minutes of the 446 meeting of the state level expert ... minutes of the 446th i.pdf · page 1 of 48...

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446thmeeting of SEAC-Gujarat, Dated 29.10.2018

Page 1 of 48

Minutes of the 446th meeting of the State Level Expert Appraisal Committee held on 29/10/2018

at Committee Room, Gujarat Pollution Control Board, Sector 10-A, Gandhinagar.

The 446h meeting of the State Level Expert Appraisal Committee (SEAC) was held on 29th October

2018 at Committee Room, Gujarat Pollution Control Board, Sector 10-A, Gandhinagar. Following

members attended the meeting:

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

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

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

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

The additional agenda of TOR/Scoping cases and Appraisal was taken up. The applicants made

presentations on the activities to be carried out along with other details furnished in the Form-1, PFR,

EIA-EMP reports and other reports.

6. IA/GJ/IND2/65259/2017 M/s Indian Oil Corporation Limited. (IOCL)

Kandla Foreshore Terminal Near Booster

Station.

PO – Old Kandla, District –Kutch, Taluka

Gandhidham, Gujarat-370210

Appraisal

Project / Activity No.: 6(b)

Project status: Expansion

• PP has submitted online application vide no. IA/GJ/IND2/65259/2017 of dated 04/10/2018 for

obtaining Environmental Clearance.

• MoEf & CC has issued TOR to PP vide letter No: IA-J-11011/318/2017-IA-II(I) Date: 17/08/2017.

• Project proponent has submitted EIA Report prepared by M/s Engineers India Limited based on the

TOR issued by SEIAA.

• This is an expansion unit and proposes for expansion of isolated storage and handling of Hazardous

chemicals plant as tabulated below:

Sr.

no.

Name of the

Hazardous

chemicals

for storage

Storage details

Quantity

MT/Month End-use

of the

products Existing Proposed Total

1 MS Existing: 6 tanks

Proposed: Nil tank

66080 KL

6 tanks

- 66080 KL

6 tanks

Motor

Spirit

2 HSD Existing: 9 tanks 214386 KL - 214386 KL Diesel

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Proposed: Nil tank 9 tanks 9 tanks

3 SKO Existing: 2 tank

Proposed: Nil

47500 KL

2 tank

- 47500 KL

2 tank

Kerosene

4 ATF Existing: 3 tanks

Proposed: Nil

71298 KL

3 tanks

- 71298 KL

3 tanks

ATF

5 Naphtha Existing: 4 tanks

Proposed: Nil tank

94246 KL

4 tanks

- 94246 KL

4 tanks

Naphtha

5 Ethanol Existing: 3 tanks

Proposed: 3 tanks

110 KL

3 tanks

600 KL

3 tanks

710 KL

6 tanks

Ethanol

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

2006.

• PP was called for presentation in the SEAC meeting dated 29/10/2018.

• Salient features of the project are as under:

Sr.

no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing: NA

Proposed: 2.8 crores

Total: 2.8 crores

B Total Plot area

( sq. meter)

Existing: 146 acre (590841sq. m)

Proposed: Nil

Total: 146 acre (590841 sq. m)

Green belt area,/Tree Plantation area

( sq. meter)

Existing: 2.0 acre (8093.71 sq. m)

Proposed: Nil

Total: 2.0 acre (8093.71 sq. m)

C Employment generation Existing: 75

Proposed: Nil

Total: 75

D Water

i

Source of Water Supply (GIDC Bore well,

Surface water, Tanker supply etc...)

Gujarat Water Supply and Sewerage Board

Status of permission from the concern

authority.

Pipeline connection from Gujarat Water Supply and

Sewerage Board

ii

Water consumption (KLD)

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Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 8 Nil 8

(B) Gardening - - -

Industrial

Process - - -

Washing 3 - 3

Boiler - - -

Cooling - - -

Others - - -

Industrial Total 11 - 11

Grand Total (A+B+C) 11 - 11

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

existing water supply i.e. 11 KLD available to Kandla Fore Shore terminal.

2) Quantity to be recycle: 8 KLD

3) Total fresh water requirement: 11 KLD.

iii

Waste water generation (KLD)

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 6 - 6

Industrial

Process - - -

Washing 2 Intermittent 2

Boiler - - -

Cooling - - -

Others - - -

Total Industrial

waste water

8 - 8

-

iv Treatment facility within premises with

capacity

[ETP (Primary, Secondary, Tertiary), MEE,

ETP of 120 m3/day

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Stripper, Spray Dryer, STP etc].

v Mode of Disposal & Final meeting point

Domestic: Soak pit

Industrial: The treated water is used inside the

terminal for gardening purpose.

vi In case of Common facility (CF) like CETP,

Common Spray dryer, Common MEE etc. ,

name of CF

Not Applicable

Membership of CF Not Applicable

vii Reuse/Recycle details (KLD) 8 KLD

E Air [Existing & Proposed]

i Flue gas emission details

No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc.

Diesel consumption in the terminal is 65 Litre/Day.

SR.

no.

Source of

emission

With Capacity

Stack

Height

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1 DG-500 KVA 16 M HSD 5

Litre/Day SO2, NOx

Acoustic

enclosures

2 DG-500 KVA 16 M

HSD 5

Litre/Day SO2, NOx

Acoustic

enclosures

3 DG-500 KVA 16 M

HSD 5

Litre/Day SO2, NOx

Acoustic

enclosures

4 DG-500 KVA 16 M

HSD 5

Litre/Day SO2, NOx

Acoustic

enclosures

5 Fire Engine-1 &

2 (358 KW) 11 M HSD

15

Litre/Day SO2, NOx

Acoustic

enclosures

6

Fire Engine

3,4,5,6,7 (261

KW)

11 M HSD 30

Litre/Day SO2, NOx

Acoustic

enclosures

-

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

[Existing & Proposed]

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Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution Control

Measures

(APCM)

1 DG Stack SO2,

NOx

As per serial

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

-

iii Fugitive emission details with its mitigation measures.

[Existing & Proposed]GAs below:

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

be taken.

iv VOC emission sources and its mitigation measures

Proposed Ethanol tanks are above ground horizontal tanks. Only one tank will be operated for

receipt as per present practice. Therefore there will not be any increase in quantity of emission

from present limit.

F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary

Movement) Rules 2016.


i

Sr.

no.

Type/Name of

Hazardous

waste

Source of

generation

Category and

Schedule as

per HW Rules.

Quantity

(MT/Annum)

Disposal Method

1 Chemical

Sludge from

ETP

ETP 35.3 24 MT/Year Collection, storage,

Transportation and

Disposal by selling out to

authorized recycler

2 Used Oil DG sets 5.1 1.5 MT/Year Collection, storage,

transportation, and

disposal at TSDF

ii Membership details of TSDF, CHWIF etc. Saurashtra Enviro Project Pvt. Ltd.

iii Details of Non-Hazardous waste & its

disposal (MSW and others)

All hazardous waste will be given to Saurashtra

Enviro Project Pvt. Ltd. for safe disposal.

• During the meeting dated 29/10/2018, technical presentation made by project proponent.

• At present unit is engaged in isolated storage and handling of Hazardous chemicals for which they

have obtained CC&A of the Board. The proposal is for expansion of isolated storage and handling of

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Hazardous chemicals.

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

Observation:

• This proposal is for expansion of existing unit and for now proposes isolated storage and handling of

Hazardous chemicals. This unit is having valid CC&A for existing unit. Copy of CC&A, CC&A

compliance report is submitted. PP ensured that there are no court cases pending and no public

complaints against the project.

• Total water consumption will be 11 KLD. Total wastewater generation will be 8 KLD. After proposed

expansion, there will be no change in industrial and domestic waste water generation i.e. 8 KLD.

• 8 KLD treated effluent will be used for gardening purpose within premises..

• HSD will be used as fuel for DG set and fire engine..

• Hazardous waste management will be as per the HW Rules.

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

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

xbeen conducted for the study area of 10 km radial distance from project site for the period March -

April, 2018. site will remain within the National Ambient Air Quality Standards (NAAQS).

• Risk assessment including prediction of the worst-case scenario and maximum credible accident

scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site

Emergency Plan has been covered in the RA report.

Discussions & Conclusion:

• Committee noted that proposal is for enhancement of the storage tank capacity for Ethanol. It is

noted that three Above Ground Horizontal tanks of Ethanol each of 200 KL (Total capacity of 600 KL)

are proposed to be installed. PP has obtained TOR from MOEF&CC where in PP is asked to conduct

Public hearing. Asking for details of Public hearing, PP mentioned that they approached MOEF&CC

for amendment in TOR to which MOEF&CC generated EDS on 10/09/2018 vide proposal NO:

IA/GJ/IND2/65259/2017 asking PP “ To refer Ministry’s OM dated 27th April 2018 providing

exemption from public consultation/ Hearing for the projects/Activities located within the industrial

areas/estates/parks and required to submit the proposal for environmental clearance accordingly to

the concerned authority (SEIAA/ MoEF&CC). Referring to this, PP was asked to submit the details of

status of notified area wherein the storage capacity enhancement is proposed. It is also noted that

proposed expansion is within the existing premises and location is within notified area, hence PP

mentioned that applicability of CRZ notification 2011 does not exist.

• Considering the proposed expansion, compliance of CCA conditions, action under various

environmental rules/acts by GPCB, public compliant/litigation pending against the unit were

discussed at length. Committee also deliberated safety measures proposed by the unit for the

additional tanks as well as for the existing facilities.

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• During appraisal, committee noted that air quality is not within the NAAQ 2009 at villages Tuna,

Galpadar, Kund.

Committee deliberated compliance of the TOR issued and asked PP to submit following details so as

to consider the proposal in one of the upcoming SEAC meeting for further consideration.

1. Detailed safety measures including SOP being implemented for existing facilities and also for the

proposed tanks for ethanol to prevent accidents.

2. Need based budgetary outlay of CER as per the OM of MOEF&CC dated 01/05/2018.

3. To address the ambient air quality at the villages Tuna, Galpadar and Kand and associated

mitigation measures to reduce GLC along with the conclusion based on air Model study.

4. Revised environmental management plan (EMP) with budgetary provision of capital cost and recurring

cost after incorporating additional environmental mitigation measures.

7. SIA/GJ/IND2/29117/2018

M/s Indian Oil Corporation Limited

Plot no- Moje Ichhapore – SR No. 270/3 &

Moje Kawas SR No. 32/P, PO – Ichhapore,

Hazira Road, District – Surat Gujarat-394510

Appraisal

Project / Activity No.: 6(b)


• PP has submitted online application vide no. SIA/GJ/IND2/29117/2018 of dated 04/10/2018 for


• SEIAA has issued TOR to PP vide letter No: SEIAA/GUJ/TOR/6(b)/893/2018 dated 28/08/2018.

• Project proponent has submitted EIA Report prepared by M/s Engineers India Limited based on the

TOR issued by SEIAA.

• This is an expansion unit and proposes for expansion of isolated storage and handling of Hazardous

chemicals plant as tabulated below:

Sr.

no.

Name of the

Hazardous

chemicals

for storage

Storage details Quantity

MT/Month

End-use

of the

products Existing Proposed Total

1 MS BS-IV Existing: 7 tanks

26771 KL

7 tanks

- 26771

KL

7 tanks

Motor

Spirit

2 HSD BS-IV Existing: 5 tanks

Proposed: 2

23019 KL

5 tanks

16000 KL

2 tanks

39019

KL

Diesel

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tanks 7 tanks

3 SKO Existing: 1 tank

5639 KL

1 tank

- 5639

KL

1 tank

Kerosene

4 LSHFHSD Existing: 2 tanks

1798 KL

2 tanks

- 1798

KL

2 tanks

High

Speed

Diesel

5 Ethanol Existing: 8 tanks

499 KL

8 tanks

- 499 KL

8 tanks

Ethanol

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

2006.



Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: Not Applicable

Proposed:12 crores

Total: 12 crores

B Total Plot area

( sq. meter)

Existing: 125 acre (505857 sq. m)

Proposed: Nil

Total: 125 acre (505857 sq. m)


( sq. meter)

Existing: 13.2 acre (53418.5 sq. m)

Proposed: Nil

Total: 13.2 acre (53418.5 sq. m)

C Employment generation Existing: 41

Proposed: Nil

Total: 41

D Water

i

Source of Water Supply (GIDC Bore well, Surface

water, Tanker supply etc...)

Water thru pipeline from Singapore Weir of

KRBC Division, Surat.

Status of permission from the concern authority.

Permission taken.

ii


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Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 21 Nil 21

(B) Gardening - - -

Industrial

Process - - -

Washing 5 - 5

Boiler - - -

Cooling - - -

Others - - -

Industrial Total 26 - 26

Grand Total (A+B+C) 26 - 26

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

existing water supply)

2) Quantity to be recycle: 21 KLD

3) Total fresh water requirement: 21 KLD

iii


Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 17 - 17

Industrial

Process - - -

Washing 3 Intermittent 3

Boiler - - -

Cooling - - -

Others - - -

Total Industrial

waste water

20 - 20

-

iv Treatment facility within premises with capacity

[ETP (Primary, Secondary, Tertiary), MEE, Stripper,

ETP of 10 m3/hr capacity

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Spray Dryer, STP etc].

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

Industrial: treated effluent will be used

in gardening of the terminal

vi In case of Common facility (CF) like CETP, Common

Spray dryer, Common MEE etc. , name of CF

Not Applicable

Membership of CF Not Applicable

vii Reuse/Recycle details (KLD) 20 KLD

E Air [Existing & Proposed]



Average Diesel consumption in the terminal is 165 Litre/Day.

SR.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1 DG-500 KVA 8 M HSD 85

Litre/Hr SOx, NOx

Acoustic

enclosures

2 DG-500 KVA 8 M

HSD 85

Litre/Hr SOx, NOx

Acoustic

enclosures

3 DG-500 KVA 8 M HSD 85

Litre/Hr

SOx, NOx Acoustic

enclosures

4 DG-380 KVA 8 M HSD 80

Litre/Hr

SOx, NOx Acoustic

enclosures

5 Fire Engine-

480 HP 8 M HSD

80

Litre/Hr SO2, NOx -

6 Fire Engine-

480 HP 8 M HSD

80

Litre/Hr SO2, NOx -

7 Fire Engine-

480 HP 8 M HSD

80

Litre/Hr SO2, NOx -

8 Fire Engine-

480 HP 8 M HSD

80

Litre/Hr SO2, NOx -

9 Fire Engine-

480 HP 8 M HSD

80

Litre/Hr SO2, NOx -

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-

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


Sr. no. Source of

emission

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution

Control

Measures

(APCM)

1 DG Stack SOx,

NOx

As per serial

no E(i)

As per Serial no

E(i)

-


[Existing & Proposed]GAs below:

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

be taken.

iv VOC emission sources and its mitigation measures

Proposed HSD tanks are tanks are Cone Roof Tanks. Only one tank will be operated for receipt

at one time as per present practice. Therefore there will not be any increase in quantity of

emission from present limit.

F Hazardous waste (as per the Hazardous and Other Wastes (Management and Transboundary

Movement) Rules 2016.


i

Sr.

no.

Type/Name of

Hazardous

waste

Source of

generation

Category and

Schedule as

per HW Rules.

Quantity

(MT/Annum)

Disposal Method

1 ETP Waste ETP 34.3 18 KL/Year TSDF

2 Used Oil DG sets 5.1 0.950 MT/Year Registered

re-processors

3 Oil residue Pumps 3.1 0.750 MT/Year Registered

re-processors

4 Discarded

container

Oil

container

33.3 120 nos./year Authorized

recyclers

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Quantity of discarded containers must be in MT/Annum.

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

iii Details of Non-Hazardous waste & its disposal

(MSW and others)

Nil


• At present unit is engaged in isolated storage and handling of Hazardous chemicals for which they

have obtained CC&A of the Board. The proposal is for expansion of isolated storage and handling of

Hazardous chemicals.


Observation:

• This proposal is for expansion of existing unit and for now proposes isolated storage and handling of

Hazardous chemicals. This unit is having valid CC&A for existing unit. Copy of CC&A, CC&A



• Total water consumption will be 21 KLD. Total wastewater generation will be 20 KLD. After proposed

expansion, there will be no change in industrial and domestic waste water generation i.e. 20 KLD.

• 20 KLD treated effluent will be used for gardening purpose within premises..

• HSD will be used as fuel for DG set and fire engine..




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

March, 2018. Risk assessment including prediction of the worst-case scenario and maximum credible

accident scenarios has been carried out. The detail proposed safeguard measures including On-Site

/ Off-Site Emergency Plan has been covered in the RA report.


• Committee noted that proposal is for enhancement of the storage tank capacity for HSD. It is noted

that two additional tanks of HSD each of 8000 KL (Total capacity of 16000 KL) are proposed to be

installed. Committee noted that TOR was issued by SEIAA vide letter No:

SEIAA/GUJ/TOR/6(b)/893/2018 dated 28/08/2018 including exemption of public hearing.

• Considering the proposed expansion, compliance of CCA conditions, action under various

environmental rules/acts by GPCB, public compliant/litigation pending against the unit were

discussed at length. Committee also deliberated safety measures proposed by the unit for the

additional tanks as well as for the existing facilities.

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1. Detailed safety measures including SOP being implemented for existing facilities and also for the

proposed tanks for HSD to prevent accidents.


3. Revised environmental management plan (EMP) with budgetary provision of capital cost and recurring

cost after incorporating additional environmental mitigation measures.

8. SIA/GJ/IND2/19407/2017 M/s. Grasim Industries Ltd

Plot No. -1, GIDC Industrial Estate, P.O.-

Vilayat, Taluka-Vagra, District-Bharuch.

Appraisal

Project / Activity No.: 1(d)


• PP has submitted online application vide no. SIA/GJ/IND2/19407/2017 of dated 11/07/2017 for


• SEIAA has issued TOR to PP vide letter No: SEIAA/GUJ/TOR/1(d)/890/2017 vide dated 29-09-2017.

• Project proponent has submitted EIA Report prepared by M/s Anand Environnemental Consultants

Pvt. Ltd based on the TOR issued by SEIAA.

• This is an expansion unit and proposes for expansion of thermal power plant as tabulated below:

Sr.

No.

Name of Product CAS

no.

Quantity

MT/Month

End-use of product

Existing Proposed Total

1. Captive Power Plant

(CPP)

-- 96

MW

45

MW

141

MW

Power Generation

for self use

By-Product

NIL

• The project falls under Category B of project activity 1(d) as per the schedule of EIA Notification

2006.



Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: 500 Crores

Proposed: 250 Crores

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Total: 750 Crores

B Total Plot area

( sq. meter)

Existing: 350000 sq. m

Proposed: 69750 sq. m

Total: 419750 sq. m


( sq. meter)

Existing: 115500 sq. m

Proposed: 23017.5 sq. m

Total: 138517.5sq. m

C Employment generation

Existing:

Proposed:

Total:

Direct

110

30

140

Indirect

--

20

20

D Water

i



GIDC

Status of permission from the concern authority. Yes

ii


Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 5.5 2.5 8

(B) Gardening

* * *

* Treated domestic

wastewater will be used

for gardening

(C) Industrial

Process -- -- --

Washing 50 25 75**

Boiler 6450 3100 9550 Boiler make up water

Cooling 4000 1875 5875 Cooling make up water

Others 750 500 1250 DM water regeneration

Industrial Total 11250 5500 16750

Grand Total

(A+B+C) 11255.5 5502.5 16758

**Wash water includes Air pressure preheater/Plant wash down water/floor washing and equipment

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drain/grey water washing /seepage of ash water/bottom ash handling system

1) Total water requirement for the project: 16758KLD

2) Quantity to be recycle: 11642 KLD& 1443 KLD reuse

3) Total fresh water requirement: 5116KLD

iii


Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 4.4 2 6.4

(B) Industrial

Process 0 0 0

Washing 50 25 75

Boiler 2500 1180 3680 Boiler blow down

Cooling 1500 710 2210 Cooling purge

Others 750 500 1250 DM water regeneration

Total Industrial waste

water 4800 2415 7215

Grand Total (A+B) 4804.4 2417 7221.4

-

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

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

• Effluent generated from industry will be treated in our existing effluent treatment plant (capacity-

500 m3/day x2)

Treated effluent will be reused for cooling make-up and RO reject will be used for Dust

suppression in coal handling area, Sprinkling on fly ash, road cleaning.

• Domestic sewage will be treated in STP and treated wastewater will be reused for gardening

within premises.


Domestic: GIDC -drainage line ultimately disposal into deep sea.

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Industrial: Zero discharge

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

Name of Common facility

Not applicable, since our Effluent generated from industry and domestic will be treated in our

existing effluent treatment plant

Membership of Common facility (CF)

Not applicable, since our Effluent generated from industry and domestic will be treated in our

existing effluent treatment plant

vii Reuse/Recycle details (KLD)

5870 kl/day steam condensate will be recycled back for boiler make-up, 5772 kl/day treated

wastewater will be recycled for cooling make-up and 1443 kl/day RO reject will be reused for Dust

suppression in coal handling area, sprinkling on fly ash and road cleaning.

70% reduction in fresh water consumption by various recycle and reuse of treated wastewater

E Air



Existing & Proposed

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Name

of the

fuel

Quantity

of Fuel

MT/hr&

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

Existing*

1. Boiler 1 & 2

(2 x 175 TPH)

125 Coal

100

MT/hr

SPM

SO2

NOx

ESP and Low

NOx burners

2. Boiler 3 & 4

(2 x 175 TPH)

125 SPM

SO2

NOx

ESP and Low

NOx burners

Proposed

3. Boiler-5 125 Coal 29.16M SPM ESP and Low

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(175 TPH) T/hr SO2

NOx

NOx burners

-

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

Existing & Proposed

-

Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height (meter)

Air Pollution

Control Measures

(APCM)

1 Not Applicable

-


All possible preventive measure taken to control / minimize the Fugitive emissions

F Hazardous waste

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

2016.

Existing & Proposed

i

Sr.

No.

Type/Name

of

Hazardous

waste

Source of

generation

Category

and

Schedule

as per

HW

Rules.

Quantity

(MT/Annum)

Mode of Disposal**

Existing Proposed Total

1. ETP

Sludge

ETP 35.3 5

MT

2.5

MT

7.5

MT

Collected, stored, transported

& disposed at TSDF site of

BEIL.

2. Spent

Resin

ETP 35.2 0.33

MT

0.09

MT

0.42

MT

Collected, stored, transported

& disposed at TSDF site of

BEIL.

3. Used Manufacturing 33.1 0.54 MT 0.96 MT 1.5 Will be collected, stored and

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Drums process MT reused /sold to authorized

recycler Liners /

PPBags

0.84 MT 1.16 MT 2.0

MT

4. Used Oil From process 5.1 100 kl 28 kl 128 kl Collected, stored and sold to

authorize recycler.

5. Fly Ash/

bed Ash

From Boiler -- 86400

MT

25200

MT

11160

0 MT

Fly ash/ Bed ash sold to M/s.

Anmol&Co. J.K. Lakshmi

Cement, Ambuja.

-

ii Membership details of TSDF, CHWIF etc.

We have membership of BEIL-Dahej for TSDF


disposal(MSW and others)

Waste:Fly Ash/ Bed Ash

Existing- 86400 MT/Annum

Proposed 25200 MT/Annum

Disposal: Fly ash/ Bed ash sold to M/s. Anmol& Co.

J.K. Lakshmi Cement, Ambuja.

G Solvent management, VOC emissions etc.

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

• Not applicable

ii VOC emission sources and its mitigation measures

• Not applicable


• At present unit is engaged in thermal power plant for which they have obtained EC and CC&A of the

Board. The proposal is for expansion of thermal power plant.


Observation:

• This proposal is for expansion of existing unit and for now proposes thermal power plant. This unit is

having valid EC and CC&A for existing unit. Copy of EC, CC&A, EC compliance and CC&A



• Total water consumption will be 16758KLD. Total wastewater generation will be 7215 KLD. After

proposed expansion, waste water will be treated in ETP and RO plant and treated effluent completely

of 48


Page 19 of 48

reused back in plant.

• 5870 kl/day steam condensate will be recycled back for boiler make-up, 5772 kl/day treated

wastewater will be recycled for cooling make-up and 1443 kl/day RO reject will be reused for Dust

suppression in coal handling area, sprinkling on fly ash and road cleaning.

• Coal will be used as fuel for proposed and existing boilers.

• Adequate APCM will be installed with boilers and lime along with coal used as fuel for SO2 emission

control.




been conducted for the study area of 5 km/10 km radial distance from project site for the period

October-December 2015. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2,

NOx, CO and VOC at six locations, including the project site. Values conform to the prescribed

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

computed using AERMOD. The resultant concentrations are within the NAAQS. The modeling study

proved that the air emissions from the proposed plant would not affect the ambient air quality of the

region in any significant manner. The ambient air quality around the proposed project site will remain

within the National Ambient Air Quality Standards (NAAQS).

• Risk assessment including prediction of the worst-case scenario and maximum credible accident

scenarios has been carried out. The detail proposed safeguard measures including On-Site / Off-Site

Emergency Plan has been covered in the RA report.


• It is noted that proposal is for expansion. PP addressed compliance monitoring of environmental

conditions of RO-Bhopal. Referring to the compliance, it is noted that 14 conditions are partially

complied, 4 conditions are not complied and 3 conditions are not responded. Committee deliberated

compliance of EC conditions monitored by the RO-Bhopal, MOEF&CC at length and asked PP to

submit the fresh compliance report of EC conditions with all corrective action in context to the

observation of RO-Bhopal.

• It is further noted that for the foul odor of CS2 and H2S, GPCB has taken action. Committee asked

PP to submit all the measures implemented to curb the foul odor of H2S and CS2 with technical

details.

• Committee noted that PP has not satisfactorily addressed issues raised during the public hearing and

asked PP to identify the issues in detail raised during public hearing and make action plan to redress

the issues. It is further mentioned that activities required for taking mitigation measures for the

redressing public complaints shall be incorporated in the EMP along with its budgetary provision.

of 48


Page 20 of 48



1. To explore air cooling technology in place of water cooling system for proposed power plant

expansion that required additional 1875 KLPD of water for cooling tower make up.

2. To address quantity distribution of treated waste water (RO-Reject stream) for its utilization at (1)Dust

Suppression to coal handling area (2) Sprinkling on fly ash (3) Road Cleaning and waste water

management generating from road cleaning.

3. Fugitive emission control action plan due to proposed expansion for coal storage having existing load

of 72000 MTPM and additional load of 21000 MTPM keeping standing coal inventory in view.

4. Detailed EMP with activity and sub component based capital and recurring cost.


6. To re-identify issues raised during public hearing and make action plan to redress the issues.

Address activities required for taking mitigation measures for the redressing public complaints and

submit detailed action plan for its implementation.

7. Submit revised CSR addressing measures taken for issues raised during public hearing and its

implementation plan.

8. Submit revised EMP with additional environmental mitigation measures arising due to redressal of

public complaint/ issues raised during public hearing with details of budgetary provision.

9. SIA/GJ/IND2/28046/2018 M/s. Grasim Industries Ltd. (Chemical

Division)

Plot No.-1, GIDC-Vilayat, Taluka -Vagra,

District-Bharuch, 392 140 Gujarat

Screening and scoping

Project / Activity No.: 5(f)


• This office has received an application vide their online proposal no. SIA/GJ/IND2/28046/2018 dated

21/09/2018 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.

• Project proponent (PP) has submitted Form-1, PFR and relevant details/information.

• This is an expansion unit proposes for Synthetic Organic Chemicals manufacturing plant as tabulated

below:

Sr. Name of the CAS no. / Quantity (MT/Month) End-use of the products

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Page 21 of 48

no. Products CI no. Existing Proposed Total

Epichlorohydrin (ECH)

1 Epichlorohydrin 78-93-3 0.0 100000 100000 Epoxy Resins, Synthetic

Glycerine, Water Treatment

Chemicals, Pharmaceuticals

2 Hydrochloric

acid (20%

Technical grade)

as 20%

7647-01-0 0.0 10000 10000 Hydrochloric acid is often

used as a descaling agent.

3 NaCl (20%) 7647-14-5 0.0 172400 172400

4 Refined Glycerin

(75%)

56-81-5 0.0 40000 40000 Glycerine is being used in

pharmaceutical applications,

Chlorinated Poly Vinyl Chloride (CPVC)

5 CPVC 68648-82-8 0.0 100000 100000 Hydronic piping and

distribution (radiators, fan

coils, etc.)

Suitable for many industrial

and process piping

applications

6 Hydrochloric

acid

7647-01-0 0.0 23004 23004 Hydrochloric acid is often

used as a desca ing

agen

poxy Plant

7 Liquid Epoxy

Resin

25068-38-6

101747

100000

201747

� High solids and

solvent free coatings

� Adhesives

� Civil engineering and

construction industry

� Automotive coatings

� Intermediate for can &

coil coatings

� Marine and Industrial

protective coatings

� Tooling, potting,

8 Formulated

Resin

25068-38-6

9 Powder Coating

25036-25-

3

10 Can Coating

Resin

25036-25-3

11 Solution Cut

Resins

1330-20-7

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Page 22 of 48

casting and moulding

compounds

� Composites

Stabilizer in PVC

12 Hardeners 2855-13-2 14000 10000 24000 � High Chemical resistance

flooring/grouting

In adhesive

� Laminations

� Marine Coating

� Patch repair

� Off shore

primers/top

coatings.

� Chemical

resistance mortar.

� Concrete

Impregnation.

Crack injection system

13 Reactive

diluents

2425-79-8 7350 5000 12350 � Filament winding,

laminating,

� Vacuum pressure

impregnation

� Civil engineering

� Electronic

encapsulations

14 Salt 7647-14-5 40000 33677 73677 Dyeing industries

15 Hydrochloric

acid (20%)

7647-01-0 0 1000 1000 --

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


• The project proponent along with their expert /consultant M/s Anand Environmental Consultants

Pvt. Ltd attended the meeting and made presentation before the committee


Sr. Particulars Details

of 48


Page 23 of 48

no.


(Rs. in Crores):

Existing: 453 Cr.

Proposed: 1085 Cr.

Total: 1538 Cr.

B Total Plot area

( sq. meter)

Existing: 141953.58Sq. m.

Proposed: 36557.42Sq. m.

Total: 178511Sq. m.


( sq. meter)

Existing: GG.Sq. m.

Proposed: GG.Sq. m.

Total: It may be noted that total

area of Grasim Industries Ltd. If

567 acres out of which 33% will be

developed as greenbelt area

C Employment generation Existing:212

Proposed:581

Total:793

D Water

i

Source of Water Supply

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

GIDC

Status of permission from the concern authority.

ii Water consumption (KLD)

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 102 25.6 127.6

(B) Gardening 100 30 130

(C) Industrial

Process 656

890 1546 It may be noted that out of

1546 kl/day of total water

consist of 1037 kl/day

recycled water from

caustic & reaction water +

Steam condensate + DM

water and 509 kl/day is

fresh water

Washing 0 220 220

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Page 24 of 48

Boiler 0 0 0

Cooling 800 1235 2035

Others 0 285 2085

Industrial Total 1456 2630 4086

Grand Total (A+B+C) 1658 2685.6 4343.6

1) Total water requirement for the project: 4343.6 KLD

2) Quantity to be recycle: 1841.4KLD

3) Total fresh water requirement: 2502.2KLD

iii Waste water generation (KLD)

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 85 24 109

(B) Industrial

Process 373 335 708

Washing 0 220 220

Boiler 0 0 0

Cooling 384 430 814

Others 0 95 95

Total Industrial waste water 757 1080 1837

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

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

Existing ETP (Primary, Secondary, Tertiary) –850 M3/day and MEE - 320 M3/day for final

treatment of effluent/sewage generation 842 from existing epoxy plant

Proposed ETP – 500 kl/day capacity for treatment of 350 kl/day effluent/sewage generation from

Proposed Epoxy Plant

Proposed RO plant (750 kl/day) followed by MEE (300 kl/day)for 750 kl/day effluent generation

from proposed ECH and CPVC plant


Domestic:

Domestic sewage generated (105 kl/day) from existing and proposed epoxy plant

will be treated in above stated Existing and Proposed effluent treatment plants.

And finally discharged through underground dahej-Vilayat pipeline.

Sewage generated (4.4 kl/day) form CPCV & ECH plant will be treated in STP.

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Page 25 of 48

Treated wastewater will be used for gardening purposes within premises.

Industrial:

Industrial Effluent from epoxy plant (existing & proposed) will be treated in ETP

and treated water will be discharged to Dahej –Vilayat underground pipeline.

Effluent from ECH & CPVC plant will be Zero Discharge.

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

Name of Common facility

Not applicable


Not applicable

vii Reuse/Recycle details (KLD)

Not applicable

E Air



Existing & Proposed

- Existing

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1 D.G. Set

(2000 kVA) 30 HSD

27

Lit/Day

PM

SO2

NOx

Not

Applicable

- Proposed

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1 Incinerator 36 Hydro

gen

200

Nm3/Hr

PM

SO2

NOx

HCl

Caustic

Scrubber

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Page 26 of 48

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

Existing & Proposed

- Existing

Sr.

no. Source of emission

Type of

emission

Stack/Vent

Height

(meter)


Measures

(APCM)

1

ISBL ECH Tank

[Liquid Epoxy Resin Plant

(ECH Vent)]

VOC 30

Guard Condenser,

Scrubber, PRV, Flame

Arrester

2

ISBL Toluene Tank

[Liquid Epoxy Resin Plant

(Toluene Vent)]

VOC 30 Guard Condenser, PVRV,

(Integrated Flame Arrester)

3

OSBL ECH Tank

[Liquid Epoxy Resin tank

(ECH Vent)]

VOC 10 Scrubber, PRV ,Flame

arrestor

4

PESO Toluene Tank

[Liquid EPOXY Resin Tank

(Toluene Vent)]

VOC 10 Underground tank, PVRV

(Integrated flame arrestor)

5

Toluene Tank

[Reactive Diluents Plant

(Toluene) ]



6 Reactor

[Solution Cut Plant (Xylene) ]



7

Solution Cut Tank

[Solution Cut Tank Farm

(Xylene)]

VOC 10 PVRV, (Integrated Flame

Arrester)

8

Peso Xylene Tank

[Xylene Tank (PESO Tank

Farm)]

VOC 10 Underground tank, PVRV

(Integrated flame arrestor)

- Proposed

Sr.

no. Source of emission

Type of

emission

Stack/Vent

Height

(meter)


Measures

(APCM)

1 HCl Vent Scrubber HCl 14 Scrubber

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Page 27 of 48

[Emergency vent Scrubber] Cl2

2

HCl synthesis

HCl 30

Absorption Tower using

water as an absorption

media

3 CPVC Reactor and

Degassing Vessel Cl2 12 Alkaline Scrubber

4 PVC Conveying to Silo

Cl2 25 Bag Filter

5 PVC Conveying to Oxygen

PM 10 Bag Filter

6 Degassing

PM 35 Bag Filter

7 Conveying-Degassing

Vessel to Hopper PM 25 Bag Filter

8 Evacuation of air

PM 10 Bag Filter

9 Conveying CPVC from PVC

Reactor PM 25 Bag Filter


--

F Hazardous waste


2016.

Existing & Proposed

i

Sr.

no.

Type/Name

of

Hazardous

waste

Source of

generation

Category

and

Schedule

as per

HW

Rules.

Quantity

(MT/Annum)

Disposal Method

Existin

g

Propos

ed

Total

1 Waste

Residues

(Not made

From

Manufactu

ring

I-23.1 560 927 1487 Collection, storage,

transportation ,

disposal at Ambuja

of 48


Page 28 of 48

with animal

or

vegetable

material)

Process Cement Ltd. for

pre-processing, co-

processing/

incineration

2 Chemical

Sludge

from

wastewater

treatment

ETP I-35.3 2025 1200 3225 Collection, storage,

transportation,

disposal of landfill

waste at TSDF and

incinerable waste by

pre-processing, co-

processing/

incineration

3 Discarded

containers/

bags/ liners

contaminat

ed with

hazardous

waste/che

micals

From

Manufactu

ring


transportation,

disposal by selling to

authorized vendors.

4 Used or

Spent Oil

From

Lubricatio

n or

D.G.Set


transportation,


registered recycler

5 Waste or

residue

containing

oil


transportation,


registered recycler

6 Incinerator

waste/

residue


transportation,


waste at TSDF

7. MEE

residue


transportation,


waste at TSDF

of 48


Page 29 of 48

-

ii Membership details of TSDF, CHWIF etc. BEIL, SEPPL, RSPL, HELP


disposal(MSW and others)

NaCl (Salt ) from MEE (Epoxy plant)will be

used as product

G Solvent management, VOC emissions etc.

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

• Toluene - Falling Film Evaporator - 100% recovery, 100% Re-use

• Xylene - Production process - 100% consumption in plant

ii VOC emission sources and its mitigation measures

• Toluene, Xylene and ECH Process - Guard Condensers and Scrubbers



Observation:

• This proposal is for expansion of existing unit and for now proposes a new synthetic organic chemical

product. This unit is having valid EC and CC&A for existing unit. Copy of EC, CC&A, Ec and CC&A



• Total water consumption will be 4343.6 KLD. Total wastewater generation will be 1837 KLD. After

proposed expansion, effluent will be treated in ETP, RO plant and MEE plant. Treated effluent from

Epoxy plant ETP and STP will be discharged in Dahej-Vilayat pipeline.

• Treated effluent from ECH & CPVC plant ETP will be evaporated in MEE after ETP and RO

treatment.

• 1841.4 KLD treated effluent will be reused back in process.

• Hydrogen will be used as fuel for incinerator.

• APCM like caustic scrubber will be provided for proposed incinerator.

• Adequate APCM will be provided with each plant reactors stack.



• Committee noted that proposal is for TOR expansion. Referring to the compliance status of the

existing EC/CCA conditions, action by GPCB, details of public litigation and complaints, project

proponent could explain details with brief summary of compliance. It is also noted that existing

products along with proposed product profile is not addressed with clarity. Committee noted that

proposed production is in increasing in manifold compared to existing with increase in waste water

from 757 KLPD to 1837 KLPD.

• Considering that project proponent could not explain compliance status of EC/CCA with need of

of 48


Page 30 of 48

expansion, fresh water consumption, waste water generation, committee unanimously decided to ask

PP to represent the proposal again to the committee with details of summarized compliance status of

EC/CCA, measures to optimize fresh water consumption and to bring down the waste water

generation for the proposed products along with justification of extent of expansion for the proposed

products.

After deliberation, it was decided to defer the proposal in one of the upcoming SEAC meeting for

presentation considering aforementioned details.

10. SIA/GJ/IND2/28783/2015 M/s. Ami Organics Ltd

Plot No. 440-4/5/6 and 8206/B, Road No. 82,

GIDC Sachin, Ta.: Chorasi,

Sachin-394230, Dist.: Surat, Gujarat

EC-amendment

Project / Activity No.: 5(f)


• This office has received an application vide their online proposal no. SIA/GJ/IND2/28783/2015 dated

25/09/2018 regarding grant of amendment in Environmental Clearance.

• This is an existing synthetic Organic Chemical manufacturing unit which was accorded Environmental

Clearance vide letter no. SEIAA/GUJ/EC/5(f)/3078/2015 dated 21/08/2015.

• Details regarding proposed changes in Environmental Clearance vide letter no.

SEIAA/GUJ/EC/5(f)/3078/2015 dated 21/08/2015 as follows :

Sr.

no.

Condition no. in

which changes

proposed.

As per EC As per proposed

amendment

Justification

1 Water: point no.

9 and 10 in EC

(Way of

Disposal)

9. The RO

permeate (44 KL)

shall be reused,

whereas RO

reject (17 KL)

shall be fed to the

MEE (Multiple

Effect

Evaporator).

10. High COD

After treatment through

RO, permeate (44 KLD)

will be Recycled back to

plant and RO reject (17

KLD) will be either sent to

Common Facility of

MEPPL or will be treated

into in-house Evaporator.

4 KLD High COD solvent

bearing stream shall be

The facility is in

operation since

long time and it

requires regular

maintenance.

Also due to regular

maintenance of

evaporation plant,

it is required to

send this 20 KLD

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Page 31 of 48

Solvent Bearing

Stream shall be

stripped by using

steam in steam

stripping column

to recover the

solvent and the

rest shall be sent

to MEE.

treated in stripper and

outlet from stripper will be

either sent to Common

Facility of MEPPL or will

be treated into in-house

Evaporator.

concentrated

stream to common

facility of ‘MEPPL’.

• The project proponent requested for amendment in Environmental Clearance order as above.

• This is an existing unit engaged in Synthetic Organic Chemicals and EC obtained from SEIAA,

Gujarat with the products listed as tabulated below:

Sr.

No. Product Name CAS No. Capacity

1 4-Hydroxy Cumerine 1076-38-6

50 MT/Month

(Total 67 no of

products)

2. Dimethyl Formamide Dimethyl Acetal 4637-24-5

3. 1-(2,3-dichloro phenyl) piperazine HCL 119532-26-2

4. 1-(3-chlorophenyl) piperazine HCL 13078-15-4

5. 1- phenyl piperazine 92-54-6

6. 1-[2-(2-hydroxy ethoxy)ethyl]piperazine 13349-82-1]

7. Trimethyl Ortho Benzoate 707-07-3

8. 1-methyl-3-phenyl piperazine 5271-27-2

9. Trialkyl Ortho Alkolates 53568-66-4

10 1, 2-benzisoxazol-3-yl acetic acid 4865-84-3

11 4-Bromo -1-Methyl-1H-Pyrazole 583-70-0

12 1-methyl-4-piperidone 1445-73-4

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Page 32 of 48

13 2,4-thiazolidinedione 2295-31-0

14 2,6-difluoro benzyl chloride 697-73-4

15 1-(2-hydroxy ethyl) pyrrolidine 2955-88-6

16 3-(Piperazine-1-yl)-1, 2-benzothiazole 87691-87-0

17 3-MORPHOLIN-4-YL-1-(4-NITROPHENYL)-5,6-

DIHYDROPYRIDIN-2(1H)-ONE 503615-03-0

18 4-[1, 2, 4-triazolo-1-yl] methyl phenyl hydrazine 212248-62-9

19 4 – HYDROXY COUMARIN (HC) 1076-38-6

20 5,6- Dimethoxy Indanone (5,6-DMI) 2107-69-9

21 AMINO ACETALDEHYDE DIMETHYL ACETAL

(AADMA)

22483

-09-6

22 1-ALKYL PIPERAZINE

i. 1-Allyl Piperazine

ii. 1-Formyl Piperazine

iii. 1-Carbethoxy Piperazine

iv. 1-Acetyl Piperazine

v. 1 - (3-Chloro propyl)piperazine

vi. 1-Benzyl Piperzaine

vii. 1-(Furoyl)piperazine

viii. 1-(Tetrahydrofuroyl)piperazine

ix. 1-Benzoyl Piperazine

x. 1-Cinnamyl Piperazine

xi. 1-BOC piperazine

xii. 1-CBZ Piperazine

xiii. 1-Isopropyl Piperazine

xiv. 1-Cylco pentyl Piperazine

xv. 1-Cyclo Butyl Piperazine

xvi. 1-Cyclo propyl piperazine

xvii. 1-Cyclo propyl methyl piperazine

xviii. 1-Benzyloxy ethyl piperazine

-

23 1 – Methyl – 3 – Phenyl Piperazine 5271-27-2

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Page 33 of 48

24 1-ARYL PIPERAZINE

i. 1-(3-Chloro Phenyl )Piperazine

ii. 1-(2-Chloro Phenyl)piperazine

iii. 1-(4-Chloro Phenyl )Piperazine

iv. 1-(2,3-DiChloro Phenyl )Piperazine

v. 1-(3,4-DiChloro Phenyl )Piperazine

vi. 1-(2,6-DiChloro Phenyl )Piperazine

vii. 1-(2-Methoxy Phenyl )Piperazine

viii. 1-(3-Methoxy Phenyl )Piperazine

ix. 1-(4-Methoxy Phenyl )Piperazine

x. 1-(2-Hydroxy Phenyl )Piperazine

xi. 1-(3-Hydroxy Phenyl )Piperazine

xii. 1-(4-Hydroxy Phenyl )Piperazine

xiii. 1-(2-Bromo Phenyl )Piperazine

xiv. 1-(3-Bromo Phenyl )Piperazine

xv. 1-(4- Bromo Phenyl )Piperazine

xvi. 1-(2-Nitro Phenyl )Piperazine

xvii. 1-(3-Ntiro Phenyl )Piperazine

xviii. 1-(4-Ntiro Phenyl )Piperazine

xix. 1-Phenyl Piperazine

xx. 1-(3-Trifluoro Phenyl)Piperazine

xxi. N-(3,4-METHYL ENEDIOXY PHENYL)

PIPERAZINE

xxii. N-(2,4-DIMETHOXY PHENYL)

PIPERAZINE

xxiii. 1-(3,4-DIMETHOXY PHENYL)

PIPERAZINE

xxiv. 1-(3-Fluoro Phenyl )Piperazine

xxv. 1-(2-Fluoro Phenyl)pIperazine

xxvi. 1-(4-Fluoro Phenyl )Piperazine

xxvii. 1-(3-Tollyl )Piperazine

xxviii. 1-(2-Tollyl )Piperazine

xxix. 1-(4-Indolyl)piperazine

xxx. 1-Cyclohexyl piperazine

xxxi. 1-(2-Pyridyl)-piperazine

xxxii. 1-Pyridin-4-yl-piperazine

-

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Page 34 of 48

xxxiii. 1-(2-Cyanophenyl)piperazine

xxxiv. 1-(4-Iodo-phenyl)-piperazine

xxxv. 1-(3-nitro-2-pyridyl)piperazine

xxxvi. 1-(2-Pyrimidyl) Piperazine

25 4-hydrzino benzene sulphonamide 17852-52-7

26 4-(methyl amino)-3-nitrobenzoic acid 41263-74-5

27 ethyl 3-(pyridin-2-ylamino)propanoate 103041-38-9

28 dibenzo[b,f][1,4]thiazepin-11(10H)-one 3159-07-7

29 N, N-Dimethyl Formamide Dimethyl Acetal 4637-24-5

30

Ethyl 1-(4-methoxyphenyl)-6-(4-nitrophenyl)-7-oxo-

4,5,6,7-tetra hydro-1H-pyrazolo[3,4-c] pyridine-3-

carboxylate

536759-91-8

31 Ethyl (4-amino-2-nitrophenyl) carbamate 73895-87-1

32 Ethyl (4-aminophenyl) carbamate 57399-97-0

33 Ethyl (4-nitrophenyl) carbamate 2621-73-0

34 Ethyl{4-[4-fluorobenzyl]amino}-2-

nitrophenyl}carbamate 150812-23-0

35 ETHYLCHLORO[(4-METHOXY

PHENYL)HYDRAZONO]ACETATE 27143-07-3

36 1 – (3 – CHLORO PHENYL) – 4 – (3 – CHLORO

PROPYL) PIPERAZINE HCl (ECPH) 52605-52-4

37 1-[2-(2-HYDROXY ETHOXY) ETHYL]

PIPERAZINE 13349-82-1

38 Ibandronic Acid 114084-78-5

39 Methyl Cyclobutane carboxylate 765-85-5

40 S-(2, 3-epoxypropyl) Phthalamide 161596-47-0

41 2H-[1,2,4]-TRIAZOLO-[4,3-a]-Pyridine (124TPO) 6969-71-7

42 ETHYL 5- NITROBENZOFURAN-2-

CARBOXYLATE 69604-00-8

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Page 35 of 48

43 ETHYL-5- AMINOBENZOFURAN-2-


44 ETHYL-5- PIPERAZINYL BENZOFURAN-2-


45 1-(2, 6-dichlorophenyl) indoline-2-one 15362-40-0

46 1-(4-methylphenyl)-4,4,4-triflurobutane-1,3-dione 720-94-5

47 1-Benzyl-4-piperidone 3612-20-2

48 1-Boc-3-piperidone 98977-36-7

49 1-Boc-4-piperidone 79099-07-3

50 1-Hydroxy benzotriazole 2592-95-2

51 3-CHLORO-1-(4-NITROPHENYL)-5,6-

DIHYDROPYRIDIN-2(1H)-ONE 536760-29-9

52 3-methoxy propiophinone 37951-49-8

53 4-(2-chloroethyl) morpholine 3647-69-6

54 4-(4-aminophenyl) morpholin-3-one 438056-69-0

55 4-chloro butyraldehyde dimethyl acetal 29882-07-3

56 Cyclohexane Carboxaldehyde 2043-61-0

57 1-(4-Rphenyl)-2-piperidone -

58 2-PIPERIDONE(2-PD) 675-20-7

59 N-Boc-2-PIPERIDONE 85908-96-9

60 3, 4 – DIHYDROXY – 5 – NITRO

BENZALDEHYDE (3,4DH5NBZ) 116313-85-0

61 N-Methyl amino Acetaldehyde Dimethyl Acetal 122-07-6

62 2-(chloromethyl)-4- methyl quinzoline

109113-72-6

63 4-cyano-4-(4-fluorophenyl) cyclohexan-1-one. 56326-98-8

64 5-(2-Methoxyphenoxy)-2,2’-bipyrimidine- 150728-12-4

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Page 36 of 48

4,6(1H,5H)-dione

65 Bromo acetaldehyde diethyl acetal 2032-35-1

66 Diethyl (2-methoxy phenoxy) malonate 20730-58-9

67 Methyl di-(2-thienyl)glycolate 26447-85-8

BY PRODUCTS NAME AND CAPACITY

1 1-(2-Hydroxy ethyl) piperazine 103-76-4 14 MT/Month

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


• During the meeting dated 29/10/2018, technical presentation made during the meeting by project

proponent.


Sr.

no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): There will be no increase in project cost.

Capital cost for EMS (Environmental Management System): - No Changes as amendment is only

for way of disposal of effluent

Recurring cost towards the environmental protection measures: No changes.

B Total Plot area ( sq. meter) 8250 sq. m.

Green belt area/Tree Plantation area ( sq. meter) 2500 sq. m.

C Employment generation

Direct No additional manpower will be require as

amendment is only for change in mode of

effluent disposal.

Indirect

Total

D Water

i



The water requirement of this project is

69.5 KLD and will be supply by Sachin

Infra Management Ltd.

No change in water consumption due to

proposed EC Amendment.

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Page 37 of 48

Status of permission from the concern authority. Not Applicable as there is no expansion.

ii


Existing which will remain same

Sr. No. Purpose Ultimate (KLD)

1 Domestic 10

2 Industrial 59.5

(A) Processing 44.5

(B) Boiler feed

15 (C) Cooling make up

(D) Miscellaneous

TOTAL 69.5

Total water requirement for the project: 132.5KLD

Quantity to be recycle: 63 KLD

Total fresh water requirement: 69.5KLD

When 20 KLD effluent will be sent to Common facility of MEPPL ,

Total water requirement for the project: 113.5KLD

Quantity to be recycle: 44 KLD

Total fresh water requirement: 69.5KLD

iii Waste water generation (KLD)

-

Sr. No. Source Ultimate (KLD)

1 Domestic 10

2 Industrial 65.0

(A) Processing 60.0

(B) Boiler Blow down

5

(C) Cooling bleed off

(D) Miscellaneous

TOTAL of Industrial & Domestic 75

-

iv Treatment facility with capacity

(ETP, CETP, MEE, STP, Spray Dryer etc).

61 KLD shall be send to ETP followed by

RO. RO permeate (44 KLD) will be

Recycled and RO reject (17 KLD) will be

either treated in in-house Evaporator or

of 48


Page 38 of 48

sent to Common Facility of MEPPL

(Mahavir Eco projects Pvt. Ltd.).

4 KLD High COD solvent bearing stream

shall be treated in stripper. Outlet from the

stripper shall be either sent to Common

Facility of MEPPL or will be treated in in-

house Evaporator.

10 KLD domestic effluents will be sent to

soak pit/septic tank as per existing EC.


Domestic: 10 KLD Domestic water is being

treated in to Septic Tank / Soak Pit

System/ Packaged STP and will be reused.

Industrial: As mention above and, it is

proposed to sent

17 KLD RO reject and 3 KLD effluent from

stripper to Common facility of MEPPL.

vi In case of Common facility (CF) like CETP, Common

Spray dryer, Common MEE etc. , name of CF

As mentioned in point iv.


Proponent has obtained NOC letter from

MEPPL for disposal of effluent.

vii Reuse/Recycle details (KLD) 44 KLD effluent will berecycled.

E Air



There will be no change in existing APC as mentioned below:

FLUE GAS EMISISON

Sr.

No. Stack Attached to

Stack Height and

Diameter

Fuel

Consumption


System

1. Steam Boiler

Capacity : 1 MT/Hr

Height -. 30 Meters

Dia. - 40 cm Natural Gas

–

1500 m3/day

(Total)

As Natural Gas is used

as a fuel. Adequate

Stack Height is

provided.

2. Steam Boiler

Capacity : 2 MT/Hr

Height -. 30 Meters

Dia. - 40 cm

3. Steam Boiler

Capacity : 2 MT/Hr

Height -. 30 Meters

Dia. - 40 cm

4. Thermopack Unit Height -. 30 Meters

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Page 39 of 48

Capacity : 200 U Dia. - 40 cm

5. Thermopack Unit

Capacity : 400 U

Height -. 30 Meters

Dia. - 40 cm

6. D. G. Set - Stand By

Capacity : 250 KVA

Height -.11 Meters

Dia. - 25 cm

LDO – 40

Liters/Hr

(Total)

As LDO is use as a

fuel. Adequate Stack

Height is provided.


Capacity : 250 KVA

Height -.11 Meters

Dia. - 25 cm

As LDO is use as a


Height is provided.


Capacity : 250 KVA

Height -.11 Meters

Dia. - 25 cm

As LDO is use as a


Height is provided.

-

ii Process gas i.e. Type of pollutant gases e.g: HCl

There will be no change in existing Process gas emission control system

PROCESS GAS EMISSION

Sr.

No. Vent Attached to

Vent Height and

Diameter Pollutant

Air Pollution

Control System

1. Reaction Vessel Height - 11 Meters

Dia. – 15 cm

HCl Ventury & packed

bed Scrubber

-


As below:

There shall be fugitive emissions during handling of raw materials

Mitigation Measures:

Vents of storage tanks are connected to Scrubbers to minimize fugitive emissions of gases.

F Hazardous waste


2016.

i

Cat. of

waste

Type of

Hazardous

Waste

Source Generated

Quantity Treatment

34.3 ETP Waste From ETP 500 Kg/Day Collection / Storage /

of 48


Page 40 of 48

i. e. 180

MT/Year

Transportation / sent to TSDF

site for secured land filling

36.4 Distillation

residue

From

Distillation

287.7

MT/Month

Collection / Storage /


site for incineration.

5.1 Used Oil From plant &

machineries

1000

Liters/year

i. e.

0.85 MT/Year



site / send to registered recycler

33.3 Discarded

Barrels/Liners

/

Containers

From raw

material

packaging

200

Nos/Month

i. e.

19.2 MT/Year


Transportation / sent back to

supplier / sent to registered

recycler

--- Evaporated

Salt *

From

Evaporator

2 MT/Day

i. e.720

MT/Year



Site

20.2 Spent Solvent

**

From Process 1150

MT/Month

Collection / Storage / recycle in to

process / sent to authorized end

users i. e. M/s. Rhythm

Chemicals Pvt. Ltd. / sent to

TSDF site for incineration

*Salts generated from evaporator will be eliminated when 20 KLD (17 KLD RO Reject + 3 KLD

treated effluent after stripper) effluent is sent to Common facility of MEPPL.

** The generation of detailed solvent list is as per below:

D 3 Sodium

Sulphate

From the

manufacturing

of 4-Bromo -1-

Methyl-1H-

Pyrazole / 2-

PIPERIDONE(

2-PD)

138.90

MT/Month

Collection / Storage / send to

TSDF site

B 11 Thionyl

Chloride

From the

manufacturing

of 2,6-difluoro

benzyl chloride

127.2

MT/Month


process

B 6 Raney Nickel From Process 9.5 MT/Month Collection / Storage / recycle in to

of 48


Page 41 of 48

process / send to original

Catalyst Manufacturer

From the manufacturing of 4-[1, 2, 4-triazolo-1-yl] methyl phenyl hydrazine / 5,6- Dimethoxy

Indanone (5,6-DMI) / Ethyl (4-aminophenyl) carbamate / ETHYL-5- AMINOBENZOFURAN-2-

CARBOXYLATE

Ammonia From the

manufacturing

of 2H-[1,2,4]-

TRIAZOLO-

[4,3-a]-Pyridine

(124TPO)

13.61

MT/Month


manufacturing of 1 – Methyl – 3 –

Phenyl piperazine, Amino

Acetaldehyde Dimethyl Acetal

and 1 – methyl – 3 – Phenyl

Piperazine

28.2 Palladium

Carbon

From the

manufacturing

of 1-Boc-3-

piperidone

14.20

MT/Month


process / send to original

Catalyst Manufacturer

26.1 Process

Waste

From the

manufacturing

of 1-[2-(2-

Hydroxy

Ethoxy) Ethyl]

Piperazine

150.8

MT/Month



site

28.2 Carbon

Residue

From the

manufacturing

of 1-Hydroxy

benzotriazole /

3, 4 –

Dihydroxy – 5

– Nitro

Benzaldehyde

(3,4dh5nbz)

8.57

MT/Month



site

-

ii Membership details of TSDF, CHWIF etc.

Industry is a member of TSDF site of M/s.

Bharuch Enviro Protection Ltd., Bharuch

for the disposal of Solid / Hazardous

Waste.

ii Details of Non-Hazardous waste & its disposal Not Applicable

of 48


Page 42 of 48

(MSW and others)

G Solvent management& VOC emissions etc.

i Details of Solvent recovery (As per respective ToR)

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

Sr.

No.

Type of solid

waste Source

Generated

Quantity Treatment

1. Spent

Solvent

(Toluene)

From Process 1150

MT/Month


process / sent to authorized end users i.

e. M/s. Rhythm Chemicals Pvt. Ltd. /

sent to TSDF site for incineration

Generated from the manufacturing of 4 Hydroxyl Cumarine, 1-(2,3-dichloro phenyl)

piperazine HCL, 1-(3-chlorophenyl) piperazine HCL, 1- phenyl piperazine, 1-methyl-3-

phenyl piperazine, 1-methyl-4-piperidone, 1-(2-hydroxy ethyl) pyrrolidine, 4 – HYDROXY

COUMARIN (HC), 5,6- Dimethoxy Indanone (5,6-DMI), 1 – Methyl – 3 – Phenyl

Piperazine, 1-(3-Chloro Phenyl ) Piperazine, 1-(2-Chloro Phenyl) piperazine, 1-(4-Chloro

Phenyl ) Piperazine, 1-(2,3-DiChloro Phenyl ) Piperazine, 1-(3,4-DiChloro Phenyl )

Piperazine, 1-(2,6-DiChloro Phenyl ) Piperazine, 1-(2-Methoxy Phenyl ) Piperazine, 1-(3-

Methoxy Phenyl ) Piperazine, 1-(4-Methoxy Phenyl ) Piperazine, 1-(2-Hydroxy Phenyl )

Piperazine, 1-(3-Hydroxy Phenyl ) Piperazine, 1-(4-Hydroxy Phenyl ) Piperazine, 1-(2-

Bromo Phenyl ) Piperazine, 1-(3-Bromo Phenyl ) Piperazine, 1-(4- Bromo Phenyl )

Piperazine, 1-(2-Nitro Phenyl ) Piperazine, 1-(3-Ntiro Phenyl ) Piperazine, 1-(4-Ntiro

Phenyl ) Piperazine, 1-Phenyl Piperazine, 1-(3-Trifluoro Phenyl) Piperazine, N-(3,4-

METHYL ENEDIOXY PHENYL) PIPERAZINE, N-(2,4-DIMETHOXY PHENYL)

PIPERAZINE, 1-(3,4-DIMETHOXY PHENYL) PIPERAZINE, 1-(3-Fluoro Phenyl )

Piperazine, 1-(2-Fluoro Phenyl) piperazine, 1-(4-Fluoro Phenyl ) Piperazine, 1-(3-Tollyl )

Piperazine, 1-(2-Tollyl ) Piperazine, 1-(4-Indolyl) piperazine, 1-(2-Pyridyl)- piperazine, 1-

Pyridin-4-yl-piperazine, 1-(2-Cyanophenyl) piperazine, 1-(4-Iodo-phenyl) - piperazine, 1-

(3-nitro-2-pyridyl) piperazine, 1-(2-Pyrimidyl) Piperazine.

2. Spent

Solvent

(Methanol /

Iso Propyl

Alcohol)

From Process 195

MT/Month





Generated from the manufacturing of 1-(2,3-dichloro phenyl) piperazine HCL, 1-(3-

chlorophenyl) piperazine HCL and 1- phenyl piperazine,

of 48


Page 43 of 48

3. Spent

Solvent

(Solvent)

From the

manufacturing

of 1-[2-(2-

hydroxy ethoxy)

ethyl]

piperazine

158.33

MT/Month





4. Spent

Solvent

(Piperazine)

From Process 175

MT/Month





Generated from the manufacturing of 1-[2-(2-hydroxy ethoxy) ethyl] piperazine, 3-

(Piperazine-1-yl)-1, 2-benzothiazole, 1-(2-hydroxy ethyl) piperazine, 1-Formyl

Piperazine, 1-Carbethoxy Piperazine, 1-Acetyl Piperazine, 1 - (3-Chloro

propyl)piperazine, 1-Benzyl Piperzaine, 1-(Furoyl)piperazine, 1-

(Tetrahydrofuroyl)piperazine, 1-Benzoyl Piperazine, 1-Cinnamyl Piperazine, 1-BOC

piperazine, 1-CBZ Piperazine, 1-Isopropyl Piperazine, 1-Cylco pentyl Piperazine, 1-

Cyclo Butyl Piperazine, 1-Cyclo propyl piperazine, 1-Cyclo propyl methyl piperazine, 1-

Benzyloxy ethyl piperazine, 1 - methyl Piperazine, 1-Hydroxy benzotriazole.

5. Spent

Solvent

(Acetic Acid)

From Process 50

MT/Month





Generated from the manufacturing of 1, 2-benzisoxazol-3-yl acetic acid, ethyl 3-(pyridin-

2-ylamino)propanoate,

6. Spent

Solvent

(Methanol)

From Process 555.12

MT/Month





Generated from the manufacturing of Tri Methyl Ortho Benzoate, Tri Alkyl Ortho

Alkonate, 1, 2-benzisoxazol-3-yl acetic acid, 2,6-difluoro benzyl chloride, 4-[1, 2, 4-

triazolo-1-yl] methyl phenyl hydrazine, 1-(2-hydroxy ethyl) piperazine, 1-Formyl

Piperazine, 1-Carbethoxy Piperazine, 1-Acetyl Piperazine, 1 - (3-Chloro

propyl)piperazine, 1-Benzyl Piperzaine, 1-(Furoyl)piperazine, 1-

(Tetrahydrofuroyl)piperazine, 1-Benzoyl Piperazine, 1-Cinnamyl Piperazine, 1-BOC

piperazine, 1-CBZ Piperazine, 1-Isopropyl Piperazine, 1-Cylco pentyl Piperazine, 1-

Cyclo Butyl Piperazine, 1-Cyclo propyl piperazine, 1-Cyclo propyl methyl piperazine, 1-

of 48


Page 44 of 48

Benzyloxy ethyl piperazine, 1 - methyl Piperazine, dibenzo[b,f][1,4]thiazepin-11(10H)-

one, N, N-Dimethyl Formamide Dimethyl Acetal, Ethyl{4-[4-fluorobenzyl]amino}-2-

nitrophenyl}carbamate, 1-[2-(2-HYDROXY ETHOXY) ETHYL] PIPERAZINE, Methyl

Cyclobutane carboxylate, 2H-[1,2,4]-TRIAZOLO-[4,3-a]-Pyridine (124TPO), 1-Boc-3-

piperidone, 4-chloro butyraldehyde dimethyl acetal, Cyclohexane Carboxaldehyde, 4-

cyano-4-(4-fluorophenyl) cyclohexan-1-one., 5-(2-Methoxyphenoxy)-2,2’-bipyrimidine-

4,6(1H,5H)-dione, Methyl di-(2-thienyl)glycolate.

7. Spent

Solvent

(IPE)

From Process 1125

MT/Month





Generated from the manufacturing of 4-Bromo -1-Methyl-1H-Pyrazole, ethyl 3-(pyridin-2-

ylamino)propanoate, 1-Boc-3-piperidone, Cyclohexane Carboxaldehyde, N-Methyl

amino Acetaldehyde Dimethyl Acetal,

8. Spent

Solvent

(MDC)

From Process 1550

MT/Month





Generated from the manufacturing of 2,6-difluoro benzyl chloride, 3-(Piperazine-1-yl)-1,

2-benzothiazole, 5,6- Dimethoxy Indanone (5,6-DMI), Methyl Cyclobutane carboxylate,

ETHYL 5- NITROBENZOFURAN-2-CARBOXYLATE, ETHYL-5- PIPERAZINYL

BENZOFURAN-2-CARBOXYLATE, 4-(2-chloroethyl) morpholine, 4-chloro

butyraldehyde dimethyl acetal, Cyclohexane Carboxaldehyde, 4-cyano-4-(4-

fluorophenyl) cyclohexan-1-one.

9. Spent

Solvent

(IPA)

From Process 190

MT/Month





Generated from the manufacturing of 5,6- Dimethoxy Indanone (5,6-DMI), Ethyl 1-(4-

methoxyphenyl)-6-(4-nitrophenyl)-7-oxo-4,5,6,7-tetra hydro-1H-pyrazolo[3,4-c] pyridine-

3-carboxylate, S-(2, 3-epoxypropyl) Phthalamide, 4-(4-aminophenyl) morpholin-3-one.

10 Spent

Solvent

(Ethyl

Acetate)

From Process 200

MT/Month





Generated from the manufacturing of 1 – Methyl – 3 – Phenyl Piperazine, 1 - Methyl - 3 -

of 48


Page 45 of 48

Phenyl Piperazine, Ethyl (4-nitrophenyl) carbamate, S-(2, 3-epoxypropyl) Phthalamide.

11 Spent

Solvent

(Phenol)

From the

manufacturing

of

dibenzo[b,f][1,4]

thiazepin-

11(10H)-one

9.41

MT/Month





12 Spent

Solvent

(DMF)

From Process 260

MT/Month





Generated from the manufacturing of dibenzo[b,f][1,4]thiazepin-11(10H)-one, ETHYL 5-

NITROBENZOFURAN-2-CARBOXYLATE, 3-CHLORO-1-(4-NITROPHENYL)-5,6-

DIHYDROPYRIDIN-2(1H)-ONE. .

13 Spent

Solvent

(Ethanol)

From Process 935.20

MT/Month





Generated from the manufacturing of Ethyl (4-aminophenyl) carbamate, Ibandronic Acid,

Methyl Cyclobutane carboxylate, ETHYL 5- NITROBENZOFURAN-2-CARBOXYLATE,

ETHYL-5- AMINOBENZOFURAN-2-CARBOXYLATE, 5-(2-Methoxyphenoxy)-2,2’-

bipyrimidine-4,6(1H,5H)-dione.

14 Spent

Solvent

(Acetone)

From Process 1040

MT/Month





Generated from the manufacturing of ETHYLCHLORO[(4-METHOXY

PHENYL)HYDRAZONO]ACETATE and Ibandronic Acid.

15 Spent

Solvent

(Mono

Ethylene

Glycol)

From the

manufacturing

of 2H-[1,2,4]-

Triazolo-[4,3-a]-

Pyridine

(124TPO)

100

MT/Month





16 Spent

Solvent (Di

From the

manufacturing

105

MT/Month



of 48


Page 46 of 48

Chloro

Methane)

of ETHYL 5-

NITROBENZOF

URAN-2-

CARBOXYLAT

E



17 Spent

Solvent

(THF)

From Process 180

MT/Month





From the manufacturing of 1-Boc-3-piperidone / 3-methoxy propiophinone / 4-(4-

aminophenyl) morpholin-3-one

18 Spent

Solvent (t -

Butanol)

From the

manufacturing

of 1-Boc-3-

piperidone / 1-

Boc-4-

piperidone

28.76

MT/Month





19 Spent

Solvent

(Hexane)

From the

manufacturing

of 1-Boc-4-

piperidone

35

MT/Month





20 Spent

Solvent

(Chloro

Benzene)

From the

manufacturing

of 1-(4-

Rphenyl)-2-

piperidone

194

MT/Month





21 Spent

Solvent

(Methylene

DiChloride)

From the

manufacturing

of 3, 4 –

Dihydroxy – 5 –

Nitro

Benzaldehyde

(3,4DH5NBZ)

301.93

MT/Month





22 Spent

Solvent

(1, 4

From the

manufacturing

of 2-

130

MT/Month




of 48


Page 47 of 48

-

Dioxane) (chloromethyl)-

4- methyl

quinzoline


23 Spent

Solvent

(o-xylene)

From the

manufacturing

of 4-cyano-4-(4-

fluorophenyl)

cyclohexan-1-

one

166.40

MT/Month





24 Morpholine From the

manufacturing

of 3-morpholin-

4-YL-1-(4-

nitrophenyl)-

5,6-

dihydropyridin-

2(1H)-one

67.50

MT/Month





25 Salicyladehy

de

From the

manufacturing

of ethyl 5-

nitrobenzofuran

-2-carboxylate

20

MT/Month





26 Propionic

Acid

From the

manufacturing

of 3-methoxy

propiophinone

22.55

MT/Month





27 N-heptane From the

manufacturing

of Methyl di-(2-

thienyl)glycolate

392

MT/Month





ii VOC emission sources and its mitigation measures NIL

• During the meeting dated 29/10/2018, Committee observed that unit has proposed to amend in

condition no-9 and 10 of EC order. Committee deliberated on the possible impacts on surrounding

environment due to proposed amendments.

of 48


Page 48 of 48


• Committee deliberated on EC-amendment proposal as above.

• Committee noted that PP has requested amendment in EC condition for allowing them to send

treated waste water of 20 KLPD after treatment to common facility of MAHAVIR ECO for pursuing

zero liquid discharge. It is noted that quality of treated waste water will be COD: 10,000 mg/litre to

12,000 mg/litre, TDS: 12000 mg/litre to 15000 mg/litre. Further PP mentioned that during failure of

operation of in-house MEE, alternative source of disposal of treated waste water for pursuing ZLD is

needed. Committee asked PP to submit details of overhauling hours of existing MEE since

commissioning and to justify how frequent the operation of in-house MEE gets overhauled and also

to submit compliance status of common infrastructure of MAHAVIR ECO that pursues zero liquid

discharge (ZLD).

After deliberation, committee asked PP to submit aforementioned details and after submission, it

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

Meeting ended with thanks to the Chair and the Members.

Minutes approved by:

1. Shri S. C. Srivastav, Vice Chairman, SEAC 2. Shri V. N. Patel, Member, SEAC

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

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

minutes of the 446 meeting of the state level expert ... minutes of the 446th i.pdf · page 1 of 48...

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