Ritonavir Schedule
-(I)-(28.1)
45 Collection,
Storage,
Transportation
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and Sell to end
users Having
Rule-9
permission.
17 Sodium Bromide
(95%)
2,2-Dibromo-2-
Cyanoacetamide,
Telmisartan
Schedule
-(I)-(28.1)
144 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
18 Sodium Bisulfite
(30-40%)
Triclosan Schedule
-(I)-(28.1)
726 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
19 KCl (50%) Sofosbuvir Schedule
-(I)-(28.1)
492 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
20 Ammonium
Chloride (10-
15%)
Sofosbuvir Schedule
-(I)-(28.1)
15 Collection,
Storage and
Reuse in
Sofosbuvir
(Reqd Qty.
14.4
MT/Annum)
excess qty will
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be sold to end
users having
rule-9
permission.
21 Magnesium
Sulphate Salt
1,2,4-Triazole &
Scrubber
Schedule
-(I)-(28.1)
144 Collection,
Storage and
Reuse in
Sofosbuvir
(Reqd Qty.
144
MT/Annum)
22 Liq. Ammonia
(20-25%)
1,2,4-Triazole &
Scrubber
Schedule
-(I)-(28.1)
1,836 Collection,
Storage and
Reuse in
Hydrazine
Hydrate (Reqd
Qty. 3000
MT/Annum)
23 Potassium
Acetate (50%)
Telmisartan Schedule
-(I)-(28.1)
72 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
24 HBr (30-35%) 2-Amino-5-nitro
thiazole
Schedule
-(I)-(28.1)
84 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
25 Sodium Sulphite Scrubber Schedule 504 Collection,
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(28%) -(II)-B36 Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
26 Dil. Hydrogen
Bromide (25%)
Scrubber Schedule
-(II)-B36
480 Collection,
Storage,
Transportation
and Sell to end
users Having
Rule-9
permission.
27 ETP Sludge ETP Treatment Schedule
-(I)-(35.3)
1,680 Collection,
Storage,
Transportation
and Disposal to
co-processing
in cement
industries or
sent to TSDF
site of M/s.
SEPPL.
ii Membership details of TSDF, CHWIF etc.
(For HW management)
Proponent has applied for
membership
iii Details of Non-Hazardous waste & its disposal
(MSW and others)
There will be no
generation of Non-
Hazardous waste.
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered
Solvents etc. (Details in Table Format)
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Solvent
Boiling
Point
(0C)
Vapor
Pressur
e
Input
(MT)
Output
(MT) Loss
%
Recovery
%
Loss
EDC 83.47
100 mm
Hg @
300C
513 492 21 95.91 4.09
MDC 39.6
400 mm
Hg @
24.10C
389 379 10 97.43 2.57
Toluene 111
22 mm
Hg @
200C
654 629 25 96.18 3.82
Methanol 64.7
96 mm
Hg @
200C
803 765 38 95.27 4.73
Phenol 181.7
0.4 mm
Hg @
200C
615 597 18 97.07 2.93
IPA 82.2
82.2 mm
Hg @
200C
356 346 10 97.19 2.81
Xylene 139.3
8.3 mm
Hg @
200C
543 528 15 97.24 2.76
Ethyl
Acetate 96.5
10 mm
Hg @
200C
750 732 18 97.60 2.40
Acetone 76.4
11.1 mm
Hg @
200C
687 663 24 96.51 3.49
DMF 153 3.7 mm 369 353 16 95.66 4.34
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Hg @
250C
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.
• Close feeding system will be provided for centrifuges. Centrifuge and filtrate
tank vents will be connected to vent chillers.
• Fugitive emission over reactors, formulation areas, centrifuges, chemical
loading, transfer area, will be collected through hoods and ducts by induced
draft and controlled by scrubber/dust collector.
• Emphasis will be given to solvent management/solvent loss prevention.
• Control by having proper scrubbing system.
• Condenser to trap VOC.
• 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.
• 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.
• All the raw materials will be pneumatically transfer to the reactor.
• All rotating equipments like pumps will be installed with mechanical seals to
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arrest any sort of emissions.
• 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.
H � Details regarding storage of Hazardous chemicals
Storage details Name of major
Hazardous chemicals
Remarks
Storage tanks
HCl, H2SO4, Methanol,
Toluene, Ethylene Oxide,
Chloroform, Liq. Ammonia
Drum/Barrel storage Ammonium Chloride,
Chloro Acetyl Chloride,
Phenol, Methyl
Cynoacetate,
Cylinder Chlorine, Hydrogen,
Nitrogen
� Applicability of PESO : Yes Applicable
• After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant
of Terms of Reference.
• 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
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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. Explore the use of renewable energy to the maximum extent possible. Details of provisions
to make the project energy-efficient through 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.
3. 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.
4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard
during unloading, storage, transportation, handling and processing of Solvents.
5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form.
• 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.
• Further Project Proponent may be advised to submit final EIA Report with EC application within 100
days from the date of issuance of this ToR to expedite processing of Environment Clearance
application.
• The project proponent shall have to apply for Environmental clearance through online portal
http://environmentclearance.nic.in/ along with final EIA report.
9 SIA/GJ/IND2/37751/2019 M/s. Valencia Life Sciences
Plot No.1108 ,GIDC. Bamanbore ,
Chotila, Dist.: Surendranager.
ToR –
Reconsideration
Category of the unit: 5(f)
Project status: New
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• This office has received an application vide their online proposal no. SIA/GJ/IND2/37751/2019 dated
14/06/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for
preparation of EIA/EMP report.
• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.
• This is a new unit proposes for manufacturing of synthetic organic chemicals as tabulated as below:
Sr
No
Name of Product Production
MT/M
CAS No End use of Product
1 1,3-Dichloroacetone 10 534-07-6 Famotidine &Nizatidine
2 2-Amino-5-Methyl
Thiazole
5 7305-71-7 Meloxicam & Piroxicam
3 4-Bromomethyl-2-
cyanobiphenyl
10 114772-54-2 Irbesartan, Losartan,
Valsartan, Azilsartan &
Telmisartan
4 4-Hydroxy, 2-Methyl-
2H, 1,2-Benzothiazine
Carboxylic Acid
Isopropyl Ester, 1,1-
Dioxide
5 118854-48-1 Meloxicam & Piroxicam
5 4-Hydroxy, 2-Methyl-
2H, 1,2-Benzothiazine
3-Carboxylic Acid
Methyl Ester, 1,1-
Dioxide
5 35511-15-0 Meloxicam & Piroxicam
6 Benzocaine 10 94-09-7 Local anaesthetic
7 Cetylpyridinium
Chloride
5 3473-63-0 Cetrimide
8 Cis Bromo Benzoate 13 61397-56-6 Ketoconazole
9 Cis Tosylate 10 154003-23-3 Ketoconazole & Itraconazole
10 Febuxostat 2 144060-53-7 Xanthine Oxidase Inhibitor
11 Fexofenadine
Hydrochloride
1 83799-24-0 Antihistamine
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12 Fluconazole 5 86386-73-4 Antifungals
13 Lidocaine Hydrochloride 10 137-58-6 Local anaesthetic; Class I
antiarrhythmic
14 Lidocaine 5 6108-05-0 Local anaesthetic; Class I
antiarrhythmic
15 Meta Bromo Anisole 10 2398-37-0 Tramadol HCl
16 Meta Bromo Nitro
Benzene
13 585-79-5 Meta Bromo Anisole
17 Meta Chloro Anisole 5 2845-89-8 Tramadol HCl
18 n-Butyl Bromide 10 106‐65‐9 Alkylating agent
19 Tetra Butyl Ammonium
Bromide
10 1643-19-2 Phase transfer catalyst
20 Tri Ethyl Benzyl
Ammonium Bromide
5 554-68-7 Phase transfer catalyst
21 Pregabalin 2 148553-50-8 Anticonvulsant
Total Production 151
By-Product
1 Basic Chromium
Sulphate
64.609 39380-78-4
Lather industry
• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.
• PP was called for presentation in the SEAC meeting dated 19/09/2019.
• Technical presentation was made by the project proponent with consultant/expert T R Associates
during SEAC meeting dated 24/07/2019.
• Committee noted that this proposal is for new unit located at GIDC.
• Committee deliberated on location of the proposed project, product profile, waste water & Hazardous
waste management etc.
• While discussing regarding waste water management, PP informed that they will maintain zero liquid
discharge (ZLD). However, consultant as well as PP could not satisfactorily reply about treatability and
adequacy of ZLD.
• After deliberation, SEAC unanimously decided to consider the proposal after submission of
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the following details.
1. Technical justification for Basic Chromium Sulphate as By-Product.
2. Treatability and adequacy of ZLD considering worst case scenario based on mass balance.
• Project proponent presented for the following points in SEAC meeting dated 19/09/2019 for the above
mentioned points.
• PP has replied as below:
1. PP presented technical justification for basic chromium sulphate and addressed the same in
hazardous waste as per hazardous waste rule.
2. PP presented treatability and adequacy of ZLD considering worst case scenario based on mass
balance.
• The case was reconsidered in the SEAC meeting dated 19/09/2019. During the said
meetingCommittee observed that reply submitted by PP is satisfactory.
• Salient features of the project including Water, Air and Hazardous waste management (Revised):
Sr.
no.
Particulars Details
A Total cost of Proposed Project (Rs. in Crores) 2.50 Cr
B Total Plot area ( sq. meter) Plot Area :4617Sq.m
Green belt area,/Tree Plantation area ( sq. meter) 1391 Sq.m within premise.
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. Not applicable.
ii Water consumption (KLD)
Sr No Description Water Consumption KL/Day
A Domestic 1.5
B Industrial
a. Process (including Scrubber) 17.528
B DM plant( for backwash) 4.382
b. Boiler 1.50
c. Cooling 2.00
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d. Washing 2.00
Total B 27.410
C Gardening 3.00
Total (A+B+C) 31.91
D RO permeate 23.95
Ultimate fresh water required(C-
D) 7.76
Source of fresh Water : GIDC water Supply
Quantity to be recycle : 23.95 KL/Day(RO permeate)
Total Fresh water requirement : 31.91KL/Day -23.95 KL/Day= 7.76 KL/Day
iii Waste water generation (KLD)
CATEGORY WISE WASTEWATERGENERATION
Description Waste Water
Generation KL/Day
Mode of Disposal
A Domestic 1.30 Soak Pit
B Industrial
a. Process 22.703 MEE
B DM plant( from backwash) 4.382 ETP & RO
b. Boiler 0.200 ETP & RO
c. Cooling 0.250 ETP & RO
d. Washing 2.000 ETP & RO
Total (B) 29.535
C RO permeate reuse in process,
Washing, and Cooling
23.95 Reuse
Domestic waste water will be disposed in to Soak Pit. Treated waste water will be evaporated in
MEE to maintain Zero Discharge.
iv Treatment facility within premises with capacity
In-house ETP (Primary, Secondary,RO Plant, MEE).
• Domestic waste water will be discharged in to soak pit.
• Industrial wastewater will be segregated in two stream i.e dilute stream and
concentrated stream which will be collect separately in collection cum neutralization
tank.
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• Concentrated stream will be passed through VOC stripper to remove VOC content from
w.w, Generated stream from VOC stripper will be evaporated in MEE. Generated
Condensate equalised with dilute stream. After pH correction, wastewater will be given
polyelectrolyte treatment. Then wastewater will be collet in settling tank. Bottom Sludge
will be collected will be stored in bags and ultimately disposed of at TSDF site. Treated
waste water from settling tank and will be treat in aeration tank and then clarifier. Then
after , it will be passed through RO. Permeate of RO will be reuse in washing activity.
RO Reject water will be send to MEE .Evaporation residue from evaporator will be send
to ETP sludge. Condensate of MEE will be send to ETP for treatment. Thus, unit will
maintain Zero Effluent Discharge.
Treatment plant units
ETP unit Cap Nos
Collection cum neutralization Tank for dilute
Stream
5 KL 1
VOC stripper - 1
Filter Nutch 1
Collection tank for concentrated stream 30 KL 2
Equalization tank 30 KL 2
Coagulation Tank 10 KL 1
Sedimentation Tank 20 KL 1
Aeration Tank 45 KL 1
Clarifier 30KL 1
RO Plant 3.00 KL/Hr 1
MEE 3.00 KL/Hr 1
VOC Stripper 1
Treatment Scheme including segregation at source
• Domestic waste water will be disposed in to Soak Pit.
• Generated industrial waste water will be treat in P+S treatment plant and pass through
RO. Permeate of RO will be reuse in process. RO reject will be evaporated in MEE
within premises.
Note (in case of CETP discharge )
Management of waste water keeping in view direction under section 18 (1) (b) of the Water
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(Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.
Not applicable as there is no CETP in Bamanbore industrial estate. Unit will maintain Zero
Discharge.
v Mode of Disposal & Final meeting point
Domestic: Go to soak pit via septic tank
Industrial:
Treated waste water will be evaporated in MEE within premises to maintain
Zero Discharge.
vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , Name
of CF : Not applicable as unit will maintain Zero Discharge
Membership of Common facility (CF).
(For waste water Treatment )
Unit will maintain Zero Discharge
vii Simplified water balance diagram with reuse/Recycle details (KLD)
Water Consumption: Industry will need 31.91 KL/Day (Domestic: 1.5 KL/Day, Industrial: 27.410
KL/Day and Gardening 3.00 KL/Day) water for the proposed production which will be met by
water supply from GIDC Service.
Waste Water Generation: Domestic waste water (1.30 KL/Day) will be discharged in to soak pit.
21.910
4.382
17.528 0.2 0.25 2
Soak Pit (1.3)
6.832
Attach to Recovery System 22.703
Loss 21.95 4.835
4.78 23.95
Permeate Reuse
0.7 T MEE Sludge to TSDF
Water Balance Diagram
Domestic (1.5) RO Followed by
DM Plant Boiler(1.5) Cooling (2) Washing(2)
Gardaning
(3)
Process(17.528)
P+S+T (28.790)
RO Plant
MEE (22.603+4.835=
27.438)
VOC sripper
First Day : Fresh Water(31.910)
From Second Day : 31.910-23.95=7.96 KL/Day
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The industrial waste water generation will be 29.535 KL/Day (Process-22.703 +Reject Water
4.382 + 0.005+Cooling blow down-0.250 + boiler blow down-0.200 +washing-2.00).
Mode of Disposal : Treatment and evaporation ( i.e ZLD)
viii Reuse/Recycle details (KLD) Source of reuse & application:
Source of waste
water for reuse with
quantity in KLD
(From where it is
coming)
Application
area with
quantity in
KLD
(Where it is
used)
Characteristics of
waste water to be
reused (COD, BOD,
TDS etc.)
Remarks
regarding
feasibility to reuse
i.e.
RO permeate Process pH : 6.5-7.5
TSS <120 mg/Lit
TDS<300 mg/Lit
COD <150 mg/Lit
RO permeate
suitable for use in
process and
washing activity
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.N
O.
STACK
ATTAC
HED TO
STAC
K
HEIGH
T (M)
FUEL
REQUIRE
MENT
Quantit
y of
Fuel
MT/Day
EXPECTED
POLLUTAN
T
APC
SYSTEM
1
Steam
Boiler
(1 TPH)
30
White
Coal
/Briquette
600
Kg/Day SPM ≤150
mg/Nm3
SO2 ≤100
ppm
NOX ≤ 50
ppm
Dust
collector
followed by
Bag Filter
2 D.G. set
(65 HP) 6.5 Diesel
40 L/Hr Inbuilt
Acoustic
enclosure
ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)
SR. STACK STACK APC EXPECTED CONCENTRA
Gardening
(2)
Gardening
(2)
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NO ATTACHED TO HEIGHT
(M)
SYSTEM POLLUTANT TION
1
Reactor of CIS
Bromo Benzoate,
Meta Bromo Nitro
Benzene
12
Two stage
alkali
scrubber
Bromine <2 mg/NM3
2 Reactor of
Pregabaline 12
Water
scrubber Ammonia <150 mg/NM3
3
Reactor of
Fexofenadine
Hydrochloride
and Fluconazole
12 Water
Scrubber
Hydro Chloric
Acid <20 mg/NM3
4 Solvent Recovery
system 12
Activated
Carbon
column
VOC BDL
iii Fugitive emission details with its mitigation measures.
As below:
Sources of fugitive emissions include storage of chemicals, loading and unloading
section, raw material handling, hazardous waste storage area.
Mitigation Measures
Water shall be sprinkled during the construction
- Mechanical seals for pumps etc. should be used and maintained.
- Closed unloading, conveying and packing system
- All the reactors shall be closed.
- Safety devices shall be provided to workers
- Raw material storage in closed storage area.
F Hazardous waste
(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules
2016.
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i
Sr
No
Name of
Hazardous
Waste
Categ
ory
T/Year Source Mode of disposal
1
Aluminum
Chloride
C2 of
Sch-II
60.5
T/Year
Manufacturing process
of Fexofenadine
Hydrochloride and
Fluconazole
Collection ,Storage
,transportation and
Partially (15.06
T/Year reuse)
remaining will be sold
out of actual end
users
2
Distillation
Residue 28.1
261.24
T/Year
Manufacturing process
of
• 2-Amino-5-Methyl
Thiazole
• 4-Bromomethyl-2-
cyanobiphenyl
• 4-Hydroxy, 2-
Methyl-2H, 1,2-
Benzothiazine
Carboxylic Acid
Isopropyl Ester,
1,1-Dioxide
• 4-Hydroxy, 2-
Methyl-2H, 1,2-
Benzothiazine 3
Carboxylic Acid
Methyl Ester, 1,1-
Dioxide
• Benzocaine
• Cetylpyridinium
Chloride
• Cis Bromo
Collection ,Storage
,transportation and
send to CHWIF for
incineration
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Benzoate
• Cis Tosylate
• Febuxostat
• Fexofenadine
Hydrochloride
• Fluconazole
• Lidocaine
Hydrochloride
• Lidocaine
• Meta Bromo
Anisole
• Meta Chloro
Anisole
• n-Butyl Bromide
• Pregabalin
3
Inorganic
Solid waste
28.1 5.16
T/Year
Manufacturing process
of Fexofenadine
Hydrochloride
4
Spent
Carbon
28.3 36
T/Year
Manufacturing process
of
• Benzocaine
• Cetylpyridinium
Chloride
• Febuxostat
• Fexofenadine
Hydrochloride
• Fluconazole
• Lidocaine
Hydrochloride
• Lidocaine
Collection ,Storage
,transportation and
send to CHWIF for
incineration
5
Spent HBr D2 of
Sch-II
324,532
T/Year
Manufacturing process
of
Collection ,Storage
,transportation and
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• 4-Bromomethyl-2-
cyanobiphenyl
• Cis Bromo
Benzoate
• Meta Bromo Nitro
Benzene
sale to actual end
user having
permission under
Rule-9
6
Spent
Hydrochloric
Acid
D2 of
Sch-II
424.332
T/Year
Manufacturing process
of
• 1,3-Dichloroacetone
• Cis Bromo Benzoate
• Fexofenadine
Hydrochloride
Collection ,Storage
,transportation and
sale to actual end
user having
permission under
Rule-9
7
Spent
Sulphuric
Acid
D2 of
Sch-II
7912.96
T/Year
Manufacturing process
of Meta Bromo Nitro
Benzene
And n-Butyl Bromide
Collection ,Storage
,transportation and
sale to actual end
user having
permission under
Rule-9
9
ETP Waste 35.3 360
T/Year
Effluent treatment
plant
Collection ,Storage
,transportation and
send to TSDF for safe
dispsposal
10
MEE Salt 35.3 218.400
T/Year
Multi Effect evaporator Collection ,Storage
,transportation and
send to TSDF for safe
disposal
11
Discarded
Containers 33.1
1.00
T/Year
Raw Material Collection ,Storage
,transportation and
sale to authorized
recycler
12
Used Oil 5.1 0.2
KL/Year
Production machinery Collection ,Storage
,transportation and
sale to authorized
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rerefiner recycler
13 Off
Specificatio
n
28.4 2 T/Year
Process Collection ,Storage
,transportation and
send to CHWIF for
incineration
14
Date Expiry
Products 28.5 2 T/Year
Process Collection ,Storage
,transportation and
send to CHWIF for
incineration
15
Basic
Chromium
Sulphate
A4 LE
II
775.308
T/Year
Manufacturing process
of 1,3-Dichloroacetone
Collection ,Storage
,transportation and
sale to actual end
users having
permission under
rule-9
ii Membership details of TSDF, CHWIF etc. Will become a member of
SEPPL,Kutch after getting TOR.
iii Details of Non-Hazardous waste & its disposal
(MSW and others) -
G Solvent management, VOC emissions etc.
i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents
Name of Solvent used in
process Recovered Loss Total
%
Loss
Acetone 26.509 0.657 27.166 2
Acetonitrile 6.24 0.21 6.45 3
Benzene 5.195 0.105 5.3 2
Chloroform 18.24 0.96 19.2 5
Dichloromethane 84.683 4.083 88.766 5
Diethyl Amine 27.467 1.171 28.638 4
Dimethyl Formamide 3.569 0.095 3.664 3
Ethyl Acetate 26.318 0.81 27.128 3
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imidazole 11.481 0.597 12.078 5
Isopropyl Alcohol 34.568 0.643 35.211 2
MDC 142.252 3.056 145.308 2
Methanol 110.683 3.657 114.34 3
Methyl Isobutyl Ketone 4.87 0.1 4.97 2
n-Hexane 4.144 0.216 4.36 5
Toluene 119.878 2.543 122.421 2
ii VOC emission sources and its mitigation measures
The unit will provide solvent recovery system/distillation for the recovery of solvent. The
solvent will be recovered and reused back in manufacturing process. The solvent will be
recovered through distillation process. The distillation is a process where because of
difference in boiling point solvent will be recovered.
• After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant
of Terms of Reference.
• 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. Explore the use of renewable energy to the maximum extent possible. Details of provisions
to make the project energy-efficient through 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.
3. 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.
4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard
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550th meeting of SEAC-Gujarat, dated 19.09.2019
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during unloading, storage, transportation, handling and processing of Solvents.
5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form.
• 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.
• Further Project Proponent may be advised to submit final EIA Report with EC application within 100
days from the date of issuance of this ToR to expedite processing of Environment Clearance
application.
• The project proponent shall have to apply for Environmental clearance through online portal
http://environmentclearance.nic.in/ along with final EIA report.
Following proposal for which additional details sought in previous SEAC meeting was reviewed
and found that reply is still awaiting from the project proponent even after considerable time has
been lapsed.
Committee unanimously decided to delist the following proposals from the pending application
list of SEAC. It was decided to reopen the file upon submission of additional detail by the Project
Proponent.
1 SIA/GJ/IND2/35239/2019 M/s. Dharti Industries
Plot No.57/1,Sr.No.453, Katosan road,
Detroj, Dist -Ahmedabad
Screening and scoping
2 SIA/GJ/IND2/34081/2010 M/s. Gulshan Polyols Ltd.
Plot No.762, 762/1, 762/2, 762/3, 769/1 &
769/2, GIDC-Jhagadia, Bharuch.
Appraisal
3 Offline Application (B2
Category)
M/s. Mirash industries pvt. Ltd. (UNIT-I)
PLOT NO. D2/14, GIDC Dahej-II, Ta:-
Vagra, Dist:-Bharuch
Screening & Scoping
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Meeting ended with thanks to the Chair.
Minutes approved by:
1. Dr. Dinesh Misra, Chairman, SEAC
2. Shri S. C. Srivastav, Vice Chairman, SEAC
3. Shri Rajesh. I. Shah, Member, SEAC
4. Shri. R. J. Shah, Member, SEAC
5. Shri V. N. Patel, Member, SEAC