minutes of the 424 committee room, geer foundation ... minutes of the 424th i.pdf3 two stage alkali...

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424thmeeting of SEAC-Gujarat, Dated 09.08.2018

Page 1 of 80

Minutes of the 424thmeeting of the StateLevelExpertAppraisalCommittee held on 09/08/2018 at

Committee Room, GEER Foundation, Gandhinagar.

The 424thmeeting of the StateLevel ExpertAppraisalCommittee (SEAC) was held on 9thAugust2018 at

Committee Room, GEER foundation, Gandhinagar. Following members attended the meeting:

1. Dr. Dinesh Misra, Chairman, SEAC

2. Shri S. C. Srivastav, Vice Chairman, SEAC

3. Shri V. N. Patel, Member, SEAC

4. Dr.V. K. Jain, Member, SEAC

5. Shri Rajesh I Shah, Member, SEAC

6. Shri A. K. Muley, Member, SEAC

7. Shri R. J. Shah, Member, SEAC

The agenda of TOR/Scopingcases and Appraisal was taken up. The applicants made presentations on

the activities to be carried out along with other details furnished in the Form-1, PFR, EIA-EMP reports

and other reports.

8. SIA/GJ/IND2/19089/2017 M/s. Krishna Chemicals, Plot No. 6910/A, 6911 GIDC,Ankleshwar, Dist.: Bharuch

Appraisal

Project / Activity No.: 5(f)

Project status: Expansion

• PP has submitted online application vide no. SIA/GJ/IND2/19089/2017dated 07/06/2018 for obtaining

Environmental Clearance.

• The SEAC has recommended to the SEIAA and SEIAA has issued TOR to PP vide letter dated

30/04/2017.

• Project proponent has submitted EIA Report prepared by Aqua-Air Environmental Engineers Pvt.

Ltd., Ankleshwarbased on the TOR issued by MoEF&CC.

• This is an existing unit engaged in Synthetic Organic Chemicals and now proposes for expansion as

tabulated below:

Sr. no.

Name of the Products CAS no. Quantity (MT/Month) End-use of the products Existing Proposed Total

1. Diethyl Meta Amino Phenol

(DEMAP)

91-68-9 2.5 -- 2.5 Dyes Industries 2. Basic Rhodamine B 81-88-9 2.0 -- 2.0

3. Rhodamine B Base 509-34-2 2.0 -- 2.0

4. Metanilic Acid 45% Liquid 121-47-1 -- 200.00 200.00

5. Liquid Basic Dyes

Rhodamine Liquid

81-88-9 --

50.00 50.00

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(Minimum 10% to 40%

Maximum) AND / OR

Auramine O Liquid (Minimum 20% to 50% Maximum)

6. Drying of WetCake of Dyes -- -- 50.00 50.00

7. Liquid Dyes from WetCake of Dyes

-- -- 50.00 50.00

8. Repacking of Dyes and/or Pigments [ Liquid / Dry ]

-- -- 30.0 30.0

TOTAL 6.5 380.0 386.5

• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.

• PP was called for presentation in the SEAC meeting dated 09/08/2018.

• Salient features of the project are as under:

Sr. no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing:0.86 Crores Proposed:0.38 Crores Total: 1.24 Crores

(1) Capital cost for EMS (Environmental Management System):-0.18Crores(Existing +

Proposed)

(2) Recurring cost towards the environmental protection measures:-0.075Crores per Annum.

B Total Plot area ( sq. meter)

Existing:1233sq.meter Proposed:--- Total:1233sq.meter

Green belt area,/Tree Plantation area ( sq. meter)

Existing: 300 sq.meter Proposed:--- Total:300sq.meter

C Employment generation

1. Direct Existing:14 Proposed:35 Total:49

2. Indirect Existing:4 Proposed:8 Total:12

D Water

i

Source of Water Supply(GIDC Bore well, Surface water, Tanker supply r etc...)

GIDC water is a source of water.

Status of permission from the concern authority. Permission letter is attached in EIA report as Annexure-VII.

ii

Water consumption (KL/day)

Existing KL/day

Proposed (Additional) KL/day

Total after Expansion KL/day

Remarks

(A) Domestic 2.0 0.0 2.0 Unit is using fresh

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water for domestic purpose.

(B) Gardening 0.0 0.6 0.6 --

(C) Industrial

Process 1.0 1.8 2.8

Washing& Scrubbing water

3.0 0.03 (Boiler blow down and

cooling bleed off)

3.03

Boiler 1.5 0.2 1.7

Cooling 0.5 0.1 0.6

Others 00 00 00

Industrial Total 6.0 2.13 8.13

Grand Total (A+B+C) 8.0 2.73 10.73

iii

Waste water generation (KL/day)

Category Existing KL/Day



(A) Domestic 1.5 0.0 1.5

(B) Industrial

Process 1.0 0.0 1.0

Washing& Scrubbing water 3.0 0.0 3.0

Boiler 0.0 0.02* 0.02*

Cooling 0.0 0.01* 0.01*

Others 0.0 0.0 0.0

Total Industrial waste water 4.0 0.03* 4.03

* The generated [i.e 0.03 KLD] boiler blow down and cooling bleed off will be mixed with raw water and reused within the plant premises.

iv Treatment facility with capacity (ETP, MEE, STP etc).

Unit has provided primary effluent treatment plant and treated effluent send to CETP-ETL for the further treatment and Total capacity of the ETP is 5.0 KL/day.

v Mode of Disposal & Final meeting point

Domestic:1.5 KL/Day

Industrial:4.03 KL/Day

4 KL/day effluent is being treated in unit’s own effluent treatment plant. After treatment send to ETL. The generated [i.e 0.03 KLD] boiler blow down and cooling bleed off will be mixed with raw water and reused within the plant premises. Sewage will be send in soak pit.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , name of CF

M/s. Environ Technology Ltd., Ankleshwar.

Membership of Common facility (CF) Membership of 4 KLD is attached as Annexure-XVI

vii Reuse/Recycle details (KL/day) --

E Air[Existing & Proposed]

i Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

-

SR. no.

Source of emission

Stack Height

Name of the

Quantity of Fuel

Type of emissions

APCM Emission Standards

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With Capacity e.g. Boiler (8 TPH)

(meter) fuel MT/hr& MT/Day

i.e. Air Pollutants

For Consented Production Capacity

1

Baby Boiler (Capacity 400kg/hr)

10 Natural

Gas

40 Nm3/day

PM SO2 NOx

Not Applica

ble

150 mg/NM3

100 ppm 50 ppm

For Proposed additional production capacity

1

Baby Boiler (Capacity 200kg/hr)

10 Natural

Gas

400 Nm3/day

PM SO2 NOx

Not Applica

ble

150 mg/NM3

100 ppm 50 ppm

-

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.) [Existing & Proposed]

Sr. No.

Stack Attached to

Stack Height(m)

Air Pollution Control System

Parameter Permissible Limit

Existing Process Gas Emission as per CCA –AWH-59287-NIL

Proposed Process Gas Emission

1. Sulphonator Vessel

3 Two stage alkali scrubber

SO2

40 mg/Nm3

2. Blender 3 Bag filter PM 150 mg/Nm3

iii Fugitive emission details with its mitigation measures. [Existing & Proposed] As below

- Carry out work plant area monitoring to find out concentration level in ambient air. - Close handling system. - Provision of breather valve cum flame arrester.

F Hazardous waste (As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.[Existing & Proposed]

i Sr.

no

Type/Nam

e of

Hazardou

s waste

Source of

generation

Categor

y and

Schedul

e as per

HW

Rules.

Quantity

(MT/Annum)

Disposal Method

Existing Proposed Total

1 Used Oil From

lubrication of

machineries

5.1 0.024 KL/year

0.024 KL/year

0.048 KL/year

Collection, Storage,

Transportation and

sold to authorized

Recyclers.

2 Discarded

containers

From raw

material

packing

33.1 1.2 MT/year

1.2 MT/year

2.4

MT/year


Decontamination or

sold to authorized

recycler.

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3 Filter & Filter bags from centrifuge

From

centrifuge

35.1 24-36 nos/year

24-36 nos/year

48-72 nos/year

Reused or sale to

GPCB authorized

recycler.

4 Process waste [ Gypsum]

From

manufacturin

g process

26.1 26.4 MT/year

1284 MT/year

1310.4 MT/year

Collection, Storage, Transportation and sent to Co-process / TSDF site.

5 Process waste [ Iron sludge]

From

manufacturin

g process

26.1 96 Mt/year

1920 MT/year

2016 MT/year

Collection, Storage, Transportation and sent to Co-process / TSDF site.

Quantity of discarded containers must be in MT/Annum.

ii Membership details of TSDF, CHWIF etc. Unit is having membership in common TSDF site M/s. BEIL, Ankleshwar.

iii Details of Non-Hazardous waste & its disposal (MSW and others)

Association is collecting MSW and disposed as per rule.

G Solvent management, VOC emissions etc. Not applicable

i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents.

Unit is using methanol, acetic acid, nitrobenzene as a reactant. It will be fully consume in process. There is no solvent recovery required.

ii VOC emission sources and its mitigation measures

Source:-Flange joints of pipelines & pumps, Liquid raw material transferring to reactor, Loading /unloading at storage area Mitigation Measures:- 1) Routine &periodic inspection to check leakage. 2) Preventive maintenance, Follow SOP for maintenance. 3) Pumps are mechanical seal type. 4) LDAR program is being followed. Provision of Flange guard. Feeding of liquid raw material is carried out by closed pipeline and mechanical seal pump. Unloading through pipeline to tank in a close system.

• During the meeting dated 09/08/2018, technical presentation made by project proponent.

• The proposal is for expansion of existing products and addition of new products.

• Salient features of the project submitted by PP are as mentioned above.

Observation:

• This unit is having valid CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP

ensured that there are no court cases pending and no public complaints against the project.

• Existing 4 KLD effluent is being treated in unit’s own effluent treatment plant before sending to ETL.

No additional discharge to ETL after proposed expansion. Generated additional waste water [i.e 0.03

KLD] from boiler blow down and cooling bleed off will be mixed with raw water and reused within the

plant premises.

• Natural gas will be used as a fuel.

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• There will be no process gaseous emission.

• Management of Hazardous waste is proposed as per the HW Rules 2016.

• The baseline environmental quality has been assessed for various components of the environment

viz. air, noise, water, biological and socioeconomic aspect. The baseline environmental study has

been conducted for the study area of 5 km radial distance from project site for the period March 2017

to May 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, and VOC

at eight locations, including the project site. Values conform to the prescribed standards for Ambient

Air Quality. The incremental Ground Level Concentration (GLC) has been computed using ISCST-3.

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). Though the area is found to be of rocky terrain but

the TDS content of the sample is observed to be maximum up to 2020mg/l in Motali which is little bit

above on acceptable limit. Flash Fire, UVCE & Late Pool Fire Scenarios is considered as worst case

scenario; for that maximum distance of vapour travel is 3.46 m in case of release of methanol. The

detail proposed safeguard measures including On-Site / Off-Site Emergency Plan has been covered

in the RA report.

Discussions & Conclusion:

• Generated bleed liquor will be sent to ETP, however it is not shown as Hazardous waste.

• Safety details of Oleum are required to be submitted by PP.

• Characteristics of waste water shown are different than presented before the Committee.

• Committee instructed to re-check the EIA report & come again after resubmission of EIA report with

all corrected details/Information.

After deliberation, it was unanimously decided to consider the project for further appraisal only after

satisfactory submission of the revised EIA report.

9. SIA/GJ/IND2/19967/2017 M/s.Novazeal Life Science Plot No. 806, GIDC, Kerala, Ta.: Bavla, Dist.: Ahmedabad

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/19967/20177dated 18/06/2018 for

obtaining Environmental Clearance.

• The SEAC has recommended to the SEIAA and SEIAA has issued TOR to PP vide letter dated

31/01/2018.

• Project proponent has submitted EIA Report prepared by M/s: Excel Enviro Tech,

Ahmedabadbased on the TOR issued by SEIAA.

• This is an existing unit engaged in Synthetic Organic Chemicals and now proposes for expansion as

tabulated below:

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Sr.

No.

Name of the

Products CAS no. /CI no.

Quantity, MT/Month End-use of products

Existing chang

e Total

1 Sodium Bromide powder

7647-15-6 50 -50 0 Hypnotic,

Anticonvulsant

2 Sodium Bromide solution

7647-15-6 25 -20 5

3 Potassium Bromide powder

7758-02-3 25 -25 0 Anti-Seizure

4 Chlomiphene Citrate

50-41-9 0 1 1 Treating Infertility.

5 Oxyclozanide 2277-92-1 0 15 15 Used In The Treatment

And Control Of Fascioliasis In Ruminants.

6 Bupropione hydrochloride

31677-93-7 0 5 5 To Treat Major Depressive

Disorder & Seasonal Affective Disorder.

7 Benfotiamine 22457-89-2 0 1 1 As A Prescription Drug For

Diabetes In Europe.

8 n-butyl bromide AND/OR Iso propyl bromide AND/OR

n-propyl bromide

109-65-9

0 30 30

Used As A Source Of

The Butyl Group In

Organic Synthesis

9 75-26-3

10 106-94-5

11 Chlorzoxazone 95-25-0 0 10 10 Muscle Relaxer.

12 Piroxicam 36322-90-4 0 5 5 Used To Reduce Pain,

Swelling, And Joint Stiffness From Arthritis.

13 NitrazepamAND/OR

Diazepam

146-22-5 0 10 10

Used For Short-Term Treatment Of Sleeping

Problems

14 439-14-5 To Treat Anxiety, Alcohol Withdrawal, And Seizures

15 BuclazinedihydrochlorideAND/OR Meclazinedihydro

chloride

129-74-8

0 10 10

Used As An Antivertigo/Antiemetic

Agent.

16 1104-22-9 Used To Prevent And Treat

Nausea, Vomiting,

17 Tramadol hydrochloride

36282-47-0 0 5 5 To Help Relieve Moderate To Moderately Severe Pain

Bulk Drugs

18 Duloxetine hydrochloride

136434-34-9 0 5 5 Used To

Treat Depression And Anxiety

19 Dapoxetine hydrochloride

129938-20-1 0 5 5 Bulk Drugs

20 Lidocaine hydrochloride

73-78-9 0 5 5 Used To Decrease Discomfort Or Pain.

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Total 100 12 112

• The project falls under Category B of project activity 5(f) as per the schedule of EIA Notification 2006.



Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: 0.75 Crore

Proposed: 1.00 Crores

Total: 1.75

B Total Plot area

( sq. meter)

Existing: 1036 Sq. m.

Proposed: -- NIL Sq. m.

Total: 1036 Sq. m.

Green belt area,/Tree Plantation area

( sq. meter)

Existing: 24.5 Sq. m.

Proposed: 280.5 Sq. m.

Total: 305 Sq. m.

C Employment generation Existing: 10

Proposed: 20

Total:30

D Water

i

Source of Water Supply

(GIDC Bore well, Surface water, Tanker supply etc...)

GIDC

Status of permission from the concern authority. Water requirement will be fulfilled by

GIDC water supply.

ii Water consumption (KLD)

Existing

KLD

Proposed (Additional)

KLD

Total after Expansion

KLD Remarks

(A) Domestic 1.5 1.5 3.0

(B) Gardening 0.0 0.5 0.5

(C) Industrial

Process 0.0 1.7 1.7 The generated waste water will be sent to evaporator system and condensate

recovery 4 KL/day will be reused in boiler within the

plant premises.

Washing 0.0 0.5 0.5

Boiler 2.0 4**+ 6 4** + 8

Cooling 0.0 3.0 3.0

Others 0.0 0.2 0.2

Industrial Total 2.0 4** + 11.4 4** + 13.4

Grand Total (A+B+C)

3.5 4** + 13.4 4** + 16.9

Note - ** - includes the reuse water quantity

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1) Total water requirement for the project: 20.9 KLD

2) Quantity to be recycle: 4.0 KLD

3) Total fresh water requirement: 16.9 KLD

iii Waste water generation (KLD)

Category Existing

KLD

Proposed (Additional)

KLD

Total after Expansion

KLD Remarks

(A) Domestic 1.0 1.2 2.2

(B) Industrial

Process 0.0 3.4 3.4 The generated waste water will be sent to evaporator system and condensate recovery 4 KL/day will be reused in boiler within the

plant premises.

Washing 0.0 0.5 0.5

Boiler 0.05 0.45 0.5

Cooling 0.00 0.02 0.02

Others 0.0 0.2 0.2

Total Industrial waste water

0.05 4.57 4.62

Total (A + B) 1.05 5.82 6.87

iv Treatment facility within premises with capacity [For existing and Proposed]

[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc..

Details of the ETP Units (ETP Adequacy)

Sr. No.

Name of Unit Capacity in m3 Retention time

1 Collection Cum Equalization Tank 5.00 >24 hours

2 Neutralizer Tank 5.00 > 24 hours

3 Filter Press 24 X 24 X 24 nos. ---

4 Final Holding Tank 6.00 >24 hours

5 Stripper unit followed by single effect evaporator

250 kg/hr --


Domestic: Domestic :2.2 KLD To soak pit through septic tank

Industrial: Industrial : 4.67 KLD The industrial effluent (4.62 KL/day) shall be treated in ETP; consisting of

primary treatment facilities & then it will be evaporated within the plant premises

through evaporator system

Vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF etc.

Name of Common facility

Unit has CHWIF facility.

SEPPL certificate of CHWIF.

Membership of Common facility (CF)

Unit has received CHWIF membership of SEPPL on dated 08/03/2018.

vii Reuse/Recycle details (KLD)

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4.0 KLD Condensate water reused.

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)

Consented

1 Boiler (400 Kg/hr)

10 m Agrowaste / Briquettes

2 MT/day

PM SO2 NOx

Multi cyclone Dust Collector

Additional

1

Steam Boilers – 2 Nos. (1T/hr.)

11 m Coal / Agro

waste 0.8 T/hr

PM SO2 NOx

Multi cyclone, bag filter followed by water scrubber

2 D. G. Set (10 KVA)

6 m Diesel 7.5 L/hr. PM SO2 NOx

--

Ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)

Existing & Proposed

Sr. no.

Source of emission

Type of emission

Stack/Vent Height (meter)

Air Pollution Control Measures (APCM)

Consented

1 Reaction Vessel Br2, HBr2 30 m Alkali scrubber

Additional

1 Reactors

HCl Cl2 SO2 NOx

11 m Waterscrubber followed by CausticScrubber

Iii Fugitive emission details with its mitigation measures.

There will be a chance of fugitive emission from the manufacturing process as well as due to storage & handling of raw materials and product. The unit will take following adequate precaution for the control of fugitive emission: 1. Install appropriate, effective equipment for complete combustion. 2. Unit is using coal/agro waste as a fuel in High therm Boiler & Glass Line Reaction vessel, which is ecofriendly& less polluting. So, there will be no APCM is required. 3. We will use D.G.Set only in case of power failure. 4. Moreover, adequate stack height is provided. 5. Wind breaking walls provided to ensure that the fugitive emissions are not travelling beyond the premises. Green belt will be developed along the periphery.

F Hazardous waste

(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules

2016.Existing & Proposed

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I

Sr. no.

Type/Name of

Hazardous waste

Source of generation

Category and

Schedule as

per HW Rules.

Quantity (MT/Annum)

Disposal Method Consent

ed Additio

nal Tota

l

1

Discarded containers / barrels /

liners

Raw materials Handling

33.1 0.6 MT 4.4 MT 5 MT

Collection, Storage, transportation and

sold out to Registered Recyclers.

2 Used Oil Manufacturing Process

5.1 0.005 MT 0.3 MT 0.305 MT


sold out to Registered Recyclers.

3 Spent

Solvent Manufacturing Process

20.2 0.0 300 MT 300 MT

Recycled and Reused back in next batch.

4 Distillation Residue

Manufacturing Process

20.3 0.0 8 MT 8 MT Collection, Storage, transportation and

sent to CHWIF.

5 Inorganic

Acid HCl


B-15 0.0 15 MT 15 MT

Collection, storage, transportation and

sold out to the authorized person.

6

ETP sludge

including Evaporator

Residue

ETP Process

35.3 Whatever generate

d 14 MT

14 MT


sent to secured land fill site.

Ii Membership details of TSDF, CHWIF etc.

Unit has membership of SEPPL for CHWIF

facility.

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

The unit proposes in-house facility for solvent recovery.

Ii VOC emission sources and its mitigation measures

VOC Emission sources solvent handling and it will be controlled with packed carbon column

• During the meeting dated 09/08/2018, technical presentation made by project proponent.

• At present unit is engaged in manufacturing of Inorganic products for which they have obtained

CC&A of the Board. The proposal is for expansion by addition of new Synthetic Organic Chemicals.

• Salient features of the project submitted by PP are as mentioned above.

Observation:

• This unit is having valid CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP

ensured that there are no court cases pending and no public complaints against the project.

• The water consumption will be 20.9 KLD after proposed expansion and wastewater generation will be

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4.62 KLD. The industrial effluent will be treated in primary ETP and then evaporated in plant

premises throughEvaporator system.

• Agro waste briquettes & Coal will be used as a fuel. APCM is proposed for flue gas & process

gaseous emission.

• Sources of Hazardous waste not properly addressed.



been conducted for the study area of 10 km radial distance from project site for the period October

2017 to December 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2,

NOx, HCl, Cl2 and VOC at eight locations, including the project site. Values conform to the

prescribed standards for Ambient Air Quality. The incremental Ground Level Concentration (GLC)

has been computed using AERMOD. 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). The absence of

heavy metals and other pollutant concentration indicates that any industrial waste, sewage water

does not pollute the ground water quality.Toluene and xylene, butanol, methanol and propanol,

mono-Chloro-Benzene, mono-Chloro-Benzene, Thionylchloride, chlorine gas is major hazardous

chemicals used as raw material to be stored. Risk assessment including prediction of the worst-case

scenario and maximum credible accident scenarios has been carried out. The detail proposed

safeguard measures including On-Site / Off-Site Emergency Plan has been covered in the RA report.

Discussions & Conclusion:

• Generated bleed liquor & its management is not properly addressed.

• Committee deliberated on fire safety, storage of hazardous chemicals, LDAR, adequacy of

ETP,reuse of treated waste water etc.

• All the solvents will be stored in Drums only.

• No storage tanks for storage of Hazardous chemicals.

• Only one Cylinder (Cap. 100 Kg) will be kept for storage of Chlorine as a raw material.

• After deliberation, it was unanimously decided to consider the proposal only after satisfactory

submission of the following:

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.

2. Adequacy of ETP for achieving ZLD & feasibility of waste water reuse for industrial purpose. .

Stage wise characteristics of waste water considering worst case scenario. Qualitative &

quantitative analysis for Product wise waste water generation shall be incorporated.

3. Revised Lay-out plan with fire & safety details.

4. Safety precautions including flame proof electric fittings to be taken for solvent storage area to

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avoid fire hazard.

5. Exact sources of Hazardous wastes & management of bleed liquor as per the HW Rules

2016.

10. SIA/GJ/IND2/27670/2017 M/s. IOCL SidhpurTerminal Sidhpur Terminal Sujanpur State Highway, Sidhpur, Patan.

Appraisal

Project / Activity No.: 6(b)


• PP has submitted online application vide no. SIA/GJ/IND2/27670/2017dated30/06/2018 for obtaining

Environmental Clearance.

• MoEF&CChas issued TOR to PP vide letter dated 08/12/2017.

• Project proponent has submitted EIA Report prepared by Engineers India Limited,based on the TOR

issued by MoEF&CC.

• This is an existing unit engaged in Hazardous waste storage facility and now proposes for expansion

as tabulated below:

Sr. no.

Name of the Hazardous chemicals for storage

Storage details Quantity (MT/Month) End-use of the products Existing Proposed Total

1 MS Existing: 4 tanks Proposed: Nil

11195 KL 4 tanks

- 11195 KL 4 tanks

Motor Spirit

2 SKO Existing: 3 tanks Proposed: Nil

6090 KL 3 tanks

- 6090 KL 3 tanks

Kerosene

3 HSD Existing: 4 tanks Proposed: Nil

31038 KL 4 tanks

- 31038 KL 4 tanks

Diesel

4 Ethanol Existing: 2 tanks Proposed: 1 tank

140 KL 2 tanks

750 KL 1 tank

890 KL 3 tanks

Ethanol

• The project falls under Category B of project activity 6(b) as per the schedule of EIA Notification

2006.



Sr. no.

Particulars Details


(Rs. in Crores):

Existing: NA Proposed: 2.51 crores Total: 2.51 crores

1. Capital cost for EMS (Environmental Management System): 5-6 Lakhs

2. Recurring cost towards the environmental protection measures: 2-3 Lakhs per Annum.

B Total Plot area ( sq. meter) Existing: 71 acre (287327 sq. m) Proposed: Nil Total: 71 acre (287327 sq. m)

Green belt area,/Tree Plantation area ( sq. meter) Existing: 9.8 acre(39659.2 sq. m) Proposed: Nil Total: 9.8 acre(39659.2 sq. m)


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1. Direct Nil

2. Indirect 30

Total 30

D Water

i


Bore well

Status of permission from the concern authority. -

ii

Water consumption (KLD)

Category

Water Consumption KLD

(A) Domestic 2

(B) Gardening -

(C) Industrial

Process 6

Washing -

Boiler -

Cooling -

Others -

Industrial Total 6

Total (A + B + C) 8

1) Total water requirement for the project: Nil. The water requirement will be adjusted from

existing water supply i.e. 8 KLD available to Sidhpur terminal.

2) Quantity to be recycle: 5 KLD

3) Total fresh water requirement: 8 KLD.


-

Category KLD

(A) Domestic 1

(B) Industrial

Process 5 (intermittent)

Washing -

Boiler -

Cooling -

Others -

Total Industrial waste water 6

-

iv Treatment facility with capacity (ETP, CETP, MEE, STP, Spray Dryer etc).

ETP of 20 m3/Day

v Mode of Disposal & Final meeting point Domestic: Soak pit

Industrial: Treated effluent will be used in gardening of the terminal.


Not Applicable

Membership of Common facility (CF) Not Applicable

vii Reuse/Recycle details (KLD) 5 KLD

E Air

i Flue gas emission details

of 80


Page 15 of 80


-

SR. no.

Source of emission

With Capacity

Stack Height (Feet)

Type of

Fuel



Air Pollution Control Measures

(APCM)

1 DG-320 KVA 32.8 ft HSD 60

Litre/Day SOx, NOx

Acoustic enclosures

2 DG-320 KVA 32.8 ft

HSD 60

Litre/Day SOx, NOx

Acoustic enclosures

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)

-

Sr. no.

Source of emission

Type of emission


Air Pollution Control Measures

(APCM)

1 DG Stack SOx, NOx

As per serial no

E(i) As per Serial no E(i)

iii Fugitive emission details with its mitigation measures. As below:

Fugitive emission will be identified through LDAR program and adequate mitigation measures will be taken.

F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.

i

Sr. no.

Type/Name of Hazardous waste


Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Disposal Method

1 ETP Waste ETP 34.3 200 kg/Year TSDF

2 Used Oil DG sets 5.1 50 L/year Registered re-processors

3 Oil residue Pumps 3.1 50 L/year Registered re-processors

4 Discarded container

Oil container

33.3 120 nos./year

Authorized recyclers


ii Membership details of TSDF, CHWIF etc. GPCB approved TSDF sites.

ii Details of Non-Hazardous waste & its disposal (MSW and others)

Nil

G Solvent management& VOC emissions etc.

i Details of Solvent recovery (As per respective ToR) Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents

Not Applicable

ii VOC emission sources and its mitigation measures Proposed Ethanol tank is Internal Floating Roof Tank with mechanical seal fitted over it. Therefore there will not be any increase in quantity of emission from present limit.

• During the meeting dated 09/08/2018, technical presentation made by the project proponent.


of 80


Page 16 of 80


been conducted for the study area of 10 km radial distance from project site for the period January to

March 2018. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, and VOC

at 6 locations, including the project site. Values conform to the prescribed standards for Ambient Air

Quality.

• The project does not envisage any air pollution. Only during power failures, DG sets shall be used

and it has been provided with adequate stack height for dispersion.

• All Motor spirit tanks are floating roof followed by Diesel tanks and SKO tanks are cone roof type.

Existing Ethanol tanks are underground.

• During meeting, Committee discussed about safety awareness, fire detection, fire fighting system,

CSR etc.

• The fire protection system confirms to OISD‐117 guidelines. Fire protection system consists of

� Fire water system with fire hydrants and monitors covering the entire Terminal

� Water cooling system (Sprinkler System) for MS and HSD storage tanks.

� Portable fire extinguishers and foam monitors for firefighting operations

� Firefighting, first aid and safety appliances.

� High Volume Long Range Monitors (HVLR)

� Rim Seal Fire Detection and Extinguishing System

� Water for firefighting is stored in above ground tanks of 10300 KL capacity. Water storage

capacity is sufficient to fight fire for 4 hrs conforming to OISD‐117.

• 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.

• The existing plant has valid CC&A vide no. AWH-64898 valid up to 20/07/2019. This unit was

established well before year 2006. PP has submitted compliance of the existing unit. Instructions

received from GPCB are submitted and are compiled being general in nature. PP ensured that there

are no court cases pending against the project and there are no public complaints against the unit.

Compliance of the ToR was found satisfactory. After detailed discussion, it was decided to

recommend the project to SEIAA Gujarat for grant of Environmental Clearance.

11. IA/GJ/IND2/65259/2017 M/s. IOCL Kandla Fore Shore terminal Gandhidham, Kutch.

TOR Amendment

Project / Activity No.: 6(b)


• MoEF&CC, New Delhi has accorded Terms of Reference [ToR] to IOCL, Kandla Fore Shore

terminal vide letter dated 17/08/2017.

• PP has submitted online application vide no. IA/GJ/IND2/65259/2017dated 30/06/2018 for obtaining

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Page 17 of 80

amendment for TOR.

• PP has requested to amend the additional storage capacity of Hazardous Chemicals as below:

Sr. no.

Name of the Hazardous chemicals for storage

Storage details Quantity (MT/Month) End-use of

the products Existing Proposed Total

1 MS Existing: 4 tanks Proposed: Nil tank

70684 KL 4 tanks

- 70684 KL 4 tanks

Motor Spirit

2 HSD Existing: 7 tanks Proposed: Nil tank

191250 KL 7 tanks

- 191250 KL 7 tanks

Diesel

3 SKO Existing: 1 tank Proposed: Nil

23750 KL 1 tank

- 23750 KL 1 tank

Kerosene

4 ATF Existing: 2 tanks Proposed: Nil

47500 KL 2 tanks

- 47500 KL 2 tanks

ATF

5 Naphtha Existing: 10 tanks Proposed: Nil tank

160326 KL 10 tanks

- 160326 KL 10 tanks

Naphtha

5 Ethanol Existing: 3 tanks Proposed: 3 tanks

110 KL 3 tanks

600 KL 3 tanks

710 KL 6 tanks

Ethanol


• During the meeting, technical presentation made by the project proponent.

• Presentation was made by the project proponent for TOR amendment.

• PP presented that they had applied for TOR in June 2017 to MoEF&CC when SEIAA/SEAC of

Gujarat were not in function.

• Standard TOR was issued by MoEF&CC considering Public Hearing for the proposed project.

• TOR Amendment for the proposed project was applied to SEIAA/SEAC for waiver of Public Hearing

considering the location in the Port Notified area.

Referring to the circular dated 23/10/2017 of MoEF&CC, New Delhi. Committee deliberated that

since TOR is accorded from MOEF&CC and this application is not for appraisal, hence PP was

asked to apply for amendment in TOR for the aforementioned changes to MoEF&CC/EAC, New

Delhi only.

12. SIA/GJ/MIS/26169/2018 M/s. Zydus Infrastructure Pvt Ltd. “PHARMEZ”, Pharmaceutical SEZ, SarkhejBavla Road, N.H. No. 8-A, Matoda, Sanand, Ahmedabad

Screening & Scoping

Project / Activity No.: 7(h)


• PP has submitted online application vide no. SIA/GJ/IND2/26169/2018 dated 18/06/2018 for


• This is an existing unit engaged in Common effluent treatment plant and now proposes for expansion as tabulated below:

Sr. no.

Treatment Facility Capacity

ExistingKLD

ProposedKLD Total After Proposed Expansion KLD

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Page 18 of 80

1 Common Effluent Treatment Plant (CETP)

3000 4500 7500

2 MEE 150 x 2 Nos. (1

W + 1 S)

1 standby will come in

operation

300

• The project falls under category B of project activity 7(h) as per the schedule of the EIA notification

2006.

• PP was called for presentation in SEAC meeting dated 09/08/2018.

• Salient feature of the project including Water, Air and Hazardous waste management:

Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 20 Proposed: 15 Total: 35


Existing: 17919.26 Proposed:3867.15 Total: 21786.41


Existing: 3318.47 Proposed: 3867.15 Total: 7185.62

C Employment generation Existing: 51 Proposed: 19 Total: 70

D Water i

Source of Water Supply (GIDC Bore well, Surface water, Tanker supply r etc...)

Bore well

Status of permission from the concern authority. Application is submitted to CGWA

ii

Water consumption (KLD)

Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

Remarks

(A) Domestic 15 11 21 Fresh water from bore well

(B) Gardening 50 - 50

Industrial

Process - - -

Washing 50 60 110 Treated wastewater from CETP.

Boiler 25 - 25 14 KL/d treated wastewater from CETP and rest fresh water.

Cooling 120 - 120 52 KL/d treated wastewater from CETP and rest fresh water.

Other-Laboratory 1 1 2 Fresh water from bore well

Others-chemical preparation

13 17 30

Industrial Total 209 78 287

Grand Total (A+B+C) 274 84 358

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Page 19 of 80

1) Total water requirement for the project: 358 KLD


3) Total fresh water requirement: 182 KLD

iii

Waste water generation (KLD)

Category Existing KLD



Remarks

(A) Domestic 12 5 17 To CETP

Industrial

Process - - -

To CETP

Washing 50 60 110

Boiler 3 - 3

Cooling 19 - 19

Other-Laboratory 1 1 2


73 61 134

-

iv Treatment facility within premises with capacity [ETP (Primary, Secondary, Tertiary),MEE, Stripper, Spray Dryer, STP etc].

CETP Existing: 3 MLD Proposed: 4.5 MLD Total: 7.5 MLD MEE Existing: 150 x 2 Nos. KLD (1 W + 1 S) Proposed: 1 standby will come in operation Total: 300 KLD


Domestic:Reuse by CETP & member units after treatment in CETP followed by RO & MEE.

Industrial: Reuse by CETP & member units after treatment in CETP followed by RO & MEE.


--

Membership of CF --

vii Reuse/Recycle details (KLD) --

E Air [Existing & Proposed]


-

SR. no.

Source of emission

With Capacity


Type of Fuel

Quantity of Fuel

MT/Day

Type of emissions

i.e. Air Pollutants


Measures (APCM)

Existing

1 Boiler for Multiple Effect Evaporator (3 TPH x 1 No)

30 FO/HSD/ LDO

300 Lit/Hr PM: 150 mg/NM3

NOx: 50 ppm

Not Applicable

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Page 20 of 80

2 D. G. Set (720 kVA x 1 No.)

12 100 Lit/Hr SO2: 100 ppm Not Applicable

3 D. G. Set (320 kVA x 3 Nos)

12 150 Lit/Hr Not Applicable

Proposed

1 D. G. Set (720 kVA x 1 No)

12 FO/HSD/ LDO

100 Lit/Hr PM: 150 mg/NM3

NOx: 50 ppm SO2: 100 ppm

Not Applicable

Existing 2 nos. of 320 kVA DG to be replaced with proposed 720 kVA.

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) [Existing & Proposed]

There is no process gas emission from existing as well in expansion facility.

Iii Fugitive emission details with its mitigation measures. [Existing & Proposed]SAs below:

Following measures are adopted to ensure compliance and further reductions in fugitive emissions wherever possible; the same will be continued after expansion.

• The fugitive emissions in terms of handling losses are reduced by proper storage and handling.

• Chemicals are stored as per standard criteria.

• Proper ventilation in storage area is provided and all materials are being stored in suitable packing to prevent contamination of air due to particulates.

• The coverage of greenbelt around the plant consisting of noise and air pollution capturing species also acts as natural barrier to stop carrying of dust along with the wind current. Good housekeeping is maintained in the plant

F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. [Existing & Proposed]

i

Sr. no.




Quantity (MT/Annum)

Disposal Method

Existing

Proposed

Total

1 CETP Sludge CETP 35.3 45 68 113 Collection storage & disposal to approved TSDF for land filling.

2 MEE/ Decanter salt

MEE 37.3 340 510 850 Collection storage & disposal to approved TSDF for land filling.

3 Used oil Plant Machiner

y

5.1 1 1 2 Collection, storage and reuse as lubricants in

plant within the premises only and/or send to authorized

recyclers.

4 Discarded bags Raw material storage

area

33.1 574 864 1438

Collection storage & use for packing of chemical sludge


ii Membership details of TSDF, CHWIF etc. Unit has obtained required membership of TSDF

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Page 21 of 80

site. The details are as under:

• ZIPL has obtained membership of TSDF site of Nandesari Environment Control Limited for disposal of ETP sludge and MEE/Decanter salts wide letter no. 922 dated 24.11.2014.

• Membership certificate no. ECIPL/TSDF/001 dated 06-04-2016 is issued by Eco-care Infrastructure Private Limited


None

Technical presentation was made by the project proponent. The proposal is for expansion of existing CETP

capacity 3000 KLD to 7500 KLD and MEE capacity 150 KLD to 300 KLD. ZIPL has obtained EC for existing

CETP from SEIAA, Gujarat. Unit has valid CC&A. Compliance status of EC and CC&A was discussed at

length. There was no court case and legal action pending against unit. Committee noted that PP has

proposed to receive waste water from the member units located within the SEZ of ZIPL as well as the units

located outside the SEZ. Upon asking about the justification to receive effluent from the outside members,

Project proponent could not reply satisfactorily.Committee also noted that PP could not justify the proposed

expansion up to 7.5 MLD.

• After deliberation, it was unanimously decided to consider the proposal for scoping, only after

satisfactory submission of the following:

1. Executive summary regarding a prima facie idea of the objectives of the proposed expansion.

2. Need for the proposed expansion should be justified in detail and Justification for selecting the

proposed unit size.

13. SIA/GJ/MIS/21284/2017 M/s. Zydus Infrastructure Pvt Ltd “PHARMEA”, Special Economic Zone (SEZ), Matoda, Sanand, Ahmedabad

EC Amendment

I. SEIAA, Gujarat has accorded Environmental Clearance to Zydus Infrastructure Pvt Ltd vide letter no.

SEIAA/GUJ/EC/7(h)/237/2017 vide dated 24/04/2017.

II. Now, project proponent has applied online vide proposal no. SIA/GJ/MIS/21284/2017 vide dated

15/05/2018 for Corrigendum in EC.

III. This proposal was considered in the SEAC meeting dated 09/08/2018. During the meeting, Committee

noted that SEIAA, Gujarat has issued Environmental Clearance to Zydus Infrastructure Pvt Ltd for

setting up of ‘Common Effluent Treatment’ plant at “PHARMEA”, Special Economic Zone (SEZ),

Matoda, Sanand, Ahmedabad. During SEAC meeting, referring to the Earlier Environmental Clearance

and amendment application, Committee noticed that PP requested to amend as below:

Sr. no.

Condition no. in which changes proposed.

As per EC As per proposed amendment

Justification

1 Condition No.

2

Page-1

ZIPL shall accept

wastewater from

Pharmaceutical formulation

ZIPL shall accept industrial

and sewage wastewater

confirming CETP inlet

At current facility

GPCB has allowed

members units

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Page 22 of 80

units located within the

Pharmez-Special Economic

Zone and under no

circumstances any other

unit shall be allowed to be

the member of the CETP

as per the undertaking

submitted with EIA report

norms from only those

pharmaceutical industries

(formulation, R & D,

Diagnostic kits, Trans

Dermal Patches) permitted

by GPCB located within

Pharmez-Special

Economic Zone as well as

outside the SEZ.

located outside the

SEZ (CTE of CETP is

submitted)

2 Condition No.

17

Page-2

ZIPL shall establish the

CETP of 3 MLD capacity

having adequate

Equalization, Primary

Treatment, Biological

Treatment (based on SBR

process) and tertiary

effluent treatment facilities

(as mentioned in EIA

report)

ZIPL shall establish the

CETP of 3 MLD capacity

having adequate

Equalization, Primary

Treatment, Biological

Treatment (based on MBR

process) and tertiary

effluent treatment facilities

(as mentioned in EIA

report)

Typographical error.

As per Section

2.5.2.3 page no. 2-9

of EIA report

biological treatment

is MBR based

3 Condition No.

20

Page-2

The effluent to be received

at CETP shall not have any

sewage from member

units.

CETP may accept

industrial effluent and

sewage from member

units.

At current facility

GPCB has allowed

members units to

convey sewage with

industrial effluent

(CTE of CETP is

enclosed as

Annexure-1)

4 Condition No. 57 Page-3

Project proponent shall

develop green belt all along

the periphery of the TSDF

as per the CPCB guidelines

with plant species that are

significant and used for the

pollution abatement. Drip

irrigation system shall be

used for the green belt for

optimum utilization of the

water resources.

Project proponent shall

develop green belt all

along the periphery of the

CETP as per the CPCB

guidelines with plant

species that are significant

and used for the pollution

abatement. Drip irrigation

system shall be used for

the green belt for optimum

utilization of the water

resources.

Typographical error.

IV. During the meeting, Committee deliberated on the amendment sought.

V. Committee noted that earlier, ZIPL has proposed that they will accept wastewater from Pharmaceutical

formulation units located within the Pharmez-Special Economic Zone only and based on the EIA report

and Public hearing carried out by GPCB SEAC had recommended the same to SEIAA, Gujarat which

was approved by the Authority. Committee was of the view that under no circumstances any other unit

shall be allowed to be the member of the CETP as per the undertaking submitted with EIA report.

Hence, Committee decided to not amend point no.1 i.e. Condition no.2 will remain unchanged.

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Page 23 of 80

VI. Further, Committee noted thatMBR process was proposed as Biological Treatment in EIA report.It was

mentioned in the EIA report that industrial effluent and sewage from member units will be accepted.

VII. Committee noted that at Condition No. 57 Page-3 of said EC letter, TSDF was inadvertently written due

to typographical error in place of CETP.

VIII. After deliberation, Committee decided to recommend amendment in Environment Clearance dated

24/04/2017 vide letter no. SEIAA/GUJ/EC/7(h)/237/2017 for amended as below:

Sr. no.

Condition no. in which changes proposed.

Amendment of EC as below:

1 Condition No.

17

Page-2

ZIPL shall establish the CETP of 3 MLD capacity having adequate

Equalization, Primary Treatment, Biological Treatment (based on MBR

process) and tertiary effluent treatment facilities (as mentioned in EIA

report)

2 Condition No.

20

Page-2

CETP may accept industrial effluent mixed with sewage of their own from

member units.

3 Condition No. 57 Page-3

Project proponent shall develop green belt all along the periphery of the

CETP as per the CPCB guidelines with plant species that are significant

and used for the pollution abatement. Drip irrigation system shall be used

for the green belt for optimum utilization of the water resources.

Additional Agenda:

1 SIA/GJ/IND2/21984/2015 M/s. Consumer Plastic Private Limited Plot No. 16-19, Phase-I, GIDC, Taluka Vapi, Dist. Valsad.

Reconsideration – EC





• MoEF&CC issued TOR to PP vide letter dated 26/05/2015.

• Project proponent has submitted EIA Report prepared by M/s: Precitech Laboratories Pvt.

Ltd., based on the TOR issued by MoEF&CC.

• This is an existing unit engaged in Synthetic organic chemicals and now proposes for

expansion as tabulated below:

Sr. No.

Name of Finished products

CAS No. Quantity in T/month End use of product Existin

g Propose

d Total

1. PVC/ HDPE Pipes ----- 40.0 NIL 40.0

Agriculture piping & plumbing

2. EpoxidisedSoyabean Oil

8013-07-8 200.0 400.0 600.0

Used as plasticizers in PVC, Cable,

Adhesive and plastic films

3. Methyl Soyate -----

4. Di Octyl Phthalate (DOP) (117-81-7) Nil 1000.0 1000.0 5. Di-Iso-Nonyl Phthalate 28553-12-

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Page 24 of 80

(DINP) 0 etc.

6. Di-IsoDecyl Phthalates (DIDP)

26761400

7. Di Butyl Phthalates (DBP)

(84-74-2)

8. Di Octyl Maleate (DOM) (142-16-5)

9. Di Butyl Maleate (DBM) (105-76-0)

10.

Di (2-Ethylhexyl) Adipate (DOA)

(103-23-1)

11.

Polymer Compound & Master Batch

----- Nil 500.0 500.0

Plastics & PVC products

12.

Plastic Extruded &Moulded Products

----- Nil 500.0 500.0

Household & Packaging

items

Total 240.0 2400.0 2640.0

• The project falls under Category B of project activity 5(f) as per the schedule of EIA

Notification 2006.



Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores):

Existing: 0.57 Proposed: 2.93 Total: 3.5

B Total Plot area (sq. meter) Existing: 6761 Sq. m. Proposed: No additional land will be required for proposed expansion. Total: 6761 Sq. m.

Green belt area, /Tree Plantation area (sq. meter)

Existing: 1500 Sq. m. Proposed: 570 Sq. m. Total: 2070 Sq. m.

C Employment generation Existing: 24 Proposed: 16 Total: 40

D Water

i Source of Water Supply (GIDC, Bore well, Surface water etc...)

GIDC Water supply department

Status of permission from the concern authority.

Available

ii Water consumption (KL/day)

*Existing KL/day


**Total after Expansion KL/day

Remarks

(A) Domestic 5.0 3.0 8.0


(C) Industrial

Process --- 20.0 20.0

Washing 1.0 3.0 4.0

Boiler 1.0 2.0 3.0

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Page 25 of 80

Cooling 15.0 25.0 40.0

Others --- --- ---

Industrial (Total) 17.0 50.0 67.0

Total (A+B+C) 28.0 53.0 81.0

Note: *In existing operations, treated water @2.2 KL/day is reused in gardening/cooling purpose. **After proposed expansion project 25 KL/day treated water will be reused for cooling purpose and 6 KL/day reused for gardening purpose

1) Total water requirement for the project: 81 KL/day 2) Quantity to be recycle: 31 KL/day 3) Total fresh water requirement: 50 KL/day

iii Waste water generation (KL/day)

Category Existing KL/Day



Remarks

(A) Domestic

4.0 2.4 6.4 To septic tank/soak pit system

(B) Industrial

Process 0.0 25.4 25.4 Treated in in-house ETP, RO and MEE

Washing 1.0 3.0 4.0

Boiler 0.2 0.4 0.6

Cooling 1.0 2.0 3.0

Others 0.0 0.0 0.0


2.2 30.8 33.0

iv Treatment facility within premises with capacity [ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.].

Full-fledged ETP followed by RO and MEE will be provided for proposed expansion project.


Domestic: Septic tank/soak pit system

Industrial: Treated water from ETP will be diverted to RO, RO reject will be sent to evaporator. RO permeate along with evaporator condensate will be reused in cooling/gardening purpose. ZLD outside premises.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc., name of CF

None. Zero liquid discharge outside premises for existing and proposed operations.

Membership of CF No

vii Reuse/Recycle details (KL/day) 31 KL/day will be recycled as cooling tower makeup (25 KL/day) and gardening purpose (6 KL/day).



of 80


Page 26 of 80

-

Sr. no.

Source of emission

With Capacity

e.g. Boiler (8 TPH)


Name of the fuel

Quantity of Fuel MT/hr & MT/Day

Type of emissions i.e. Air Pollutant

s

APCM

NAAQS (National

Ambient Air Quality

Standards)

Existing scenario

1

Boiler 600 kg/hr. (100% Load)

Stack Ht:

11m

Natural Gas

@290 SCM/day

PM, SO2, NOx

-----

PM<150 mg/Nm3 SO2< 100 ppm NOx< 50 ppm

Proposed scenario

1

Boiler 600 kg/hr. (100% Load)

Stack Ht:

11m

Natural Gas

@290 SCM/day

PM, SO2, NOx

-----


2

Thermic Fluid Heater 10 lakh kCal/hr.

Stack Ht:

11m

Natural Gas

@2000 SCM/day

PM, SO2, NOx

-----


-

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) [Existing & Proposed]

- There is/will be no process emissions from the manufacturing process.

v Fugitive emission details with its mitigation measures. [Existing & Proposed]

Source Probable pollutant

Control measures

Loading/ unloading and storage of RM & products

VOC and PM

Loading/ unloading of liquid materials in tanks will be done through pipeline. It will be done in a closed system. Hopper will be provided for transfer of solid material.

Storage tank VOC Close handling system. Provision of breather valve cum flame arrester. Regularly work place area monitoring to find out concentration level of VOC in ambient air

Excess material recovery system

VOC Close handling system. Regularly work place area monitoring to find out concentration level of VOC in ambient air

Handling of raw material bags in storage area

PM Provision of exhaust ventilation, Provision of PPE

Flange joints of pipeline, pump & motors

VOC Routine & periodic inspection to check leakage. Preventive maintenance, follow SOP for maintenance. Pumps & motors mechanical seal type

C Hazardous waste

of 80


Page 27 of 80

(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. [Existing & Proposed]

i

Sr. no.




Quantity (MT/Annum) Disposal Method Existing Proposed

after expansion

1 ETP waste/ Evaporation sludge

ETP Cat. 35.3 0.037 T/month

10 T/month Disposed of to CSWD site

2 Used Oil

Machinery

Cat. 5.1 30 Liter/annum

30 Liter/annum

Reused as lubricant in plant operation.

3 Discarded bags

Plant/ Storage

Cat. 33.3 280 Nos/month or 1.8 T/annum

11500 Nos/month or 70 T/annum

Reused for packing / sold to the authorized scrap dealers.

4 Discarded drums

Plant/ Storage

Cat. 33.3 2000 Nos/month or 2.5 T/annum

2285 Nos/month or 2.75 T/annum

Returned back to the supplier / sold to the authorized re-conditioners

5 Plastic Cutting Waste

Process Cat. 21.1 22.5 T/month

142.5 T/month

It is/will be reused back in process


ii Membership details of CETP, TSDF, CHWIF, Common MEE etc.

VGEL/SCN/2015-16/483 for disposal of hazardous waste


None


I Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents

No solvent will be used in process. However, excess material will be recovered through condenser and vacuum distillation. Approximately 90-95% of excess material recovery will be achieved.


• Routine & periodic inspection to check leakage.

• Preventive maintenance, follow SOP for maintenance.

• Pumps & motors mechanical seal type

• Close handling system.

• Regularly work place area monitoring to find out concentration level of VOC in ambient air.

• During the meeting dated 17/04/2018, technical presentation made during the meeting by

project proponent.

• During the meeting, the project was appraised based on the information furnished in the EIA

of 80


Page 28 of 80

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. The baseline

environmental study has been conducted for the study area of 5 km radial distance from

project site for the period March 2017 to May 2017. Ambient Air Quality monitoring was

carried out for PM10, PM2.5, SO2, NOx, VOC, HC, and CO at eight locations, including the

project site. Values conform to the prescribed standards for Ambient Air Quality. The

incremental Ground Level Concentration (GLC) has been computed using ISC- AIRMODE.

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.

• This unit has obtained Earlier EC from MoEF&CC dated 10th February, 2009. The compliance

of EC was submitted regularly. The certified EC compliance report from MoEF&CC, Bhopal

along with action plan has been submitted. They have 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.

• Committee noted that PP has proposed to reuse treated waste water for gardening purpose

which was not agreed to by the Committee and asked them to reuse completely for industrial

purpose.

• Generated Waste streams of Sodium Format and Glycerol are mentioned as by-product.

Committee asked PP to consider such waste streams as hazardous waste.

• Issues related to Safety, CSR etc. have been discussed in detail.

• Committee felt that need based CSR is to be prepared and implemented.

• After deliberation, it was unanimously decided to consider the project for further consideration

only after submission of the following:

1. Adequacy of Zero Liquid Discharge (ZLD) system considering complete reuse of waste water

for industrial purpose instead of reuse for gardening/Plantation.

2. Revised proposal considering Sodium Format and Glycerol which have been mentioned as

by-products in the Hazardous waste category and submit its detailed management plan as per

Hazardous and other Waste rules 2016.

3. Compliance of ToR no. 45 considering need based CSR.

• Project proponent submitted reply vide their letter dated 25/06/2018. PP has submitted as

below:

� Unit will reuse entire quantity of treated wastewater for industrial purpose only by the

adequate ETP system.

� Sodium Formate was mentioned in existing product list as it was mentioned in existing

of 80


Page 29 of 80

EC. However, due to process change in the manufacturing of EpoxidisedSoyabean oil;

there will be no generation of Sodium Formate after proposed expansion. Glycerol is

applicable for CRIT criteria as per the class C of the Sch – II of the Hazardous waste

and Other Rules, 2016. So it will be sold to actual users having permission under the

Rule-9 only.

� Detailed Need based CSR is submitted.

• During the meeting Committee considered this proposal and reply submitted by PP found

satisfactory.

• Compliance of the ToR was found satisfactory.

• After detailed discussion, it was decided to recommend the project to SEIAA, Gujarat

for grant of Environmental Clearance.

2. SIA/GJ/IND2/16029/2016 M/s. ModyChemitech Plot No. D-2/CH-107, G.I.D.C., Dahej, Tal: Vagra, Bharuch.

Corrigendum – EC

• SEIAA, Gujarat has accorded Environmental Clearance to ModyChemitech vide letter no.

SEIAA/GUJ/EC/5(h)/622/2018 vide dated 13/06/2018.

• Now, project proponent has applied online vide proposal no. SIA/GJ/IND2/16029/2016 vide

dated 18/07/2018 for Corrigendum in EC.

• This proposal was considered in the SEAC meeting dated 09/08/2018. During the meeting,

Committee noted that SEIAA, Gujarat has issued Environmental Clearance to

ModyChemitech for setting up of ‘Integrated Paint Industry’ manufacturing plant at Plot No. D-

2/CH-107, G.I.D.C., Dahej, Tal: Vagra, Bharuch.

• During SEAC meeting, referring to the EIA report, Minutes of Meeting and Recommendation

letter & relevant documents, Committee noticed that typographical error has inadvertently

been made and it was written as integrated paint industry (Category 5 h). , Committee noticed

that, category of the industry written as Integrated Paint Industry. But, unit requested to

correct as category of “Synthetic Organic Chemicals”.

• After deliberation, Committee decided to recommend amendment in Environment

Clearance dated 13/06/2018 vide letter no. SEIAA/GUJ/EC/5(h)/245/2017 for correction in

the title (Page 1 of 5) as requested.

3. SIA/GJ/IND2/20487/2017 M/s. Basic International Plot NO. 47/1/3-4-5, Nandesari, GIDC Estate, Opp. AmbikaWiegh Bridge, Nandesari, Vadodara.

Reconsideration of EC Refer back case

Category of the unit: 5(f)

Status of the project: Expansion

M/s. Basic Internationalappliedfor environmental clearance and the SEAC recommended the project

for grant of environmental clearance vide this officeletterno. EIA-10-2017-887 dated 21/03/2018for

of 80


Page 30 of 80

setting up of Synthetic Organic Chemicals manufacturing plant as mentioned therein:

The case was referred back by the SEIAA, Gujarat vide no. SEIAA/GUJ/EC/5(f)/348/2018 dated

28/03/2018 with the following point:

1) To verify the applicability of 18(1)(b) direction issued by CPCB to SPCB and the compliance of

existing infrastructure.

Project proponent submitted reply vide their letter dated 28/06/2018. PP has submitted as below:

� The unit will dispose the treated wastewater to the Common MEE facility at BEIL. So, there

will be not applicability of 18(1)(b) direction issued by CPCB to SPCB.

During the SEAC meeting dated 09/08/2018, the said reply was considered by the Committee.

Committee found that reply submitted by PP was satisfactory.

In view of the above stated facts, Committee decided to forward the proposal to SEIAA for the

grant of environmental clearance with addition of the following specific conditions and with

rest of the conditions same as prescribed in the earlier recommendation letter no. EIA-10-

2017-887 dated 21/03/2018.

1. Unit shall comply direction under section 18 (1) (b) of the Water (Prevention and Control of

Pollution) act, 1974 issued by CPCB regarding compliance of CETP.

2. In case of non-compliance of CETP, Unit shall send their waste water to Common MEE of

BEIL, Ankleshwar.

3. Unit shall have to comply any conditions imposed by GPCB regarding direction under section

18 (1) (b) of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB.

4. SIA/GJ/IND2/21230/2017 M/s. Amoli Organics Pvt Ltd. Plot No.: 322/4, 40 Shed Area, GIDC Vapi Dist: Valsad, Gujarat.






• The MoEF&CC issued TOR to PP vide letter dated 23/08/2017.

• Project proponent has submitted EIA Report prepared by M/s: Eco Chem Sales & Services,

Surat based on the TOR issued by SEIAA.

• This is an existing unit engaged in Synthetic Organic Manufacturingand now proposes for


Sr. no

Name of the Products CAS no. / CI no.

Quantity (MT/Month) End-use of the products Existing Proposed Total

1 Diclofenac Sodium 15307-79-6 20.0 245 265 Pharmaceuti

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Page 31 of 80

&its Salts cal Drugs

Diclofenac potassium 15307-81-0

Diclofenac diethyl amine

78213-16-8

Diclofenc free acid 15307-86-5

Diclofenac Resinate 56187-47-4

Diclofenac Deonal NA

Diclofenac Appolomine

119623-66-4

2 Aceclofenac 89796-99-6 0.5 49.5 50

3 Clotrimazole 23593-75-1 1.0 9 10

4 Di Hydralazene Sulphate

7327-87-9 1.0 1.5 2.5

5 Bifonazole 60628-96-8 0.5 4.5 5

6 Norethisterone Acetate 0.25 -0.25 0

7 Oxcarbazepine 5.0 -5.0 0

8 Carbamazepine 1.0 -1.0 0

9 Sildenafil Citrate 0.5 -0.5 0

10 Pioglitazole 0.5 -0.5 0

11 Momiflumate 1.0 -1.0 0

12 Celecoxib 0.5 -0.5 0

13 CetrizeneDihydrocloride

0.1 -0.1 0

14 Sertaline Hydrochloride

0.5 -0.5 0

15 NoscapineResine Complex

0.05 -0.05 0

16 Nitroxaline 0.05 -0.05 0

17 Formasulphathiazole 1.0 -1.0 0

18 MentronidazoleBebzoate

1.0 -1.0 0

19 Ascorbic Acid 10.0 -10.0 0

20 Rofecoxib 0.20 -0.2 0

21 2 Chloro Ethyl Phenyl Ether

0.1 -0.1 0

22 Venlafaxine Hydrochloride

0.5 -0.5 0

23 Fexofenadine Hydrochloride

0.5 -0.5 0

24 CatalpidogrelHydrogensulphate

0.5 -0.5 0

25 Citalopram Hydrobromide

0.5 -0.5 0

26 Pyridoxine Acetonide Hydro Chloride

58-56-0 0 2.5 2.5

Total 46.75 288.25 335.0


Notification 2006



of 80


Page 32 of 80

project proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 30.2 Cr. Proposed: 10.05 Cr. Total: 40.2 Cr.

(1) Capital cost for EMS (Environmental Management System):4.2Crores

(2) Recurring cost towards the environmental protection measures:3.76Crores per Annum.


Existing: 7801Sq. m. Proposed: 0 Sq. m. (2030 m2 existing open area will be utilized) Total: 7801Sq. m. (Expansion will be within existing factory premises)


Existing: 1200Sq. m. Proposed: 1380Sq. m. Total: 2580Sq. m.


1. Direct Existing:50 Proposed:100 Total: 170

2. Indirect Existing: 10 Proposed:80-100 Total:90-100

D Water i


GIDC

Status of permission from the concern authority. Permission is obtained letter no. vide GIDC/DEE(W/S)NA/VAPI/177 on 23/05/2017.

ii Water consumption (KLD):

Existing KLD



Remarks

(A) Domestic 15 5 20

(B) Gardening 10 5 15

Industrial

Process& Washing

55 88 143 Processing and product washing

Washing 34 6 40

Floor/container/ equipment

Boiler 20 40 60

Cooling 20 55 75

Others 5 2 7 Scrubber

Industrial Total 134 201 325

Grand Total (A+B+C)

159 8.14 360

1) Total water requirement for the project: 360KLD


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Page 33 of 80

3) Total fresh water requirement: 360KLD





Remarks


Industrial

Process& Washing

60 109 169 Process and product washing

Washing 34 6.0 40.0 Equipment & Floor washing

Boiler 18.0 7.0 25.0

Cooling 10.0 0.0 5.0

Others 3.0 2.0 5.0 Scrubber(5.0 KLD)+ Condensate from MEE (14.94 KLD)


125 118 244 After Expansion (Normal effluent 151 KLD+ Concentrated 18 KLD+ Utilities 75 KLD) )

-

iv Treatment facility within premises with capacity (ETP, MEE, STP etc).

ETP will be modified to treat normal effluent of 240.94 KLD MVR to be provided to treat 18 KLD of Concentrated effluents.

v Mode of Disposal & Final meeting point Domestic: Soak Pit

Industrial: ETP &MVR


CETP: Vapi Green Enviro Ltd.

Membership of Common facility (CF) CETP – Vapi vide letter No. VGEL/Mem. Cor-BV/2017-18/0089 dated 02/05/2007

vii Reuse/Recycle details (KLD) --



-

Sr. no.

Source of emission

With Capacity e.g. Boiler (8

TPH)

Stack Height (meter

)

Name of the fuel

Quantity of Fuel

MT/hr & MT/Day

Type of emissions

i.e. Air Pollutants

APCM

Existing

1 Boiler (3 TPH)

31 Imported

coal 583

kgs/hr PM, SO2

NOx MDC & bag filter

Proposed

1 Boiler (8 TPH)

30 Imported

coal 972

kgs/hr PM, SO2

NOx ESP

2 D.G Set -1250 KVA

11 HSD 220

kgs/hr PM, SO2

NOx Chimney

-


of 80


Page 34 of 80

[Existing & Proposed]

Sr. no.

Source of emission

Type of emission


APCM

Existing

1 Reactor HCl, Cl&

SO2 11

Two stage graphite followed by alkali scrubber

Proposed

1 Reactor HCl, Cl&

SO2 11

Two stage graphite followed by alkali scrubber

iii Fugitive emission details with its mitigation measures. [Existing & Proposed].As below

[Existing & Proposed]

• All the joints, flanges, pumps, glands, seals, valves are/ will be maintained in good

conditions through timely predictive and preventive maintenance;

• Regular workplace monitoring will be carried out for HCl at various locations within

plant.

• Phase-wise development of green belt will be undertaken in which green belt will be

developed along with construction activity.

• All tanks being used for storage of odorous chemicals/ products will be connected to

vacuum system. The vacuum will be monitored on daily basis and actions will be taken

accordingly.

• All pumps handling hazardous chemicals shall be provided with mechanical seals to

prevent fugitive emission.

• Manual Handling of various chemicals will be avoided and will be designed by

implementing latest automation technology.

All venting system will have vapor recovery system

F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.[Existing & Proposed]

i

Sr. no.




Existing Quantity (MT/Annum)

Proposed Quantity (MT/Annum)

Disposal Method

1. Used oil D.G Sets & equipment maintenance

5.1 0.24 0.3 Is being/will be sent

to registered re-processors

2. Discarded

containers

Unloading of raw materials 33.1 30.0 50.0

Collection, Storage, Decontamination

3. Process

Residue &

waste

Manufacturing process 28.1 12.0 1200.9

Is being/will be sent to incinerator

4. ETP waste ETP

35.3 180 4900 Is being/will be sent

to TSDF

5. Spent Manufacturing process

28.2 48 192.0 Is being/will be sent for co-processing

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Page 35 of 80

Carbon to RSPL, Panoli

6 Spent solvent

Manufacturing process 28.6 20.0 622.764

Is being/ will be reuse within

industrial unit

7. Aluminum Chloride

Soln.

Manufacturing process SCH:

II, B10 1500 6264

Is being/ will be sale to authorized

unit through manifest system

8 Chemical

Sludge from high

COD

stream

Manufacturing process

35.3 6.6 0 Is being sent for

incineration

9 Used Glass wool

Manufacturing process Z-22 0.06 0.12

Is being/will be sent to TSDF

10 Salt from

MVR

MEE/ MVR 35.3 0 842

Will be dispose off into TSDF

11 Inorganic Acid (30%

HCl)

Manufacturing process Sch: II

B 15 0 2922

Will be sold to authorized users

12 KCl Powder

from process

Manufacturing process 28.1 0 744


13 NaCl from

process

Manufacturing process 28.1 0 272



ii Membership details of TSDF, CHWIF etc.

• TSDF SEPPL, Kutch Membership No. 1200001191

• CSWP, Vapi Membership No. 105

• RSPL membership for co-processing: CPAW1A0012


Fly Ash from Boiler Existing : 145 TPA Proposed: 243 TPA Mode of disposal: Will be sent to brick making industries MSW: Municipal solid waste generated would include kitchen waste, cardboards, papers, plastics and garden waste. Cardboard, papers and plastic wastes will be handed over to scrap dealers and kitchen & garden waste is/ will be sent to the nearest municipal waste collection site



Solvent Stripper is/will be installed for solvent recovery.

Solvent Name

Kg/Month Overall

% Recovery Input Recovered Consumed Loss

of 80


Page 36 of 80

Toluene 376690 361625 0 15065 96.00

Methanol 50065 47815 0 2250 95.51

N-N Di Methyl Aniline

61 552 0 61 94

Formic Acid 180 1699.19 0 180 95.7

Acetone/ Ethyl Acetate

162133 156465 469 5198 96.79

IPA 989.3 637.11 876.9 112.4 60


Source:

• Process Reactor

• Raw material Handling & Storage Mitigation Measures:

• The raw materials will be stored in closed containers and will be handled through closed system to avoid the handling losses

• Reactor and solvent handling pumps will have mechanical seals to prevent leakages. Reactors shall also be provided with breather valve to prevent losses.

• Solvent Stripper is/will be installed for solvent recovery to minimize VOC emission.

The project proponent along with their experts/consultants attended the meeting of the SEAC held on

15/03/2018. During the meeting, the project was appraised based on the information furnished in the

EIA Report, details presented before the committee. Technical presentation made during the meeting

by project proponent. EIA report reveals that baseline environmental study was carried out during the

month of March 2017 to May 2017 to determine the prevailing status of ambient air, land use, noise

level topography, meteorology, ecology & socioeconomic outline and additional one month in October

2017 for ambient air. Baseline ambient air quality was measured at eight locations. Monitoring was

carried out for PM10, PM2.5, SO2, NOx, CO, Cl2 and HCl within 10 km radius from the project site.

The maximum concentrations of PM10, PM2.5, SO2, NOx, CO, Cl2 and HCl at each ambient air

monitoring locations were compared with NAAQS for industrial, residential, rural and other areas.

Concentration of PM10 ranged from 68.4 µg/m3 to 95.4 µg/m3. Concentration of PM2.5 recorded

from minimum 36.0 µg/m3 to maximum 52.9 µg/m3. Concentration of SO2 recorded ranged from

minimum 9.7 µg/m3 to maximum 22.0 µg/m3. Concentration of NO2 recorded ranged from minimum

15.1 µg/m3 to maximum 32.8 µg/m3.Concentration of CO recorded ranged from minimum 350 µg/m3

to maximum 710 µg/m3.Concentration of Cl2 recorded ranged from minimum 0.4 µg/m3 to maximum

2.4 µg/m3.Concentration of HCl ranged from BDL to 9.2 µg/m3. The incremental Ground Level

Concentration (GLC) has been computed using ISC-AERMOD View” by Lakes Environmental,

Canada. The maximum 24-hourly average ground level concentration for pollutant due to proposed

project calculated using mathematical model (ISCST3) for PM10, SO2, NOx and resultant values also

of 80


Page 37 of 80

meets with NAAQ standards. Committee observed that PP has proposed ESP for proposed Boiler.

Unit has proposed two stage graphite followed by alkali scrubber for reactor to control HCl, Cl& SO2.

The total industrial water consumption will be 360 KLD; which will be sourced from GIDC. The

industrial wastewater generation will be 244 KLD. The concentrated effluent of 18 KLD will be treated

in MVR and other wastewater will be treated in ETP and discharged into the CETP, vapi. The

domestic wastewater generation will be 17 KLD. The domestic wastewater will be disposed of

through Soak pit/septic tank.

Committee noted that proposal is falling under 5(f). Committee noted that this is a proposal for

expansion and asked PP for compliance of existing conditions of CCA, certified compliance report of

EC by ZO, MOEF&CC, Bhopal, details of public complaints/public litigation if any and action initiated

by the GPCB against the industrial unit which was satisfactorily replied by the PP.

Committee noted that existing waste water generation is 125 KLPD and after proposed expansion,

total waste water generation will be 224 KLPD. Break up of waste water generation is normal effluent

151 KLD, Concentrated effluent 18 KLD, effluent from Utilities 75 KLD. Committee asked PP not to

discharge additional waste water load to CETP instead pursue zero liquid discharge which is agreed

by the PP.PP mentioned that additional quantity of waste water will be made under zero liquid

discharge scheme by passing waste water through MVR followed by RO. For prevention of release of

VOC in the ambient air, PP is asked to address leak detection and repairing programme. Committee

deliberated on air pollution control measures for flue gas and process emission, hazardous waste

generation and management and risk assessment based on worst case scenario and found all the

TORs are addressed satisfactorily

After detailed deliberation PP was asked to submit the following details and upon submission, it was

decided to consider the proposal in one of the upcoming SEAC meeting.

1. Revised project details mentioning corrected water consumption, waste water generation,

existing consented waste water discharge quantity to CETP.

2. Proposal for making additional load of waste water under zero liquid discharge by pursuing

MVR followed by RO with details of techno-feasibility and adequacy of the said installations.

3. Detailed Leak Detection and Repairing Programme (LDAR)for all the volatile organic solvents

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.

• Project proponent submitted reply vide their letter dated 19/04/2018. PP has submitted as

below:

� Revised details with correction of water consumption and wastewater generation, existing

consented wastewater discharge quantity to CETP are submitted.

� Details with techno-feasibility and adequacy of the MVR followed by RO for making additional

load of wastewater under Zero liquid Discharge.

� Detailed LDAR for all the VOC is submitted.

of 80


Page 38 of 80

During the meeting dated 09/08/2018, Committee considered this proposal and reply submitted by PP

found satisfactory.

Compliance of the ToR was found satisfactory.

After detailed discussion, it was decided to recommend the project to SEIAA Gujarat for grant

of Environmental Clearance.

5. SIA/GJ/IND2/17964/2016 M/s. Bhagawati Organics Pvt Ltd. Plot no. 479, Phase-II, GIDC, Vatva, Ahmedabad

Reconsideration EC





• The SEAC had recommended TOR to SEIAA and SEIAA issued TOR to PP vide letter dated

24/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: SAN EnvirotechPvt Ltd.,

Ahmedabad based on the TOR issued by SEIAA.

• This is an existing unit engaged in Metallurgical industries and now proposes for expansion 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 Napthol ASG 91-96-3 10 0 10 In Pharmaceutical industry

2 O. T. Base 119-93-7 10 0 10 Raw material for Dyes and Dye Intermediate Unit

3 Sodium Format (By Product)

141-53-7 3 0 3 Raw material for Pharma Bulk Drug Industry

4 Di Methyl Amino Ethyl Chloride HCL

4584-46-7

15 0 15

Raw material for Pharma Bulk Drug Industry

5 2-Chloro Ethylamine Hydrochloride

870-24-6 Raw material for Pharma Bulk Drug Industry

6 Bis (2-Chloro Ethyl) Amine Hydrochloride

821-48-7 Raw material for Pharma Bulk Drug Industry

7

Sodium Bi Sulphite/Sodium Sulphite (By Product)

7631-90-5 3.5 0 3.5 Raw material for Pharma Bulk Drug Industry

8 1-(4-Methoxy Phenyl)Piperazine


9 1-(2,3-Dichloro phenyl) Piperazine. HCl

119532-26-2

0 10 10 Raw material for Pharma Bulk Drug Industry

10 1-(3- 6640-24-0 0 10 10 Raw material for

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Page 39 of 80

chlorophenyl)Piperazine

Pharma Bulk Drug Industry

11

N Acetyl 4(4-Hydroxy Phenyl) Piperazine


12 Glimepride 93479-97-1 0 3 3 Raw material for Pharma Bulk Drug Industry

13 Aripiprazole 129722-12-

9 0 3 3


14 Telmisartan 144701-48-

4 0 5 5


15 Omeprazole Sulphide


TOTAL 41.5 76 117.5


Notification 2006



project proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 0.71 Crores Proposed: 1.79 Crores Total: 2.5 Crores

(3) Capital cost for EMS (Environmental Management System): 0.315 Crores

(4) Recurring cost towards the environmental protection measures: 0.203 Crores per

Annum.


Existing: 2775 Sq. m. Proposed: 0 Total: 2775 Sq. m.




Direct Existing:16 Proposed:17 Total:33

Indirect Existing: 15 Proposed:15 Total:30

D Water

of 80


Page 40 of 80

i


GIDC Bore well

Status of permission from the concern authority. Yes


Existing KLD



(D) Domestic 1 0.5 1.5

(E) Gardening -- 1 1

Industrial

Process 2.05 16.95 19

Washing 1.2 1.8 3

Boiler 2.25 2.75 5

Cooling 2 1 3

Scrubber 0.5 -- 0.5

Industrial Total 8 22.5 31.5

Grand Total (A+B+C)

9 24 33

Total water requirement for the project: 33 KLD

Quantity to be recycle: No recycle

Total fresh water requirement: 33 KLD





(C) Domestic 0.6 0.3 0.9

Industrial

Process 2.75 30.2 32.95

Washing 1.2 1.8 3

Boiler 0.25 0.25 0.5

Cooling -- 0.03 0.03

Scrubber -- -- --


4.2 32.3 36.5

-

iv Treatment facility within premises with capacity (ETP,MEE, STP etc).

ETP


Domestic: 0.9 KLD_ Soak pit via Septic Tank

• Industrial: Afterproposedexpansion,totalindustrialeffluentgenerationwillbe36.5KLPD.Itwillbe segregated as follows:

HighConcentratedEffluent:[email protected] senttoETPforPrimarytreatmentandthenitwillbesenttoSocietyforCleanEarth,

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Page 41 of 80

Vatvaforspraydryingcompletely.

LowConcentratedEffluent:Lowconcentratedprocesseffluent,Cooling,Washingand [email protected],SecondaryandTertiary treatment and then it will be CETP Vatva for further treatment and disposal.


Common CETP – The Green Environment Services Co-op. Society Ltd. Common Spray Dryer – Society For Clean Earth

Membership of Common facility (CF) The Green Environment Services Co-op. Society Ltd. – For CETP Society For Clean Earth – For Spray Drye

vii Reuse/Recycle details (KLD) -



Sr. no.

Source of emission

With Capacity e.g. Boiler (8

TPH)


Name of the fuel


Type of emissions

i.e. Air Pollutants

APCM

1 Steam Boiler

(0.6 TPH) (Existing)

11

Agro Waste based

fuel

0.1 SPM SO2

NOX No

2

Hot Air Generator

(1 Lakh k Cal/hr.) (Existing)

Agro Waste based

fuel

0.1 SPM SO2

NOX No

3 Boiler

(1 TPH) (Proposed)

11 Bio

Coal 0.8

SPM SO2

NOX No

4

Thermic Fluid Heater

(6 Lakh k Cal/hr.) (Proposed)

11 Bio

Coal 0.1

SPM SO2

NOX No

-


-

Sr. no.

Source of emission

Type of emission



1 Reaction Vessel

SO2

NOx 11

Two Stage Alkali Scrubber

40 mg/Nm3

25mg/Nm3

-

iii Fugitive emission details with its mitigation measures. [Existing & Proposed]..As below

Measures taken for fugitive emission control:

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Page 42 of 80

• Proper storage of raw materials, products and fuels.

• Ensuring closed feeding and sampling.

• Establishing SOPs for start-up, shut down and maintenance operational procedures.

• Regular work place monitoring and ambient air quality monitoring as per post project

monitoring plan.

• Pneumatically transfer of raw material in reactor.

• PPE will be provided to the workers working in process area.

• Greenbelt will be developed around the plant to arrest the fugitive emission.

• Paved road will make to reduce the fugitive emission. Water sprinkler will be provided to

reduce the


i

Sr. no.

Type/Name of Hazardous

waste


Category and

Schedule as per

HW Rules.

Quantity MT/Annum

Disposal Method

1 ETP Sludge Effluent Treatment Plant

35.3 84

Collection. Storage, Transportation, Disposal at TSDF site.

2 Used Oil Lubrication Plant Machinery

5.1 12

Collection. Storage, Transportation & Disposal by selling to Registered Recycler or reused as lubricant in plant.

3 Discarded containers

Raw Material Section

33.1 2.5

Collection. Storage, Decontamination, Transportation & Disposal To authorized recycler or return back to suppliers.

4 Process (Carbon) Waste


-- 24 Collection. Storage, Transportation, Disposal at CHWIF Site

5 Sodium Format Manufacturing Process of O. T. Base

-- 36

Collection. Storage, Transportation & sell to Rule 9 authorized industries.

6 Sodium Bi Sulphite/Sodium Sulphite

Manufacturing Process of O. T. Base

-- 42

Collection. Storage, Transportation & sell to Rule 9 authorized industries.


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Page 43 of 80

ii Membership details of TSDF, CHWIF etc. SaurastraEnviro Project Pvt. Ltd. – For TSDF & CHWIF


NA



Sr. No.

Product Name

MT/Batch

Solvent Name

Solvent Use

Recovery Consume in product

Recover in %

1 Napthol ASG Ortho

Xyelene 5 4.9 0.1 98

2 O. T. Base Methanol 2.24 2.18 0.06 97.3

3 Di Methyl Amino Ethyl Chloride HCL

EDC 1 0.93 0.07 93 4 2-Chloro Ethylamine Hydrochloride

5 Bis (2-Chloro Ethyl) Amine Hydrochloride

6 1-(4-Methoxy Phenyl)Piperazine

Methanol 3 2.8 0.2 93

7 1-(2,3-Dichloro phenyl) Piperazine.HCl

o-Xylene 0.174 0.165 0.009 94.8

IPA 0.25 0.24 0.01 96

8 1-(3-chlorophenyl)Piperazine

Toluene 1 0.95 0.05 95

9 N Acetyl 4(4-Hydroxy Phenyl) Piperazine

Methanol 1.52 1.35 0.17 88.8

10 Glimepride

Acetone 6.24 5.9 0.34 94.5

methanol 12 11.5 0.5 95.8

Ethyl Acetate

1 0.95 0.05 95

Acetonitrile 1 0.95 0.05 95

11 Telmisartan DMF 3.714 3.51 0.2 94.5

Methanol 9.86 9 0.86 91.3

12 Omeprazole Sulphide

Methanol 3 2.79 0.21 89.5

Toluene 13 12.13 0.87 93.3

Hexane 0.5 0.47 0.03 94


Sources of VOC emission will be Liquid Raw material storage Area and production area. To mitigate the VOC emission unit will handle the liquid raw material by pumping system directly from Barrel to Reaction vessel. Unit ensure that there will be no any kind of leakages or spillages in the unit

• The project proponent along with their experts/consultants attended the meeting of the SEAC

held on 07/03/2018. During the meeting, the project was appraised based on the information

furnished in the EIA Report, details presented before the committee. Technical presentation

made during the meeting by project proponent. EIA report reveals that baseline environmental

study was carried out during the month of March 2017 to May 2017 to determine the

prevailing status of ambient air, land use, noise level topography, meteorology, ecology &

socioeconomic outline. Baseline ambient air quality was measured at eight locations.

of 80


Page 44 of 80

Monitoring was carried out for PM10, PM2.5, SO2, NOx, HC, CO and VOC within 5 km radius

from the project site. The maximum concentrations of PM10, PM2.5, SO2,NOx, HC, CO and

VOC at each ambient air monitoring locations were compared with NAAQS for industrial,

residential, rural and other areas. Concentration of PM10 ranged from 65.66µg/m3 to

87.67µg/m3. Concentration of PM2.5 recorded from minimum 30.41µg/m3 to maximum

42.39µg/m3. Concentration of SO2 recorded ranged from minimum 16.23µg/m3 to maximum

25.50µg/m3. Concentration of NO2 recorded ranged from minimum 30.03µg/m3 to maximum

52.76µg/m3.Concentration of HC recorded ranged from minimum 5.28µg/m3 to maximum

9.12µg/m3.Concentration of CO recorded ranged from minimum 315.71µg/m3 to maximum

493.82µg/m3. Concentration of Benzene ranged from 0.76µg/m3 to 1.16µg/m3.Concentration

of Toluene ranged from 2.61µg/m3 to 3.36µg/m3.Concentration of Xylene ranged from

0.97µg/m3 to 1.54µg/m3.The incremental Ground Level Concentration (GLC) has been

computed using ISC-AERMOD View” by Lakes Environmental, Canada. The maximum 24-

hourly average ground level concentration for pollutant due to proposed project calculated

using mathematical model (ISCST3) for PM10, SO2, NOx and resultant values also meets

with NAAQ standards.

• Technical presentation was made by the project proponent. Committee noted that proposal is

falling under 5(f). Committee noted that this is a proposal for expansion and asked PP for

compliance of existing conditions of CCA, details of public complaints/public litigation if any

and action initiated by the GPCB against the industrial unit which was replied by the PP.

Committee asked PP to submit certified compliance report of EC condition from GPCB as per

the circular dated 07/09/2017 vide letter of J-11013/6/2010-IA-II(Part)Committee note that

high concentrate process effluent @32.3KLD will be sent to ETP for Primary treatment and

then it will be sent to Society for Clean Earth, Vatva for spray drying completely. It is further

mentioned that Unit is having existing CCA for 4.20 KLPD of treated waste water disposal to

CETP which will be maintained. Low concentrated process effluent from Cooling, Washing

and Boiler of quantity 4..2 KLD will be sent to ETP for Primary, Secondary and Tertiary

treatment and then it will be CETP Vatva for further treatment and disposal as per CCA.

Committee deliberated on air pollution control measures for flue gas and process emission,

hazardous waste generation and management and risk assessment based on worst case

scenario and found all the TORs are addressed satisfactorily

• After detailed deliberation PP was asked to submit the following details and upon submission,

it was decided to consider the proposal in one of the upcoming SEAC meeting.

1. Certified compliance report of Environmental Clearance conditions from ZO,MoEF&CC,

Bhopal /GPCB as per the circular dated 07/09/2017 vide letter of J-11013/6/2010-IA-

II(Part).

2. Detailed Leak Detection and Repairing Programme (LDAR)for volatile organic solvents

proposed in house with detailed chemical properties including vapor pressure. LDAR

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Page 45 of 80

shall endeavor prevention of losses of solvents to the best minimum extent.

• PP has submitted reply vide their letter dated 30/07/2018.

• PP has submitted details regarding LDAR programme.

• This office has also received Certified Compliance Report (CCR) from the Member Secretary,

GPCB vide letter no. GPCB/DOC/VT/June-1/2018/525 dated 03/07/2018.

• During the meeting dated 09/08/2018, Committee considered this proposal. Committee

observed that following EC conditions are non-compiled.

Sr. no

as per

EC

Condit

ion

Description of Conditions Remarks as per

the CCR

A.

xv.

The Company Shall undertake Eco Developmental Measure

Including Community Welfare Measure in the Project Area for the

Overall Improvement of the Environment. The eco-development

plan may by submitted to the SPCB

Not complied

B.

ii.

No Further expansion or modifications in plant shall be carried out

without prior approval of the Ministry of Environmentand Forests. In

case of deviations or alteration in the project proposal from those

submitted to the ministry for clearance, a fresh reference and to

add additional environment protection measure required, if any

Partly complied

B.

viii.

The project authorities shall earmark separate fund to implement

the conditions stipulated by the ministry of Environment and

Forests as well as the state Government along with the

implementation and forests as well as the state Government along

with the implementation Schedule for all the conditions stipulated

herein the funds so provided shall not be diverted for any other

purpose.

Not complied

• Looking to the content of the non-complied conditions, Committee felt that project proponent

shall remain present during discussion of the said non-complied / Partially complied conditions

of CCR.

In view of the above, Committee decided to consider the proposal in one of the upcoming

SEAC meetings only after submission of the satisfactory reply or the above mentioned non-

complying conditions.

6. SIA/GJ/IND2/18797/2017 M/s. Dev pharma Chem Plot No. 109/7 (old no), 257 (new no), Ravi Industrial Estate, Bileshwarpura, Chhatral, Kalol, Gandhinagar.



Project status: New



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Page 46 of 80


30/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: Green Circle Inc, Vadodara

based on the TOR issued by SEIAA.

• This is a new unit proposes for Synthetic Organic manufacturing as tabulated below:

Sr. No.


CAS no.

Quantity MT/Months

End-use of product

1 Para Anisic Aldehyde (PAA)

794-94-5

50 MT/Month Apply as a flavour fragrance and as a raw material

2 OctylMethoxyCinnamate (OMC)

5466-73-3

25 MT/Month Apply as sunscreen and other cosmetics to absorb UV rays from the sun

3 Octyl Salicylate 118-60-5

5 MT/Month Apply as sunscreen and other cosmetics to absorb UV rays from the sun and antibacterial

4 Homosalate 118-56-90

5 MT/Month Apply as sunscreen and skincare

Total 85 MT/Month


Notification 2006



project proponent.


Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 3.50 Crores

1. Capital cost for EMS (Environmental Management System): 32 Lacs

2. Recurring cost towards the environmental protection measures:2-3 Lacs per Annum.

B Total Plot area ( sq. meter) 3204 Sq. m.

Green belt area,/Tree Plantation area ( sq. meter) 1100 Sq. m.


1. Direct

2. Indirect

D Water

i


Ravi Industrial Estate Supply

Status of permission from the concern authority. Enclosed

ii Water consumption (KL/day) : 5.0

Category

KL/day Remarks

(F) Domestic 1.0 -

(G) Gardening 0.5 -

(H) Industrial

Process 0.2 -

Washing 0.3 -

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Page 47 of 80

Boiler 2.0 -

Cooling 1.0 -

Industrial Total 3.5 -

Total (A + B + C)

5.0 -


2) Quantity to be recycle: KLD


iii Waste water generation (KL/day)

-

Category KL/Day Remarks

(D) Domestic 0.8 Discharged to Soak pit

(E) Industrial

Process 0.308 Treated in in house ETP & the entire treated effluent evaporated in evaporator in premises or Send to the Common Spray Dryer Facility of Chhatral Enviro Management System Pvt. Ltd.

Washing 0.3

Boiler/Cooling 0.102

Others 0.0


0.710

-

iv Treatment facility with capacity (ETP, CETP, MEE, STP, Spray Dryer etc).

ETP and Evaporator In house having Capacity: 1.0 KL/day & Taken membership of Common Spray Dryer Facility of Chhatral Enviro Management System Pvt. Ltd.


Domestic: Soak Pit

Industrial: Zero Discharge

vi Reuse/Recycle details (KL/day) 0.5 KL/Day

E Air


-

SR. no.

Source of emission With Capacity


Type of Fuel



Air Pollution Control Measures (APCM)

1

Steam Boiler (IBR 1.5 MT)

13 m

White Coal/Agro Waste

2.0 MT/day

PM SO2 NO2

Multi Cyclones and Bag filter

2

Thermic Fluid Heater-1 (2 Lacs Kcal)

13 m

F.O./L.D.O

1.2 MT/day

PM SO2 NO2

-

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Page 48 of 80

3

Thermic Fluid Heater- 2 (2 Lacs Kcal)

13 m

F.O./L.D.O

1.2 MT/day

PM SO2 NO2

-

4 D.G. Set 125 KVA

5 m

Diesel

0.8 KL/day

PM SO2 NO2

Adequate Stack Height

-


There is no process gas.

v Fugitive emission details with its mitigation measures.

F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.

i

Sr. no.

Type of Hazardous waste



Quantity (MT/Annum)

Disposal Method

1 ETP Sludge Effluent Treatment Plant

34.3 6.0 Collection, Storage, Transportation, Disposal at TSDF site.

2 Carbon Waste



3 Evaporation Residue

Evaporator


4 Distilled Residue


36.4 2.2 Collection, Storage, Transportation, Disposal at CHWI site.

5 Used oil/spent oil


5.1 1.92 Collection, Storage, & use as lubricant in machineries

6 Discarded Container & Bags

Raw material Section

33.3 12.0 Collection, Storage, Transportation, sold to Registered Recycler or Reuse in Premises.


ii Membership details of CETP, TSDF, CHWIF, Common MEE, Common Spray Dryer etc.

TSDF membership will be taken before CTE fresh. Common Spray Dryer Facility of Chhatral Enviro Management System Pvt. Ltd.

ii Details of Non-Hazardous waste & its disposal(MSW and others)

Kalol Collection Centre

G Solvent management (If any)

i Details of Solvent recovery (As per respective ToR)

NA


Control of VOCs and fugitive Emissions:

• Sampling points will be provided with double

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Page 49 of 80

valve followed by suction hoods which will be

connected to ducting system leading to

scrubbing system.

• Odour causing raw materials will be charged

in closed chambers with exhaust of

chambers connected to ducting system

leading to scrubbing system.

All waste storage tanks and waste preparation and raw material storage tanks will be connected to vacuum system

The project proponent along with their experts/consultants attended the meeting of the SEAC held on

08/03/2018. During the meeting, the project was appraised based on the information furnished in the

EIA Report, and details presented before the committee. Technical presentation made during the

meeting by project proponent. EIA report reveals that baseline environmental study was carried out

during the month of March 2017 to May 2017 to determine the prevailing status of ambient air, land

use, noise level topography, meteorology, ecology & socioeconomic outline. Baseline ambient air

quality was measured at Eight locations. Monitoring was carried out for PM10, PM2.5, SO2, NOx, HCl

and VOC within 10 km radius from the project site. The maximum concentrations of PM10, PM2.5,

SO2 NOx, HCl and VOC at each ambient air monitoring locations were compared with NAAQS for

industrial, residential, rural and other areas. Concentration of PM10 ranged from 50 µg/m3 to 66

µg/m3. Concentration of SO2 recorded ranged from minimum 9 µg/m3 to maximum 24 µg/m3.

Concentration of NO2 recorded ranged from minimum 18 µg/m3 to maximum 40 µg/m3.

Concentration of HCl recorded ranged from minimum 6 µg/m3 to maximum 100 µg/m3. Concentration

of VOC recorded ranged from minimum 0.1 µg/m3 to maximum 0.35 µg/m3. Concentration of all the

parameters are well within the NAAQS for industrial, residential, rural and other areas except for PM10

at Suva and Jolva villages. The incremental Ground Level Concentration (GLC) has been computed

using ISC-AERMOD View” by Lakes Environmental, Canada. The maximum 24-hourly average

ground level concentration for pollutant due to proposed project calculated using mathematical model

(ISCST3) for PM10, SO2, NOx and resultant values also meets with NAAQ standards . Committee

observed that PP has proposed Multi cyclone and bag filter for steam boiler. There will not by any

generation of process gas from the proposed project. Total water consumption of proposed project

will be 5 KLD which will be sourced from Ravi industrial estate supply. Total industrial wastewater

generation will be 0.710 KLD, which will be treated in ETP and evaporated in MEE. Generated

domestic wastewater of 0.8 KLD will be collected and treated in septic tank. While discussing about

the safety aspects of proposed project, Committee put emphasis on process hazard in the

manufacturing process of Para MethoxyPhenyl Acetonitrile. Handling of hazardous chemicals like H2,

Sodium cyanide etc. have been discussed in detail. Looking to the process hazard of said product,

PP informed that they will remove the product from the proposed project and submit the revised

details in this regard. PP has not shown management of waste streams like glaubar salt, Na2SO3,

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Page 50 of 80

MnSO4 etc. Committee observed that PP has proposed Zero Liquid Discharge by in-house ETP, RO

& Evaporator. However, PP could not justify adequacy of ZLD with reference to characteristics of the

waste water.

After deliberation, it was unanimously decided to consider the project for further

consideration only after submission of the following:

1) Revised details/information w.r.t. change in product profile i.e. removal of product namely

Para Methoxy Phenyl Acetonitrile.

2) Adequacy of ZLD considering worst case scenario & stage wise characteristics of effluent.

3) Hazardous waste management of all type of waste streams as per the HW Rules 2016.


� Unit has decided to remove manufacturing of the product Para Methoxy Phenyl Acetonitrile

(PAMPA) and necessary changes in product list, raw material quantity, manufacturing

process, water consumption, wastewater generation and hazardous waste management

accordingly.

� Adequacy for ZLD considering worst case scenario & stage wise characteristics of effluent is

submitted.

� Hazardous waste management is resubmitted with all type of waste streams considering as

per the HW Rules 2016.


found satisfactory.




7. SIA/GJ/IND2/18859/2017 M/s. Sun Pharmaceutical Industries Ltd. Plot no. 4708, GIDC Estate, Ankleshwar, Dist: Bharuch






• SEAC has recommended TOR to SEIAA and SEIAA has issued TOR to PP vide letter dated

30/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: Jyoti Om Chemical Research

Centre Pvt. Ltd. based on the TOR issued by SEIAA.

• This is an existing unit engaged in Synthetic Organic Chemicals and now proposes for


Sr. no.

Name of the Products CAS no. / CI no.

Quantity MT/Month

End-use of the products


GROUP-1 Any product not more than 50 MT/Month

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Page 51 of 80

1 Efaverinz 154598-52-4 0.1

50 MT/ MONTH (either

or)

50 MT/ MONTH (either

or)

Anti-viral

2 Glimepiride 93479-97-1 0.05 Anti-Diabetic

3 Carvedilol 72956-09-3 0.1 Anti-hypertensive

4 Ropinirol 91374-21-9 0.025 Anti-parkinsonian agent

5 ClomipmmineHCl 17321-77-6 0.25 Anti-depressant

6 Clonazepam Stage-III 1622-61-3 0.05 Anti-conversant

7 Rosiglitazone Maleate 155141-29-0 0.05 Anti-Diabetic

8 Topiramate 97240-79-4 0.1 Anti-conversant

9 Mosapride Citrate 112885-42-4 0.05 Gastroprokinetic

10 Mirtazapine 61337-67-5 0.05 Anti-depressant

11 Rofecoxib 162011-90-7 0.5 Anti-imflammatory

12 Sildenafil Citrate 171599-83-0 0.025 Anti-hypertensive

13 Pentoxifylline (Oxpentifylline)

6493--05—6 4.166 Hemorheologic agent

14 Sertraline 79559-97-0 0.1 Anti-depressant

15 Tizanidine 64461-82-1 0.1 Muscle Relaxant

16 Irbesartan 138402-11-6 0.25 Anti-hypertensive

17 Gabapentin 60142-96-3 0.3 Anti-epileptic

18 Oxcarbamazepine 28721-07-5 1 Anti-epileptic

19 Desloratidine 100643-71-8 0.1 Anti-hystaminic

20 Metazolone 1665-48-1 0.05 Muscle Relaxant

21 Flurbiprofen 5104-49-4 0.05 Anti-inflammatory

22 Theobromine 83-67-0 9.166 Diuretic

23 Azatadine 3978-86-7 0.25 Anti-hystaminic

24 Metoprolol Tartrate 56392-17-7 2.25 Anti-hypertensive

25 Acamprosate Calcium 77337-73-6 00 Alcoholism Treatment

26 Agomelatine 138112-76-2 00 Anti-depressant

27 Eslicarbazepine Acetate 236395-14-5 00 Anti-epileptic

28 Dapoxetine Hydrochloride

129938-20-1 00 Anti-depressant

29 Escitalopram Oxalate 219861-08-2 00 Anti-depressant

30 Dothiepin Hydrochloride 897-15-4 00 Anti-

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Page 52 of 80

depressant

31 Dobutamine Hydrochloride

49745-95-1 00 Cardiac drug

32 Edaravone 89-25-8 00 Anti-oxidant

33 Flupirtine Maleate 75507-68-5 00 Anti-parkinsonian agent

34 Lacosamide 175481-36-4 00 Anticonvulsant

35 Levosulpiride 23672-07-3 00 Antagonist

36 MetoprololSuccinate 37350-58-6 00 Anti-hypertensive

37 Modafinil 68693-11-8 00 CNS Stimulant

38 Olopatadine Hydrochloride

113806-05-6 00 Anti-histaminic

39 QuetiapineFumarate 111974-72-2 00 Anti-psychotic

40 Tofisopam 22345-47-7 00 Anxiolytic

41 Venlafaxine Hydrochloride Stage- I


42 Duloxetine Hydrochloride Stage-III


43 Atomoxetine Hydrochloride Stage-III


44 ImatinibMesylate Stage-III

220127-57-1 00 Anti-cancer

45 Zolpiden Tartrate Stage-II

99294-93-6 00 Sedative

46 Citalopram Hydro bromide Stage-I and II

59729-32-7 Anti-depressant

47 ClopidagrelBisulphate 120202-66-6 00 Anti-thrombotic

TOTAL (Sr No:-1 to 47) 50 MT/Month

GROUP-2 Each product is 15 MT/Month

48 Carbamazepine 298-46-4 00 15 30 MT/ MONTH

49 Lithium Carbonate 554-13-2 00 15

TOTAL(Sr. No:-48 to 49) 30 MT/Month

GROUP-3 Each product is 2 MT/Month

50 Synthetic R&D organic product

--- 00 2 4MT/ MONTH

51 Synthetic R&D Inorganic product

--- 00 2

TOTAL (Sr. No:-50 to 51) 4 MT/Month

TOTAL(Sr. No:-1 to 51) 84 MT/Month

Power Generation ---

775 KWH

589 KWH

1364 KWH

In-House


Notification 2006.

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Page 53 of 80



Sr. no.

Particulars Details


(Rs. in Crores):

Existing : 40Crores Proposed:26.10 Crores Total:66.10Crores

(5) Capital cost for EMS (Environmental Management System):13Crores

(6) Recurring cost towards the environmental protection measures: 2.7Crores per

Annum.

B Total Plot area

( sq. meter)

Existing: 24000Sq. m.

Proposed:0

Total: 24000Sq. m.


( sq. meter)

Existing: 2625.15Sq. m.

Proposed: 0

Total:2625.15 Sq. m.


1. Direct Existing:233 Proposed: 41 Total:274

2. Indirect Existing: 230 Proposed: 0 Total:230

D Water

i


GIDC water supply

Status of permission from the concern authority.

Unit is having 380 KLD water consumption permission as per Consent No.AWH-73116


Existing KLD



Remarks

(A) Domestic 30 0 30 Fresh

(B) Gardening 10 0 10 Fresh

(C) Industrial

Process 80 50 130 105 Fresh + 25 Recycle

Washing 47 -39 8 Fresh

Boiler 53 22 75 Fresh

Cooling 160 101 261 145 Fresh + 116 Recycle

Others --- --- ---

Industrial Total 340 134 474 333 Fresh + 141 Recycle

Grand Total (A+B+C) 380 134 514 373 Fresh + 141 Recycle

Note: Existing water consumption is as per actual consent taken before ZLD consent.

1) Total water requirement for the project:514KLD

2) Quantity to be recycle:141KLD

3) Total fresh water requirement: 373KLD

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Page 54 of 80

iii

Waste water generation (KLD)




Remarks


(B) Industrial

Process 65 35 100

Washing 8 00 8 Floor washing

Boiler 6 4 10

Cooling 20 13 33

Others 0 0 0


101 50 151

Total waste water (A+B)

131 39 170

- Note: Existing waste water generation is as per actual consent taken before ZLD consent.

iv Treatment facility within premises with capacity(ETP,MEE, STP etc).

ETP : 200 KLD MEE : 150KLD


Domestic: STP to ETP to RO & MEE and reuse

Industrial: TO ETP to RO & MEE and reuse


Unit is adopted ZLD.


Unit has also obtained membership of ETL for sending

Ammonical Nitrogen and of ACPCL/BEIL for sending

effluent in case of breakdown/maintenance of MEE.

Necessary permission from GPCB is also obtained.

The membership certificates and GPCB permission is

Attached as Annexure-XXXII.

vii Reuse/Recycle details (KLD) 141 KLD



-

Sr. No.

Stack Attached To

Stack Height(m)

Type of Fuel

APCM Type of Emission

Permissible Limit

AS PER CCA No:-AWH-73116

1. Smock Boiler (3 TPH)

30 Natural gas

Adequate stack height

PM SO2

NOX

150mg/NM3

100 PPM 50 PPM

2. Boiler (WHRB)

30 Natural gas

3. Smock Boiler (3 TPH)*

30 Natural gas

Proposed Expansion

4. Boiler (6 TPH)

30 Natural gas/ Furnace oil

Adequate stack height

PM SO2

NOX

150mg/NM3

100 PPM 50 PPM

5. DG Set (1500 KVA) 30 Diesel

Acoustic Encloser

-Unit is dismantle Smock boiler*3 TPH and install Boiler 6 TPH.

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Page 55 of 80


-

Sr. No. APCM attached to

Stack Height

APCM Pollutant Remarks

Existing

1. Reaction Vessel

22 Water + Acid Scrubber

NH3 175 mg/NM3

2. Reaction Vessel

12 Water + Alkali Scrubber

HCl 20 mg/NM3

For Proposed Expansion

3. Reaction Vessel


NH3 175 mg/NM3

4. Reaction Vessel


NH3 175 mg/NM3

5. Reaction Vessel


HCl 20 mg/NM3

6. Reaction Vessel


HCl 20 mg/NM3

-Unit will attach individual scrubber and stack to individual reactor.

iii Fugitive emission details with its mitigation measures. [Existing & Proposed].As below

FUGITIVE EMISSION

1 Solvent storage tank

Air pollutant (VOC)

i) Carry out work place area monitoring to find out concentration level in ambient air.

ii) Provision of breather valve cum flame arrester.

2 Solvent recovery system

Air pollutant (VOC)

i) Solvent recovery system with steam condensation system.

ii) Pumps & motors are mechanical seal type.

3 Handling of raw material bags in storage area

Air pollutant (PM)

i) Provision of exhaust ventilation

ii) Provision of PPE.

iii) Provision of Job rotation to reduce exposure.

4 Flange joints of pipeline, pump & motors

Air pollutant (VOC)

i) Routine &periodic inspection to check leakage.

ii) Preventive maintenance, Follow SOP for maintenance.

iii) Pumps & motors will be mechanical seal type.

iv) LDAR program will be followed.

Provision of Flange guard.

5 Solid raw material transferring to reactor

Air pollutant (PM)

Hopper will be provided with powder transfer system.

6 Liquid raw material transferring to reactor

Air pollutant (VOC)

Feeding of liquid raw material will be carried out by closed pipeline and mechanical seal pump.

7 Loading /unloading at storage area

Air pollutant (VOC)

Unloading through pipeline to tank in a close system.

F Hazardous waste

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Page 56 of 80

(as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. [Existing & Proposed]

i Sr. no.




Existing Quantity (MT/ Annum)

Proposed Quantity (MT/ Annum)

Total Quantity (MT/ Annum)

Disposal Method

1 Used Oil Process 5.1 6 0 6 Collection, Storage, Transportation, Disposal by selling to registered re-processor/ Refiners.

2 Process/ distillation residue

Process 28.1 18 60 78 Collection, Storage, Transportation and given to end user/ incineration/ Co-processing.

Sludge contaminated with Oil/ chemicals– (Spill decontaminated waste)

Process 14.4 0 14.4 Collection, Storage, Transportation, Disposal to BEIL.

3 Spent Carbon Process 28.3 216 0 216 Collection, Storage, Transportation, Disposal to BEIL.

4 Off Specification Products

Process 28.4 3.6 0 3.6 Collection, Storage, Transportation, Disposal by Incineration at BEIL.

5 Date Expired Discarded and off-specification Drugs/Medicines

Process 28.5 3 0 3 Collection, Storage, transportation, Disposal by Incineration at BEIL.

6 Spent Mother Liquor

Process 28.1 2160 0 2160 Collection, Storage, transportation, Disposal by Incineration at BEIL.

7 Spent Organic Solvent

Process/ MEE

28.6 720 KL 720 KL 1440 KL Collection, Storage, Transportation and given to end user/ Incineration/ Co-processing.

8 Discarded Containers/

Process 33.1 4 2.5 6.5 Collection, Storage, De-

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Page 57 of 80

Barrels contamination.

Liners Process 6.6 0 6.6 Collection, Storage, De-contamination.

Fibre Board Drums

Process 60 0 60 Collection, Storage, De-contamination.

9 ETP Sludge Process Process

35.3 90 80 170 Collection, Storage, Transportation, Disposal in TSDF, BEIL.

Solid waste from MEE Plant

0 4680 4680 Collection, Storage, Transportation, Disposal in TSDF.

10 Broken Glass Process B2 7.2 0 7.2 Collection, Storage, Transportation, Disposal in TSDF, BEIL.

11 Waste Insulation

Process -- 0 10 10 Collection, Storage, Transportation, Disposal in TSDF.

12 Cotton Waste Process -- 0 5 5 Incineration.

13 Filter and Filter Material Cloth

Process 35.1

0 5 5 Collection, Storage, Transportation & Disposal by incineration at common incinerator of SEPPL/BEIL

High Flow 0 50 50

14 Asbestos broken sheets

Process -- 0 5 5 Collection, Storage, Transportation, Disposal in TSDF.



BEIL Membership certificate is attached as Annexure-XI

iii Details of Non-Hazardous waste & its disposal(MSW and others)

As per Rules./ Waste is collected by local authority


i Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents.

Isopropyl alcohol, Methanol, Toluene and Acetone.%

recovery : 96% t0 99% Product wise details are given in Chapter-2 of EIA report.


Sources: Solvent storage tank, Solvent recovery

System, Handling of RM, Loading /unloading at

storage area, etc.

Other details are given in Chapter-8 of EIA report.

During the meeting dated 17/05/2018, technical presentation made during the meeting by project

proponent. The proposal is expansion. Proposal was appraised based on the information furnished in

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Page 58 of 80

the EIA Report and details presented during the meeting. It is noted that 514 KLPD will be the total

water requirement and 170 KLPD of waste water will be generated. Sewage of 19 KLPD will be

treated in STP and mixed with industrial wastewater and whole wastewater will be treated in

ETPfollowed by RO & MEE and MEE condensate will reused. Natural Gas will be proposed as fuel.

The baseline environmental quality has been assessed for various components of the environment


been conducted for the study area of 5 km radial distance from project site for the period January

2017 to March 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx,

NH3,HCl, CO, and VOC at eight locations, including the project site. Values conform to the prescribed

standards for Ambient Air Quality. The incremental Ground Level Concentration (GLC) has been

computed using ISCST3. The resultant concentrations are within the NAAQS. The 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. Compliance of the TOR was found satisfactory.

After detailed discussion, it was decided to consider the proposal only after satisfactory reply

of the following:

1. Submit details of reception, storage (with type of tanks), handling, consumption and losses

of high vapour pressure bearing solvents keeping production in view with their physical

and chemical properties. Also submit methodology for their handling management with

detailed Leak Detection and Repairing Programme (LDAR) which shall endeavor

prevention of losses of solvents to the best minimum extent.

2. Readdress management of process and distillation residue under compliance of HWR

2016.

3. Justify production quantum of R & D Products with reference to the routine product with all

possible unit processes with undertaking of not being sold out under the umbrella of

commercial production.


� Details of LDAR program for solvents are submitted.

� Process distillation residue shall be collected, stored, transported and incinerated at

CHWTSDF/co-processing.

� Justification for production quantum of R & D products is submitted and the undertaking for

the same is submitted.


found satisfactory.

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Page 59 of 80




8. SIA/GJ/IND2/21563/2017 M/s. Finornic Chemicals (India) Pvt Ltd Plot no. 6233 & 6234, GIDC Industrial Area, Ankleshwar, Dist: Bharuch







30/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: Earthcare Enviro Solutions

Pvt. Ltd., based on the TOR issued by SEIAA.

• This is an existing unit engaged in Synthetic organic chemicals and now proposes for


Sr. no.

Name of the Products CAS no. Quantity (MT/Month) End-use of the products Existing Proposed Total

1. 2-Mercaptobenzimidazole (Existing)

583-39-1

9.00 61.00 70.00

Pharma intermediate

2. Methyl-2-Mercaptobenzimidazole (Existing)

53988-10-6

Rubber chemical

3. Methoxy-2-Mercaptobenzimidazole (Existing)

37052-78-1

Pharma intermediate

4. Zinc Methyl-2-Mercaptobenzimidazole (Existing)

61617-00-3

Rubber chemical

5. Zinc-2-Mercaptobenzimidazole (Existing)

3030-80-6 Rubber chemical

6. Ethoxy-2-Mercaptobenzimidazole (Existing)

55489-15-1

Pharma intermediate

7. Amino-2-Mercaptobenzimidazole (Existing)

2818-66-8 Pharma intermediate

8. Nitro-2-Mercaptobenzimidazole (Existing)


9. Pyrrolyl-2-Mercaptobenzimidazole (Existing)


10. Chloro-2-Mercaptobenzimidazole (Existing)

25369-78-2

Pharma intermediate

11. 1,2-Dimethyl-2-Thiopeusdourea Hydro Iodide (Existing)

41306-45-0

Pharma intermediate

12. R & D of Derivatives / Heterocyclic Chemicals (Custom Synthesis) (Existing)

-- --

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Page 60 of 80

13. Difloromethoxy -2-Mercaptobenzimidazole (Proposed)

97963-62-7

-- 70.00

Pharma intermediate

14. Sodium 2-Mercaptobenzothiazole (50%) (Proposed)


15. Zinc Mercaptobenzothiazole(Proposed)



Notification 2006.



Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): Existing: Rs. 2.00 Crores Proposed: Rs. 0.845 Crores Total: Rs.2.845 Crores

(7) Capital cost for EMS (Environmental Management System): Rs. 0.266 Crores (8) Recurring cost towards the environmental protection measures: Rs. 5.124 Crores per

Annum.

B Total Plot area ( sq. meter) Existing: 2702 Sq. m. Proposed: 2702 Sq. m. Total: 5404 Sq. m.




3. Direct Existing: 24 Proposed: 24 Total: 48

4. Indirect Existing: 8 Proposed: 10 Total: 18

D Water I


GIDC, Ankleshwar

Status of permission from the concern authority. Requested to GIDC for additional water requirement.

Ii Water consumption (KLD)

Existing KLD



Remarks

(A) Domestic 3.50 - 3.50 -

(B) Gardening 6.00 1.00 7.00 -

Industrial

Process 5.16 34.97 40.13 -

Washing 1.62 1.62 3.24 -

Hot Water System 2.00 20.00 22.00 -

Cooling 2.00 4.00 6.00 -

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Page 61 of 80

Others (Scrubber) 0.45 3.00 3.45 -

Industrial Total 11.23 63.59 74.82 -

Grand Total (A+B+C) 20.73 64.59 85.32


2) Quantity to be recycle: Nil


Iii Waste water generation (KLD)




Remarks

(A) Domestic 3.00 -- 3.00 -

Industrial

Process 5.50 37.29 42.79 -

Washing 1.26 1.26 2.52 -

Hot Water System -- -- -- -

Cooling 0.10 0.20 0.30 -

Others (Scrubber) 0.14 1.30 1.44 -


7.00 40.05 47.05 -

-

Iv Treatment facility within premises with capacity (ETP,MEE, STP etc).

ETP exist having primary treatment.

V Mode of Disposal & Final meeting point

Domestic: At present, domestic effluent is disposed in to Septic tank / Soak pit system.

After expansion, there shall be no additional domestic wastewater generation

Industrial: After expansion, effluent coming from plant having low TDS/COD stream will be allowed into existing in-house ETP for its treatment & then disposed to CETP (M/s. ETL) for further treatment & final disposal as unit has already valid CTO for 7.0 KLD wastewater for disposal to CETP. Effluent coming from plant & utility having high TDS/COD stream will be allowed into in-house ETP for pH adjustment and after then it will be sent to common MEE facility operated by M/s. Ankleshwar Cleaner Process Technology Centre Ltd. (ACPTCL) for final disposal.

Vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE etc. , name of CF

CETP: M/s. Enviro Technology Ltd. Common MEE facility: M/s. Ankleshwar Cleaner Process Technology Centre Ltd.

Membership of Common facility (CF) Unit has got membership of CETP & common MEE facility.

Vii Reuse/Recycle details (KLD) --


I Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

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Page 62 of 80

-

Sr. no.

Source of emission With Capacity


Name of the fuel

Quantity of Fuel MT/hr&

MT/Day

Type of emissions

i.e. Air Pollutants

APCM

Existing

1. Thermopack (Capacity: 2 Lac Kcal/hr) 9.35

m

Natural Gas

40 SCM/day PM

SO2

NOx

Adequate stack height provided

2. Hot Water System-1 (Capacity: 1 Lac Kcal/hr)

Natural Gas

40 SCM/day


3. D. G Set (Stand By) (Capacity: 75 KVA)

5.00 m

HSD 10 Lit/hr Adequate stack height provided

Proposed

1. Hot Air Generator-1

(Capacity: 2 Lac Kcal/hr) 9.35 m

Natural Gas

2500 SCM/month

PM

SO2

NOx


2. Hot Air Generator-2

(Capacity: 9 Lac Kcal/hr)

Natural Gas

20,000 SCM/month


3. Hot Water System-2

(Capacity: 10 Lac Kcal/hr)

9.35 m

Natural Gas

400 SCM/day


4.

D. G Set – 02 Nos. (Stand By)(Capacity: 125 KVA each)

5.00 m

HSD 16 Lit/hr Adequate stack height provided

Ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.) [Existing & Proposed]

Sr. no.

Source of emission

Type of emission



Existing

1. Reactor – 2 Nos.

H2S 10.0 m Alkali

Scrubber ≤ 45 mg/Nm3

Proposed – NIL

-

iii Fugitive emission details with its mitigation measures. [Existing & Proposed]..As below

Sources of fugitive emissions will be from raw material storage area, handling of chemicals,

manufacturing process and from vehicle movement on internal road.

To minimize fugitive emission, powder material will be allowed in a vessel through closed loop

while liquid material will be charged through pipeline. Transportation of raw materials &

products will be carried out by trolley within premises and minimum manual material handling

will be carried, so the fugitive emission due to process activity and material handling will be

minimized.


i

Sr. no

Type/Name of Hazardo


Category and Schedule

Quantity (MT/Annum)

Disposal Method

Existing Propose Total

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Page 63 of 80

. us waste as per HWRules

d

1.

ETP Sludge

Effluent Treatment

Plant 35.3

12 MT/year

36 MT/year

48 MT/year

Collection, Storage, Transportation & Disposal at TSDF site – BEIL for secured landfill.

2.

Used Oil Thermopack& D. G Set

5.1 0.24

MT/year 0.46

MT/year 0.70

MT/year

Collection, Storage, Transportation & Disposal by selling to GPCB/CPCB approved Recyclers.

3. Discarded Drums

Raw material & Finished product packing material

33.1

2.4 MT/year

27.6 MT/year

30 MT/year

Collection, Storage, Transportation & Disposal by selling to GPCB Registered Vendor after Detoxification & Decontamination/Reuse

Bags 0.36

MT/year 1.44

MT/year 1.80

MT/year

4.

Spent Carbon

Process (Product

No. 1 to 10 & 13)

28.3 42

MT/year 42

MT/year 84

MT/year

Collection, Storage, Transportation & disposal by sending to RSPL.

5.

Spent Catalyst

Process (Product – Amino-2- Mercapto

benzimidazole)

28.2 5.4

MT/year 31.2

MT/year

36.6

MT/year

Collection, Storage, Transportation & disposal by send back to supplier for Recovery.

6. Spent Solvent (Methanol)

Process (Product No. 7 & 9)

28.6 975

MT/year 10421.4 MT/year

11396.4 MT/year

Collection, Storage & Re-use in Process. 7. Spent

Solvent (Ethyl Acetate)

Process (Product No. 11)

40.36

MT/year 305.24

MT/year 345.6

MT/year

8.

Distillation Residue

Process (Product No. 9)

20.3 -- 70.20

MT/year 70.20

MT/year

Collection, Storage, Transportation & Disposal by sending for incineration OR for co-processing as per CV.

9. Sodium Sulphide Solution

Process (Product

No. 1 to 6, 28.4

660.00 MT/year

4430.40 MT/year

5090.40 MT/year

Maximum quantity will be reused in

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Page 64 of 80

(10 –25 %)

8, 10 & 13)

process within premises and balance quantity will be disposed by selling to Authorized end user as per Haz. Waste Rule-9 and after getting prior permission from GPCB.



• Unit has got membership of TSDF site M/s. BEIL. • Unit has got membership of M/s. Recycling

Solutions Pvt. Ltd. (RSPL).

iii Details of Non-Hazardous waste & its disposal(MSW and others)

Sr. No.

Type of Waste Source of

Generation Category of Waste

Disposal

1. Domestic Waste (Food waste, Plastic, Paper etc.)

Employees working in the premises

MSW Collected in separate bin and disposed to bin of GIDC.

2. Industrial Waste (Glass wool [Insulating Material, Scrap])

Steam Pipe & Vessels

ISW Sell to local scrap vendor

3. Industrial Waste (Wooden pellets)

From Raw Material & Product storage area

ISW Sell to local scrap vender


I Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents.

Solvent recovery system will be installed. Recovered solvent will be again reused in the process and residue will be disposed to TSDF site. Recovery of solvent will be minimum 96%.


• VOCs generation will be from storage and usage of raw materials.

• VOC analyzers will be provided to detect any solvent leakages during storage and handling.

• During the meeting dated 11/04/2018, technical presentation made during the meeting by project

proponent.

• During the meeting, the project was appraised based on the information furnished in the EIA

Report and details presented during the meeting.

• The baseline environmental quality has been assessed for various components of the

environment viz. air, noise, water, biological and socioeconomic aspect. The baseline

environmental study has been conducted for the study area of 5 km radial distance from project

site for the period March 2017 to May 2017. Ambient Air Quality monitoring was carried out for

PM10, PM2.5, SO2, NOx, NH3, VOC, HCl, and CO at eight locations, including the project site.

Values conform to the prescribed standards for Ambient Air Quality. The incremental Ground

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Page 65 of 80

Level Concentration (GLC) has been computed using ISCST – 3 model. 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.

• This unit was established well before year 2006. They have 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.

• While reviewing the baseline data, project specific parameter H2S is not covered in EIA report.

• Upon asking PP could not justify regarding the same.

• Committee asked to submit exact location of the sampling points with date & time along with

photographs. Sensors of CS2 are not provided for existing project.

• Details regarding CSR, Solvent management are not properly addressed in EIA report.

• After detailed discussion, it was decided to consider the project further only after

submission of the following:

1. Submit exact location (Lat-Long) of the sampling points with date & time along with

photographs.

2. Compliance of ToR no. 44 regarding EMP.

3. Compliance of ToR no. 42 regarding Solvent management. .

4. Explore the possibilities for complete Zero Liquid Discharge considering GPCB Circular vide

dated 04/04/2018.

5. Precautionary measures for CS2 emissions. Provision of CS2 sensors.

6. Detailed Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvents

proposed for use in-house with detailed chemical properties including vapour pressure. LDAR

shall endeavour prevention of losses of solvents to the best minimum extent.


� Unit has submitted exact location (Lat-Long) of the sampling with date & time along with

photographs.

� Detailed EMP is submitted.

� Unit will provide in-house solvent recovery system including solvent loss, recovery efficiency.

All solvent will be recovered more than 95%.

� As per GPCB MOM dated 11/06/2018 regarding permission of additional hydraulic load to

CETP in Ankleshwar and Panoli area, unit will discharge existing effluent load to CETP (M/s.

ETL) as per existing valid CTO and additional effluent load will be disposed to Common MEE

facility operated by M/s. ACPTCL.

� Unit will take proper precautionary measures for CS2 emissions with provision of CS2 sensors

with safety alarm.

� Detailed LDAR program is submitted.

of 80


Page 66 of 80


found satisfactory.




9. SIA/GJ/IND2/18319/2017 M/s. RSJ Industries Plot No. 10/11, GIDC Phase-I, Vatva, Ahmedabad.

ToR Amendment



• SEIAA, Gujarat has accorded ToR [Terms of Reference] to M/s: Sanghi Industries

Limited, vide letter no. SEIAA/GUJ/TOR/5(f)/477/2017 vide dated 29/04/2017.

• Project proponent requested for amendment in the ToR as under:

• Expansion of the project instead of Fresh case.

• Project proponent has submitted revised Form-1 and PFR with their application for the

amendment sought vide online application no. SIA/GJ/IND2/18319/2017 dated

17/07/2018.

• This proposal was considered in the SEAC meeting dated 09/08/2018. During the

meeting, Committee noted that they have obtained ToR as new case. However, this

project is existing and they have obtained CC&A for the existing activity.

• After deliberation, it was decided to recommend for amendment in TOR as requested.

Based on the information furnished by the project proponent in revised Form-1, PFR and

relevant documents, Committee decided for the amendment sought and now project activity/

details mentioned in the TOR letter no. SEIAA/GUJ/TOR/5(f)/477/2017 vide dated 29/04/2017:

Product profile:



Sr.

No. Name of the Products

CAS no. /CI

no.

Quantity

MT/Month

End-use of

products

1 Foundry fluxes (Foundry mould paint) (Existing)

67-72-1 252 Foundry Industries

&

Food dyes,

printing & Textile

industries.

2 Foro Bond-1612 (Existing)

400

3 Alkaline Phenol Formaldehyde Resin (Proposed)

9003-35-4 300

4 Furfuryl Alcohol Phenol Urea

54465-67-7 300

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Page 67 of 80

(Proposed)

5 Phenol Formaldehyde Resin (Proposed)

9003-35-4 300

6

Phenol Formaldehyde Resin( Shell Sand Resin) (Proposed)

9003-35-4 300

7

Phenol Formaldehyde Resin (Cold Box Resin) (Proposed)

9003-35-4 300


Notification 2006.



Sr.

no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): Proposed: 1.015 Crore

B Total Plot area

( sq. meter)

Existing: 4401.37 Sq. m.

Proposed: 0

Total: 4401.37 Sq. m.


( sq. meter)

Existing: 40 Sq. m.

Proposed: 125 Sq. m.

Total: 165 Sq. m.

C Employment generation Existing: 6

Proposed: 14

Total: 20

D Water

i

Source of Water Supply(GIDC Bore well, Surface

water, Tanker supply etc...)

GIDC VatvaBorewell

Status of permission from the concern authority. No


Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 0.05 0.95 1

(B) Gardening 0 0.5 0.5

(C) Industrial

Process 0.2 2.8 3

Washing 0 0 0

Boiler 0 2.2 2.2

Cooling 0 6 6

Others 0 0 0

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Page 68 of 80

Industrial Total 0.2 11 11.2

Grand Total (A+B+C) 0.25 12.45 12.7


2) Quantity to be recycle: No recycle



Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 0.05 0.75 0.8

(B) Industrial

Process 0 8 8

Washing 0 0 0

Boiler 0 0.1 0.1

Cooling 0 0.3 0.3

Others 0 0 0

Total Industrial waste water 0 8.4 8.4

Iv Treatment facility within premises with capacity [For existing and Proposed]


Effluent Treatment Plant (Primary Treatment)

Capacity of ETP: 12 KLPD

V Mode of Disposal & Final meeting point

Domestic: 0.8 KLD discharge to soak pit via septic tank.

Industrial: 8.4 KLD goes to ETP than send to Chhatral Environment Management

System Pvt. Ltd. – Chhatralfor Spray Drying.

Vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE, CHWIF

etc.


Common Spray Dryer –Chhatral Environment Management System Pvt. Ltd. - Chhatral


Common Spray Dryer –Chhatral Environment Management System Pvt. Ltd. - Chhatral

Vii Reuse/Recycle details (KLD)

No Reuse/Recycle

E Air



Existing & Proposed

-

Sr.

no.

Source of

emission

With Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity of

Fuel

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1

Steam Boiler

(1 TPH)

(Proposed)

11 Natural

Gas

5

MMBTU/Day

PM

SOx

NOx

--

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Page 69 of 80

2

Thermic Fluid

Heater

(2 Lac k cal/hr)

(Proposed)

11 --

3

D. G. Set

(25 KVA)

(Proposed)

06 Diesel 50

liter/Month

Acoustic

enclosure

-

ii Process gas i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)

Existing & Proposed

-No Process Gas will be generated existing as well as proposed manufacturing activity.

iii Fugitive emission details with its mitigation measures.

Measures taken for fugitive emission control:

• Proper storage of raw materials, products and fuels.

• Ensuring closed feeding and sampling.

• Establishing SOPs for start-up, shut down and maintenance operational procedures.

• Regular work place monitoring and ambient air quality monitoring as per post project

monitoring plan.

• Pneumatically transfer of raw material in reactor.

• PPE will be provided to the workers working in process area.

• Greenbelt will be developed around the plant to arrest the fugitive emission.

• Paved road will make to reduce the fugitive emission. Water sprinkler will be provided to

reduce the

F Hazardous waste

(as per the Hazardous and Other Wastes (Management and Transboundary Movement)

Rules 2016.Existing & Proposed

i

Sr

.

n

o.

Type/Nam

e of

Hazardous

waste

Source of

generation

Categor

y and

Schedul

e as per

HW

Rules.

Quantity

(MT/Annum)

Disposal Method

Existi

ng

Propos

ed

Tot

al

1

ETP Waste From ETP 35.3 0 1 1

Collection, storage,

transportation and

disposal to TSDF site

approved by board.

2

Resin

waste/proc

ess waste

Manufacturin

g process 23.1 0 0.5 0.5


transportation

Disposal at TSDF

approval by the

Board.

3

Discarded

drums/cont

ainers/bag

s

Raw material

section 33.1 0.15 0.15 0.3


Decontamination,

Transportation,

Disposal by selling to

of 80


Page 70 of 80

authorized recycler.

4 Used/Spen

t Oil

Lubrication/D

. G. Set 5.1 0 20 Lit

20

Lit

Collections, Storage,

Transportation,

Disposal by selling to

registered reprocess

or reuse as

lubrication in plant.

-

ii Membership details of TSDF, CHWIF etc. TSDF

iii Details of Non-Hazardous waste & its


No


i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered Solvents

• Methanol, Solvent RX will use in our manufacturing process and it will be consume in

manufacturing process so, no need to recover.


• We will measure VOC level in our manufacturing unit as well as Raw Material Storage

area we will also do work place monitoring & according implementation.

Additional Terms of reference (TOR)

a) Need for the proposed expansion should be justified in detail.

b) Records of any legalbreach of Environmental laws i.e. details of show- cause notices,

closure notices etc. served by the GPCB to the existing unit in last 3 years and actions

taken then after for prevention of pollution.

c) Copy of Consent to Operate (CC&A) obtained along with point wise compliance status

of all the conditions stipulated therein.

d) Copies of XGN generated Inspection reports with analysis reports of the

water/Air/Hazardous samples collected by GPCB (Last 3 year). Copies of instructions

issued by GPCB in last 2 year and point wise compliance thereof.

10. SIA/GJ/IND2/22122/2017 M/s. Swaraj Life Science Plot No. 906/18, GIDC Panoli, Ankleshwar, Bharuch.




• PP has submitted online application vide no. IA/GJ/IND2/62315/2017dated 24/01/2018 for


• MoEF&CC has issued TOR to PP vide letter no. J-11011/89/2017-IA-II(I dated 29/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: Aqua Air Environmental

Engineers Pvt. Ltd.based on the TOR issued by MoEF&CC.



of 80


Page 71 of 80

Sr. no.


CAS no. / CI no.

Quantity MT/Month

End-use of the products


1 Sodium

Thiosulphate

7772-98-

7

60 -- 60

Dyes Industries

2 Sodium Bisulfite 7631-90-

5

Dyes Industries

3 Potassium

Chloride

7440-09-

7

Dyes Industries

4 Sodium Acetate 127-09-3 Dyes Industries

5 Recovered Piperazine Anhydrous

110-85-0 10 -- 10

Pharma Industries

6 Lamotrigine& Intermediates

84057-

84-1

-- 5 5

Anti-epileptic

7 CitrizineDihydrochloride& Intermediates

83881-

52-1

Anti-histamines

8 Levocitrizine& Intermediates

130018-

77-8

Sneezing, itching,

watery eyes

9 ClopidogrelBisulphate& Intermediates

120202-

66-6

Antiplatelet agent

10 Glimepiride &Intermediates

93479-

97-1

Anti - Diabatic

11 Sodium Valporate& Intermediates

1069-66-

5

To treat epilepsy

and bipolar

disorder

12 Riboflavine B2 Phosphate & Intermediates

130-40-5 To treat Dietary

13 Fenofibarte& Intermediates

49562-

28-9

Anti lipemics

14 Diclofenac Sodium & Intermediates

15307-

79-6

Anti - pain

15 Aceclofenac& Intermediates

89796-

99-6

Anti - pain

16 Dexametharan& Intermediates

---- To treat

inflammatory

17 Tramadol & Intermediates

27203-

92-5

Opiate (narcotic) an

algesic

18 Atorvastatin & Intermediates

134523-

00-5

Cholesterol-

lowering

19 Pregabaline & Intermediates

148553-

50-8

Neuropathic pain

Total 70 5 75 --


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Page 72 of 80

Notification 2006.



Sr.

no.

Particulars Details


(Rs. in Crores):

Existing:60 Lakhs Proposed:2.5Crore Total: 3.1Crore

B Total Plot area

( sq. meter)

Existing: 1315 Sq. m. Proposed: 0.0 Sq. m. Total: 1315 Sq. m.


( sq. meter)

Existing: 0.0 Sq. m. Proposed: 350 Sq. m. Total: 350 Sq. m.

C Employment generation Existing:10

Proposed:20

Total:30

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 water supply letter No. GIDC/DEE/PNL/1550 dated: 26/04/2017


Existing

KLD

Proposed

(Additiona

l)

KLD

Total after

Expansion

KLD

(A) Domestic 1.0 1.0 2.0


(C) Industrial

Process 3.0 7.0 10.0

Washing 0.0 0.5 0.5

Boiler 0.0 5.0 5.0

Cooling 0.0 5.0 5.0

Others 0.0 0.5 0.5

Industrial Total 3.0 18.0 21.0

Grand Total (A+B+C) 4.0 20.0 24.0

1) Total water requirement for the project: 24 KLD

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Page 73 of 80

2) Quantity to be recycle: 0.0 KLD

3) Total fresh water requirement: 24 KLD


Category Existin

g

KLD

Proposed

(Additiona

l)

KLD

Total after

Expansion

KLD

(A) Domestic 0.8 0.8 1.6

(B) Industrial

Process -- 4.47 4.47

Washing -- 0.5 0.5

Boiler -- 0.1 0.1

Cooling -- 0.1 0.1

Others -- 0.5 0.5

Total Industrial waste

water

-- 5.67 5.67

iv Treatment facility within premises with capacity [For existing and Proposed]


Existing: No ETP

Proposed: ETP Capacity -9 KL/Day

The waste water from unit will be brought to the treatment plant via a series of underground

pipelines. The waste water will be collected in the collection cum equalization tank. Two

numbers of tanks are proposed. One will in filling mode for equalization of waste water while

the other will be in pumping mode. The equalized wastewater is pumped to the flash mixer for

addition of chemicals like lime. From the flash mixer the waste water flows into the flocculator

where chemical flocs are formed by coagulation and flocculation by addition of Alum/Ferrous

sulphate and polyelectrolyte. These flocs are removed in the primary settling tank. The

underflow (sludge) from the primary settling tank is taken to sludge dewatering unit (Sludge

Drying Bed).

The Domestic wastewater is disposed of through septic tank & soak pit.


Domestic: 1.6 KL/Day Sewage is disposed through Septic Tank/Soak Pit.

Industrial: 5.67 KL/Day effluent treated in ETP then send to Common MEE of M/s.

ACPTCL for Disposal.

vi In case of Common facility (CF) like CETP, Common Spray dryer, Common MEE,

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CHWIF etc.


Common MEE facility of M/s. ACPTCL, Ankleshwar


Company has obtained membership of Common MEE facility of M/s. ACPTCL,

Ankleshwar dated: 12/09/2017

vii Reuse/Recycle details (KLD)

There is no any reuse/recyle.

E Air


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

e.g. Boiler (8 TPH)

Stack Height (meter

)

Name of the fuel

Quantity of Fuel

MT/hr&MT/Day

Type of emissions i.e. Air Pollutant

s

APCM

Emission Standard

s

Existing

1 Boiler

(1000 kg/hr.) 11

Natural Gas

200 SCM/da

y

PM SOx NOx

Adequate Height

<150mg/NM

3

<100 ppm <50 ppm

Proposed

2

Boiler (1500 kg/hr.) 30

Agro Waste

2 MT/Day

PM SOx NOx

Multicyclone Separator

with bag filter

<150mg/NM

3

<100 ppm <50 ppm

3

TFH (2 lakh kcal/hr.) 30

Agro Waste

2 MT/Day

PM SOx NOx

Multicyclone Separator

with bag filter

<150mg/NM

3

<100 ppm <50 ppm

4 DG set (100

KVA) 11 Diesel

15 Liter/HR

PM SOx NOx

Adequate Height

<150mg/NM

3

<100 ppm <50 ppm

-


Proposed

-

Sr.

no

Source of

emission

Type of

emissio

Stack/Vent

Height


Measures(APCM)

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Page 75 of 80

. n (meter)

1 Process Vent

(Chlorination)

11 m HCl < 20

mg/Nm3

Water + Caustic Scrubber

2 Process Vent

(Sulphonation)

11 m SO2 < 40

mg/Nm3

Two Stage Caustic Scrubber

-

iii Fugitive emission details with its mitigation measures.

Following measures will be adopted to prevent and control fugitive emissionsL

1. Airborne dust at all transfers operations/ points will be controlled either by

spraying water or providing enclosures.

2. Care will be taken to store construction material properly to prevent fugitive

emissions, if any.

3. Regular maintenance of valves, pumps, flanges, joints and other equipment will

be done to prevent leakages and thus minimizing the fugitive emissions of

VOCs.

4. Entire process will be carried out in the closed reactors with proper maintenance

of pressure and temperature.

5. Periodic monitoring of work area will be carried out to check the fugitive

emission.

6. Breather valves will be provided on solvent tanks.

7. Solvent tank vents will be connected to vent chillers.

8. To eliminate chances of leakages from glands of pumps, mechanical seal will be

provided at all solvent pumps.

9. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank

vents will be connected to vent chillers.

10. Minimum number of flanges, joints and valves in pipelines.

11. Enclosures to chemical storage area, collection of emission from loading of

raw materials in particular solvents through hoods and ducts by induced draft,

and control by scrubber / dust collector to be ensured.

12. Nitrogen blanketing will be provided, besides special care needs to be taken

for control in respect of odorous chemicals.

F Hazardous waste

(as per the Hazardous and Other Wastes (Management and Transboundary Movement)

Rules 2016.Existing & Proposed

i

Sr. no.




Quantity (MT/Annum)

Disposal Method

Existing

Proposed

Total

1 ETP Sludge

ETP (SCH-I/Cat. 35.3)

00 24 24 Collection, Storage, Transportation

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Page 76 of 80

And Dispose To TSDF Of M/S. PSWML, Panoli Or M/S. BEIL, Bharuch

2 Discarded Drums /Containers

Process (SCH-I/Cat. 33.1)

12 6 18 Collection, Storage, Transportation, Decontamination & Disposal By Selling To Registered Recycler

3 Discarded Liner/Bag

Process (SCH-I/Cat. 33.1)

1.2 0.24 1.44

4 Distillation Residue

Distillation (SCH-I/Cat. 20.3)

00 12 12 Collection, Storage, Transportation And Dispose To RSPL or Co-processing In Cement Industries or Common Incineration Site

5 Piperazine Ml

Process (Citrizine)

(SCH-I/Cat. 28.1)

0 240 240

Collection, Storage and Recovered in premise and reuse in citrizine.

6 Sulphuric Acid

Process (Citrizine,

LEVOCITRIZINE)

(SCH-I/Cat. 28.1)

00 84 84 Collection, Storage, Transportation and Sell To End User who is having rule-9 permission

7 Spent Catalyst

Process (ATORVAS

TATIN)

(SCH-I/Cat. 28.2)

00 6 6 Collection, Storage, Transportation and send to recycler

8 Spent Carbon

Process (Clopidogrel

, DMR, TRAMADOL

, PREGABAL

INE)

(SCH-I/Cat. 28.3)

00 6 6 Collection, Storage, Transportation and Dispose to Common Incineration Site or Co-Processing in Cement Industries

9 Used Process (SCH- 0.24 0.24 0.4 Collection,

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Oil I/Cat. 5.1)

8 Storage, Transportation, Disposal by Selling to Registered Recycler or Re-Use as Lubricant

10 INORGANIC Process Waste

Process (SCH-I/Cat-28.1)

36 60 96 Collection, Storage, Transportation and Disposal at TSDF Site Of M/S. PSWML, Panoli or M/S. BEIL, Bharuch.

11 Caustic Lye (Hydride)

Process (Piperazine)

(Cat-SCH-II/B14)

480 -- 480

Collection, Storage, Transportation and Sell To End User who is having rule-9 permission

12 Sodium bromide (30%)

Process (SODIUM

VALPROATE )

(SCH-II/B5)

00 240 240

13 Sodium Sulfite (20%)

Scrubber (SCH-I/Cat-28.1)

00 180 180

14 NaCl (18%)

Scrubber (SCH-I/Cat-28.1)

00 180 180

Collection, Storage, Transportation and send to ETP for further treatment.

-

ii Membership details of TSDF, CHWIF etc. Company has Membership of TSDF,

CHWIF – M/s. BEIL, ANkleshwar vide letter

No. BEIL/ANK/2017 dated 27/04/2017.

iii Details of Non-Hazardous waste & its


No non Hazardous waste will be generated


i Types of solvents, Details of Solvent recovery, % recovery. reuse of recovered

Solvents

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Page 78 of 80

SOLVENT

INPUT

RECOVER LOSSES

%RECOVER

%LOSSES

Toluene 30.4 28.88 1.52 95 5.0

MDC 5.32 5.15 0.17 96.80 3.2

Ethyle Acetate

5.60 5.36 0.18 95.0 5.0

IPA 6.60 6.27 0.33 95.2 4.8

Methanol 11.2 10.64 0.56 95.1 4.9

Acetone 2.26 2.15 0.11 95.13 4.87


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.

• Nitrogen blanketing will be provided, besides special care needs to be taken for control in respect of odorous chemicals.

• 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 Flange joints of the pipe lines which carry solvents will be covered with flange guards.

• 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.

• Stand by pumps will be provided on all scrubbers. Besides, scrubbers are equipped with on-line pH meter with hooter system for better operational control.

• Regular inspection of floating roof seals and proper preventive maintenance of roofs and seals for tanks.

• Adequate ventilation will be provided.

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Page 79 of 80

During the meeting dated 04/05/2018, technical presentation made during the meeting by project

proponent. The proposal is for expansion. Compliance status was discussed and found satisfactory.

Proposal was appraised based on the information furnished in the EIA Report and details presented

during the meeting. It is noted that 24 KLPD will be the total water requirement and 7.27 KLPD of

waste water will be generated. Industrial effluent of 5.67 KL/day shall be treated in ETP and

discharged to the common MEE of M/s: ACPTCL. Agro waste will be proposed as fuel. The baseline

environmental quality has been assessed for various components of the environment viz. air, noise,

water, biological and socioeconomic aspect. The baseline environmental study has been conducted

for the study area of 10 km radial distance from project site for the period March 2017 to May 2017.

Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, O3, Pb, NH3, CO,

C6H6, BaP, As, Ni, HCl, HC and VOC at nine locations, including the project site. Values conform to

the prescribed standards for Ambient Air Quality. The incremental Ground Level Concentration (GLC)

has been computed using ISCST3. The resultant concentrations are within the NAAQS. The

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.Committee discussed about specific End-use Tramadol &

Intermediates and asked to submit details. Issues regarding baseline study, CER, Hazardous waste

management etc. have been discussed. This unit have valid CC&A for existing unit. Copy of CC&A,

its compliance report is submitted. PP ensured that there are no court cases pending and no public

complaints against the project.

After detailed discussion, It was decided to further appraise the project only after submission

of the following:

1. Specific End-use Tramadol & Intermediates. Legal undertaking regarding no applicability of

any provisions of the Narcotics Control Bureau.

2. Management of spent solvent and bleed liquor as per the HW Rules 2016.

3. Details of sampling locations with Latitude-Longitude & Photographs, Date and time of

sampling of baseline study covered in EIA report.

4. Compliance of ToR no. 34 with respect to values of specific parameters.

5. Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment

Responsibility” (CER). A need-based outlay with year-wise budgetary provision including

bifurcation of each activity with provision of capital cost and recurring cost.

The PP has submitted the reply vide letters dated: 15/06/2018 as below:

� Legal undertaking regarding no applicability of any provisions of Narcotics Control Bureau.

� Management of the solvent and bleed liquor as per the HW rule 2016.

� Details of sampling locations with Latitude-Longitude & Photographs, Date and time of

sampling of baseline study covered in EIA report.

� Compliance of ToR no. 34 with respect to values of specific parameters.

� Compliance of MoEFCC’s OM dated 01/05/2018regarding “Corporate Environment

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Page 80 of 80

Responsibility” (CER).

The proposal was considered in the SEAC meeting (Table Agenda) dated 26/06/2018. During the

meeting, committee observed that PP has submitted reply for the additional details sought by SEAC.

Reply was found satisfactory except Compliance of ToR no. 34 with respect to values of specific

parameters.

In view of the above, Committee decided to consider the proposal in one of the upcoming SEAC

meetings for further reconsideration of the proposal only after resubmission of the following:

1. Compliance of ToR no. 34 with respect to values of specific parameters

The PP has submitted the reply vide letters dated: 06/08/2018 as below:

� Compliance of TOR no. 34 with respect to values of specific parameters is submitted.

The proposal was considered in SEAC meeting dated: 08/08/2018 and reply was found satisfactory.

During the meeting Committee considered this proposal and reply submitted by PP found

satisfactory.




Meeting ended with thanks to the Chair and the Members.

Minutes approved by:

1. Dr. Dinesh Misra, Chairman, SEAC 2. Shri S. C. Srivastav, Vice Chairman, SEAC

3. Shri V. N. Patel, Member, SEAC

4. Dr. V. K. Jain, Member, SEAC

5. Shri Rajesh I Shah, Member, SEAC

6. Shri A. K. Muley, Member, SEAC

7. Shri R. J. Shah, Member, SEAC

minutes of the 424 committee room, geer foundation ... minutes of the 424th i.pdf3 two stage alkali...

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