Minutes of the 438 meeting of the State Level Expert ... Minutes of the 438th I.pdf · Page 1 of 52 438 th meeting of SEAC-Gujarat, Dated 03.10.2018 Page 1 of 52 Minutes of the 438th

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438thmeeting of SEAC-Gujarat, Dated 03.10.2018

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Minutes of the 438th meeting of the State Level Expert Appraisal Committee held on 03/10/2018

at Committee Room, GEER Foundation, Gandhinagar.

The 438h meeting of the State Level Expert Appraisal Committee (SEAC) was held on 03rd October

2018 at Committee Room, GEER foundation, Gandhinagar. Following members attended the

meeting:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

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

5. Shri Rajesh I Shah, Member, SEAC

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

The 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.

7. SIA/GJ/IND2/20649/2017 M/s. Meghmani LLP [Earlier named as M/s. Meghmani Unichem LLP] Plot No. CH-3, GIDC Industrial Estate, Dahej, Taluka-Vagra, District-Bharuch.

Appraisal

Project / Activity No.: 5(f)

Project status: Expansion

• PP has submitted online application vide no. SIA/GJ/IND2/20649/2017 dated 14/11/2017 for

obtaining Environmental Clearance.

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

SEIAA/GUJ/TOR/5(f)/158/2018 dated 28/02/2018.

• Project proponent has submitted EIA Report prepared by M/s. Anand Environmental Consultants Pvt.

Ltd. based on the TOR issued by SEIAA.

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

tabulated below:

Sr. No.

Name of Product CAS no. Quantity (MT/Month) End-use of product

Existing Proposed Total

1. Para Amino Phenol 123-30-8 300 900 1200 For Mfg. Paracetamol

2. Paracetamol 103-90-2 1250 0 1250 For Mfg. Antipyretic Drug

By-Product

Dil. Acetic Acid (from Paracetamol)

64-19-7 1750 0 1750 In Textile &Glacial Acetic Acid

• 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 03/10/2018.

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• Salient features of the project are as under:

Sr. no.

Particulars Details

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

Existing: 600 Lacs Proposed:45 Crores Total: 51 Crores

B Total Plot area ( sq. meter)

Existing: 10000 sq. m Proposed: Nil Total: 10000 sq. m

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

Existing: Proposed: Total:5924 m2

C Employment generation Existing: Proposed: Total:

Direct 120 40

160

Indirect 70 40

110

D Water

i

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

GIDC

Status of permission from the concern authority. Yes

ii

Water consumption (KLD)

Existing KLD

Proposed * (Additional)

KLD

Total after* Expansion

KLD

(A) Domestic 15 0 15

(B) Gardening 5 1 6

(C) Industrial

Process 85 135 220

Washing 20 20 40*

Boiler 44 -- 44

Cooling 20 80 100

Others -- -- --

Industrial Total 169 235 404

Grand Total (A+B+C)

189 236 425

* This is 1st day fresh water requirement, from second day onwards 40 m3/day recycled water will be reused. Therefore from the second day onwards fresh water requirement will be 385 m3 /day (425 – 40).

1) Total water requirement for the project: 425KLD 2) Quantity to be recycle: 40KLD 3) Total fresh water requirement: 385 KLD

iii

Waste water generation (KLD)

Category Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

(A) Domestic 13 0 13

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(B) Industrial

Process 58 174 232

Washing 20 20 40

Boiler 10 -- 10

Cooling 20 80 100

Others

Total Industrial waste water

108 274 382

Grand Total (A+B) 121 271 395

-

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 and domestic will be treated in our existing effluent treatment plant (capacity-125 m3/day) and proposed effluent treatment plant (capacity-400 m3/day). Treated effluent will be reused in miscellaneous washing (40 m3/day) and remaining will be discharge into underground GIDC -drainage line and ultimately disposal into deep sea.

v Mode of Disposal & Final meeting point

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

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

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 (capacity-125 m3/day) and proposed effluent treatment plant (capacity-400 m3/day).

Membership of Common facility (CF)

Not applicable, since our Effluent generated from industry and domestic will be treated in our existing effluent treatment plant (capacity-125 m3/day) and proposed effluent treatment plant (capacity-400 m3/day).

vii Reuse/Recycle details (KLD)

Treated effluent will be reused in miscellaneous washing (40 m3/day) and remaining will be discharge into underground GIDC -drainage line and ultimately

E Air

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

Sr. no.

Source of emission

With Capacity

Stack Height (meter)

Name of the fuel

Quantity of Fuel MT/hr & MT/Day

Type of emissions

i.e. Air Pollutants

Air Pollution Control Measures

(APCM)

Existing

1. Steam boiler (3 ton/hr)

30 Coal

15 MT/day

SPM

SO2 NOx

Multi-cyclone & bag filter

2. Thermic fluid heater

15 LDO

50 LPH SPM

SO2 NOx

Adequate stack height

3. D.G. set * (400 KVA)

15 LDO

15 LPH SPM

SO2 Adequate stack height

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NOx

Proposed

4. Steam boiler (5 ton/hr)

30 Natural Gas

300 SCM/hr

SPM

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)


(APCM)

1 Not Applicable It may be noted that our manufacturing process is such that there is no process gas emission.

-

iii Fugitive emission details with its mitigation measures.

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

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

i

Sr. No.

Type/Name of Hazardous waste

Source of generation

Category and

Schedule as per

HW Rules.

Quantity (MT/Annum)

Mode of Disposal**


1. ETP Sludge

ETP 35.3 2880 MT

6540 MT

9420 MT

Will be collected, stored, transported & disposed at authorized TSDF site.

2. Spent Catalyst

Manufacturing process

28.2 0.3 MT

0.222 MT

0.522 MT

Will be sent back for regeneration/ reactivation

3. Used Drums


33.1 0.54 MT

0.96 MT

1.5 MT

Will be collected, stored and reused /sold to authorized recycler Liners /

PPBags 0.84 MT 1.16 MT 2.0

MT

4. Used Spent Oil


5.1 0.30 MT

0.90 MT

1.2 MT

Will be collected, stored and sold to authorized recycler.

5. Dil. Acetic Acid


-- 21000 MT

0

21000 MT

Collection, storage and sell to registered recycler/end user.

6. Waste resin from wastewater treatment

Wastewater treatment

35.2 0 12 MT

12 MT

Will be collected, stored, transported & disposed at authorized Common Haz. Waste Management Facility (CHWMF)

-

ii Membership details of TSDF, CHWIF etc. We have obtained membership of BEIL-Dahej for TSDF

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

Not applicable

G Solvent management, VOC emissions etc.

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

• Not applicable

ii VOC emission sources and its mitigation measures

• Not applicable

• During the meeting dated 03/10/2018, technical presentation made by project proponent.

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

from SEIAA & 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 proposal is for expansion of existing unit and for now proposes a new synthetic organic chemical

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

report is submitted. The compliance of EC is submitted by RO and it was discussed in detail and

found satisfactory. PP ensured that there are no court cases pending and no public complaints

against the project.

• Total water consumption will be 425 KLD. Total wastewater generation will be 382 KLD. After

proposed expansion, ETP proposed of 400 KLD capacity in addition to existing 125 KLD capacity &

after full-fledged treatment, 40 KLD treated effluent shall be reused back in washing purpose and rest

of treated effluent shall be discharged into underground drainage of GIDC which ultimately meets to

Deep sea. Domestic effluent will be 13 KLD and shall be treated in proposed ETP along with

industrial effluent.

• Coal or Natural gas will be used as fuel for proposed boiler.

• Adequate APCM will be provided for proposed flue gas emission.

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

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

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

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

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

NOx, HCl, Cl2, HBr, NH3, CO and VOC at eight locations, including the project site. Values conform

to the prescribed standards for Ambient Air Quality. The incremental Ground Level Concentration

(GLC) has been computed using AIRMOD. 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.

Discussions & Conclusion:

• Committee deliberated that PP has changed the name from M/s. Meghmani Unichem LLP to M/s.

Meghmani LLP, hence PP was asked to submit all statutory documents in this regard.

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• Committee deliberated on Compliance of existing project (CCR), automization of the manufacturing

plant, Hazardous chemicals like Cl2, Toluene & other hazardous chemicals, APCM for process gas

emission, SOP for safety precautions, Baseline, CER, HW management etc.

• PP informed that they will follow the PESO standards for unloading, storage, transportation, handling

and processing of PNCB. PP have to provide CEMS for process gas emission.

• Committee deliberated on management of acetic acid and also focused on permission of Narcotics

department for selling of dilute acetic acid.

• It is noted that capacity of boiler is increasing whereas proposed water consumption under the boiler

is shown nil. Further proposed production is increasing to 900 MTPM from 300 MTPM and water

requirement, waste water generation is not accordingly addressed.

• Referring to the baseline study for ambient air, it is noted that wind rose diagram, isopleths of gases

and particulate matter are not in consonance; hence it was decided to ask PP to readdress the same.

After detailed discussion, it was decided to ask project proponent to submit the following details and

upon receipt of the same, it was decided to consider the proposal in one of the upcoming SEAC

meeting.

1. To re-address water consumption and waste water generation considering three time expansion of

product Para Amino Phenol.

2. To re-address wind rose diagram, GLC during the study period and its associated isopleths with

coverage of area in upwind and downwind with conclusion and submit addendum in EIA report of the

same.

3. To submit all statutory documents pertaining to the change of name from M/s. Meghmani Unichem

LLP to M/s. Meghmani LLP.

8. SIA/GJ/IND2/18468/2017 M/s. Krishna Antioxidants Pvt. Ltd. Plot No. D-3/24/1, GIDC, Dahej, Village Samatpor, Taluka Vagra, Dist. Bharuch. 392130

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/18468/2017 dated 14/02/2017 for

obtaining Environmental Clearance.

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

SEIAA/GUJ/TOR/5(f)/493/2017 vide dated 30/04/2017 and ToR Amendment No.

SEIAA/GUJ/TOR/5(f)/339/2018 vide dated 28/03/2018.

• Project proponent has submitted EIA Report prepared by M/s. Kadam Environmental Consultants

based on the TOR issued by SEIAA.

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• This is an existing unit and now proposes for expansion for synthetic organic chemicals as tabulated

below:

Table 1: Details for EC Products

Sr.

No. Name of the Products

CAS no. /CI

no.

Quantity

MT/Annum End-use of products

1 Oil Soluble Demulsifier - 2400 Refinery Industry

2 Polymeric/Polyester/Polyurethane

based Polyol - 9600 Polyurethane industries

3 Octylated Butylated Diphenylamine

36878-20-3

/ 68411-46-

1

2000 Antioxidants for Lubricant

Industries

4 Amine Ethoxylate

(MDEA/MEA/DEA/TEA) - 5000

Intermediate for H2S

scavenger

5 Crude Raw (Fatty Acid) Oil Fractions - 6000 Mud Emulsifier

6 Polyol Intermediate Products such as; - 6000

a N Polyethylene Glycol -

Intermediate for Drilling

Chemicals

b Oxo Alcohol & Its Higher Derivative

Ethoxylate -

Additive for Drilling

Chemicals

c Oxo Alcohol & Its Higher Derivative

Condensate -

Additive for drilling

Chemicals

d Nonyl Phenol Ethoxylate/Condensate

127087-87-

0

Textile, Detergent & Soap

Industries

e Glycerine Propoxylate - Intermediate for Drilling

Chemicals

f Iso Propyl Alcohol Ethoxylate - Intermediate for Drilling

Chemicals

7 Drilling Additive Intermediate Products

such as; - 3000

a Primary & Secondary Surfactant for

Drilling - Mud Chemicals

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8 Surfactants & Other EO/PO

Condensate such as; - 3000

a Fatty / Lauryl Alcohol Ethoxylate 24938-91-8

Surfactants for cosmetics,

Detergent industries

b Phenoxy Ethanol 122‐99‐6 Additives for Paints & Inks

c Castor Oil Ethoxylate 61791-12-6 Additive for Personal Care

d Hydrogenated Castor Oil Ethoxylate 61788-85-0 Additive for Oil & Wax

Industries

e Tallow Amine Ethoxylate - Textile Industries

f Styrenated Phenol Ethoxylate - Additive for Industrial

Chemicals

g Phenolic Derivative Ethoxylate - Additive for Industrial

Chemicals

h Synthetic Alcohol Ethoxylate - Surfactants for Textile, Soap

& Detergent Industries

i Styrenated Phenol 61788-44-1 Antioxidants for Rubber

j Soybean Oil/Base oil Ethoxylate - Surfactants for Textile

Industries

Total 37000

Table 2: Details for Non-EC Products

Sr.

No. Name of the Products

CAS no. /CI

no.

Quantity

MT/Month End-use of products

1. Lubricity Improver

Such as Diesel Lubricity Improver - 333 Additive for Diesel

2.

Drilling Chemicals such as.

Cloud Point Glycols (CPG grades

like– 108, 208, 308, 308 P, 308 PM,

608, ADN’ etc.).

Welcol B

Drill Fast etc.

- 250 Additive for Oil Drilling

3. Polyol - 500 Additive for Oil Drilling

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Grades like Grade I, Grade II etc.

4. Emulsifier for Agrochemicals

Cristol grades like E55 A, E55 T etc. - 40

Additive for Insecticide /

Pesticide Spraying

5.

Conning oil Emulsifier

Grades like COE 70, COE 150,

Antistatic Conning oil etc.

- 150 Additive for Textile

6. Oil based Agrochemicals such as

Tree Spray Oil - 15

Additive for Apple & Tea Anti

insect Spray

7. Octane Booster - 300 Additive for Gasoline

8. Cold flow Plug Point (CFPP) - 100 Additive for Diesel for Cold

Countries

Total 1688




Sr.

no. Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing: 9.82 Crores

Proposed: 26.18 Crores Total: 36 Crores

B Total Plot area

( sq. meter)

Existing: 24094 Sq. m.

Proposed: 16063.67 Sq. m.

Total: 40157.67 Sq. m.

Green belt area,/Tree Plantation area

( sq. meter)

Existing: 6289 Sq. m.

Proposed: 6010 Sq. m.

Total: 12299 Sq. m.

C Employment generation

Existing: 15

Proposed: ~145 People (30 Direct +15

Indirect (contract employee during

operation phase) +100 Contractor Workers

will involve only during Project Phase)

Total: ~160

D Water

i Source of Water Supply Water will be sourced from GIDC water

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

Status of permission from the concern authority. Letter from GIDC for water supply is

shown in Annexure 5 in EIA Report.

ii Water consumption (KLD)

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 0.5 2 2.5

(B) Gardening 2 8 10

(C) Industrial

Process 0 9 9

Washing 1 5 6

Boiler 4 19.5 23.5

Cooling Tower 20 183 203

Softener Unit 1 3.5 4.5

DM Unit 1 4 5

Blending 9 2 11

Scrubber 0 3 3

Industrial Total 36 229 265

Grand Total (A+B+C)

38.5 239 278

278 KLD is

Including 40 KLD

recycled water

from RO

1) Total water requirement for the project: 278 KLD

2) Quantity to be recycle: 40 KLD

3) Total fresh water requirement: 238 KLD

iii Waste water generation (KLD)

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 0.4 1.6 2 To ETP followed by

RO, 40 KLD RO

permeate to be

recycled and 21

KLD RO Reject will

(B) Industrial

Process 0 9 9

Washing 1 3 4

Boiler 0.4 3 3.4

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Cooling Tower 1 28 29 be discharged into

GIDC Drain Softener Unit 1 3.5 4.5

DM Unit 1 4 5

Blending 0 0 0

Scrubber 0 3 3

Lab Equipment Washing 0 2 2

Total Industrial waste

water 4.4 55.5 59

RO Reject to GIDC

Drain - - 21

To GIDC drain for

Sea disposal

iv

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

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

The process wastewater and utilities blow down will be treated in ETP followed by RO. Capacity of

ETP is 70 KLD (35 KLD x 2).

v

Mode of Disposal & Final meeting point

Domestic: Treated wastewater will be discharged into GIDC drain matching with GPCB

standards.

The permission letter from the GIDC for effluent discharge into drain is shown in

Annexure 6 in EIA Report.

Industrial:

vi

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

Name of Common facility

Not Applicable


Not Applicable


40 KLD RO permeate to be recycled.

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

Kg/Hr

Type of

emissions i.e.

Air Pollutants

Air Pollution

Control

Measures

(APCM)

Existing

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1

Steam Boiler

– 1

(1500 Kg/hr.)

31 Furnace

Oil 94

PM, SO2, NOx

Adequate Stack

Height is

provided 2

DG set -1

(600 kVA) 11 HSD 127

Proposed

1

Steam Boiler

– 2

(1500 Kg/hr.)

31 Furnace

Oil 94

PM, SO2, NOx

Adequate Stack

Height is

provided

2

Steam Boiler

– 3

(2000 Kg/hr.)

31 Furnace

Oil 127

3

Thermic

Fluid Heater

(10 Lac

Kcal/hr.)

31 Furnace

Oil 120

After Proposed Expansion

1

Steam Boiler

– 1

(1500 Kg/hr.)

31

Furnace

Oil 94 Kg/hr.

PM, SO2, NOx

Adequate Stack

Height is

provided

2

Thermic

Fluid Heater

(10 Lac

Kcal/hr.)

Furnace

Oil 120 Kg/hr.

3

Steam Boiler

– 2

(1500 Kg/hr.) 31

Furnace

Oil 94 Kg/hr.

4

Steam Boiler

– 3

(2000 Kg/hr.)

Furnace

Oil 127 Kg/hr.

5 DG set -1

(600 kVA) 11 HSD 127 Kg/hr.

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 Reactor (6 Nos.) VOC 10 Water Scrubber

2 Storage Tank Area VOC 10 Water Scrubber

-


Fugitive Emission:

Dust from the Road during transportation, leaks from Pressure vessel, valves, pumps, compressor

& flanges.

Mitigation Measures:

Routine inspections of process & Storage equipment/vessel with gas detectors, Hydro-test to

identify leaks and estimate the leak rate in order to decide on appropriate corrective action.

Replacement of old gaskets, tightening of flanges, Replacement/repair of valves etc. Water

sprinkling at road & Green belt development in plant and nearby road area.

F

Hazardous waste

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

2016.

Existing & Proposed

i

Sr.

no.

Type/Name

of

Hazardous

waste

Source of

generation

Category

and

Schedule as

per HW

Rules.

Quantity

(MT/Annum)

Disposal

Method

Ex

isti

ng

Pro

po

se

d

To

tal

1 Skimmed oil

in ETP

Equipment

washing,

spillage or

leakage during

process/

drumming

35.4 0.4 0.36 0.76

Store in

Carboys &

resale for

reuse

2 ETP Sludge Microbiological

activity in ETP 35.3 0.12 36

36.1

2

Collect in bags

send to GPCB

approved

party for

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disposal

3 Used oil

Gear, pump,

DG, Forklift,

Transformer

5.1 0.2 0.12 0.32

GPCB

approved

authorized

recycler

4 Cotton waste Generate during

cleaning 33.2 0.16 0.12 0.28

Collect in bags

GPCB

approved

authorized

recycler

5

Used

container/

barrel

Manufacturing

Process 33.1

130

Nos.

120

Nos.

250

Nos.

GPCB

approved

party

6

Waste drum

seals and

caps

Manufacturing

Process 33.1 0.16 0.012

0.17

2

GPCB

approved

party

7 Waste

Catalyst

Spent catalyst in

process 18.1 0 14.4 14.4

Collect in bags

for land filling

as per CPCB

guideline for

waste disposal

8 Waste Filter

Cloth

Waste filter cloth

after filtration 36.2 0 1.2 1.2

Collect in bags

and Send to

GPCB

approved

party for

disposal

9 Spent Carbon

From

manufacturing

Process and

ETP

36.2 0 12 12

Collect in bags

and send to

GPCB

approved

party for

disposal

ii Membership details of TSDF, CHWIF etc. TSDF: Membership letters from the M/s.

BEIL & RSPL for Liquid waste & hazardous

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waste disposal is given in Annexure 7 in

EIA Report.

iii Details of Non-Hazardous waste & its disposal

(MSW and others)

Bio-medical waste:

The generated waste will be collected

separately and handed over to bio medical

waste treatment agencies as per the GPCB

regulation and bio-medical waste

management rule 2011. Quantity of Bio-

medical waste generation is 0.030

MT/Annum.

Domestic Waste:

Electronic Wastes

Generated Electronic wastes will be

collected separately and handover to e-

waste disposal agencies to dispose as per

the provisions of the E-Wastes

(Management and Handling) Rules, 2011.

Quantity of E-waste generation is 0.2

MT/Annum.

Kitchen/canteen waste and other

biodegradable waste is collected separately

and sent to authorize agencies of

Vermicomposting.

The non-hazardous recyclable waste like

paper, plastic, metal and wooden waste will

be sold further to Authorize Re-Processor &

recycler. Quantity of Non-Hazardous solid

waste is 0.05 MT/Annum.



There are different types of Aromatic & Hydrocarbon solvents are used in the Process. Quantity &

Name of each solvent is mentioned in above Table. Most of the solvents are mixed for the dilution

of the product as per the requirement. Only in Octylated/Butylated Di Phenyl Amine based product

the excess solvent is added into the feed to reactivate the catalyst and steady the rate of reaction.

The excess solvent is recovered by flash distillation method and same will be reused as a raw

material for next batch. The mass balance of the same is given below.

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S.

No. Name of Solvent

Solvent

Used in

MTPM

Spent Solvent

recovered in

MTPM

%

Recovery Remark

1 Fresh C4 Olefins

Solvent 83 22 27

Recovered

solvent is reused

in the process


• Source:

S. No. Stack Attached to Nos. of

Stack

Stack Height

in m

Pollutants

Emitted


Measures Attached to

1 Reactor (6 Nos.) 1 10 VOC Water Scrubber

2 Storage Tank Area 1 10 VOC Water Scrubber

• Mitigation Measures:

Water Scrubber

VOC is pulled out through vacuum after completion of reaction and passed through packed column

water scrubber and majority VOC will be dissolved in water while ppm level VOC will be discharged

through vent along with air. Dissolved VOC will be sent to ETP for the further treatment.

Detection and monitoring of VOC’s / gases

For the detection of VOC's /Gases fixed detector will be installed at prominent locations and

portable leak detector sensors will be used whenever required.



Observation:


product. This unit is having CTE for existing unit and production is not yet started. Copy of CTE and

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

complaint is there against the project.

• Total water consumption will be 278 KLD. Total wastewater generation will be 59 KLD. After

proposed expansion, ETP proposed of 70 KLD capacity & after full-fledged ETP treatment and RO

plant treatment, 40 KLD treated effluent i.e. RO permeate shall be reused back in washing purpose

and rest of treated effluent i.e. RO reject shall be discharged into underground drainage of GIDC

which ultimately meets to Deep sea. Domestic effluent will be 2 KLD and shall be treated in proposed

ETP along with industrial effluent.

• Furnace oil will be used as fuel for proposed boilers and thermic fluid heater.

• Adequate APCM will be provided for proposed process gas emission.

Page 17 of 52


Page 17 of 52

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

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

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

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

2017-May, 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NOx, HCl,

Cl2, HBr, 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 AIRMOD. 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 deliberated on Compliance of existing project (CCR), possibilities of automization of the

manufacturing plant, handling and storage of Hazardous chemicals like Cl2, Toluene & other

hazardous chemicals, APCM for process gas emission, SOP for safety precautions, Baseline, CER,

HW management etc.

• PP informed that they will follow the PESO standards for unloading, storage, transportation, handling

and processing of solvents.

• During appraisal committee noticed that quantities of waste water generation, permeate and RO

rejection are not in consonance and asked PP to submit revised water balance.

• It is noted that solvent recovery for Fresh C4-Olefin is 24 % and could not justify its balance quantity,

hence PP was asked to address details solvent recovery after considering its quantity used in

product.

• Need based survey for implementing CER with outlay of upcoming years could not be addressed

satisfactorily by the PP.



meeting.

1. Revised Water balance with detailed break up of water consumption, reuse and waste water

generation with quality of treated waste water discharge to underground GIDC drain.

2. Revised details for recovery of fresh C4 Olefin solvent along with other high vapour pressure solvents

Page 18 of 52


Page 18 of 52

considering consumption in product.

3. Revised CER details as per the MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment

Responsibility” (CER). The details of fund allocation and activities for CER shall be incorporated in

EIA/EMP report based on need-based survey.

4. .Revised details of Hazardous waste as per the Hazardous and Other Waste (Management and

Transboundary Movement)Rules 2016.

9 SIA/GJ/IND2/19982/2017 Tatva Chintan Pharma Chem Pvt. Ltd. (Unit-2),Plot: Z/103/F/2, Dahej, SEZ, Part-II,Vagra,Bharuch

EC Amendment

Project Proponent could not attend the meeting. Committee decided to defer the proposal in one of

the upcoming SEAC meeting.

10 SIA/GJ/IND2/28455/2018 M/s. Vaidik Industries Plot No- C-218, Saykha Industrial Estate, Ta: Vagra, Dist.: Bharuch

Screening and scoping


Project status: New

• This office has received an application vide their online proposal no. SIA/GJ/IND2/28455/2018 dated

10/08/2018 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 a new unit proposes for Synthetic Organic Chemicals manufacturing plant as tabulated below:

SR. NO PRODUCT NAME Proposed

1. Dyes

1. Reactive Orange ME2RL

600

MT/Month

2. Reactive Orange 122 AA

3. Reactive Orange H2R

4. Reactive Yellow 160

5. Reactive Yellow M8G

6. Reactive Red 223

7. Reactive Blue R

8. Reactive Violet 5R

9. Reactive Red ME6BL

10. Reactive Yellow ME4GL

11. Reactive Blue M2R

12. Reactive Blue 220




16. Reactive Blue PGR

Page 19 of 52


Page 19 of 52

17. Reactive Black 5

18. Reactive Black B

19. Reactive Black HN

20. Reactive Black RL




24. Reactive Blue 5RH

25. Reactive Blue P3R

26. Reactive Blue BB,BF

27. Reactive Blue GG(203)

28. Reactive Blue HEGN

29. Reactive Blue HERD(Blue 160)

30. Reactive Blue ME2RL

31. Reactive Golden Yellow RNL

32. Reactive Green HE4BD

33. Reactive Orange M2R

34. Reactive Orange W3R

35. Reactive Red BB(21)

36. Reactive Red CD

37. Reactive Red H7B(Red 227)

38. Reactive Red H8B

39. Reactive Red HE3B

40. Reactive Red HE7B

41. Reactive Red ME3BL(Red 194)

42. Reactive red ME4BL

43. Reactive Red P2B

44. Reactive Red P6B

45. Reactive Red PB

46. Reactive Yellow F3R

47. Reactive Yellow H7GL (Yellow 157)

48. Reactive Yellow HE4G (Yellow 88)

49. Reactive Yellow HE4R(84)

50. Reactive Yellow HE6G(Yellow 135)

51. Reactive Yellow MERL

52. Reactive Yellow P6G

53. Acid Black 194

54. Acid Black 234

55. Direct Black 22

56. Acid Black 210

57. Direct black 168

58. Direct Black 80

59. Acid Brown 14

2. Intermediates

1. NMJ (N Methyl J Acid) 20

2. Sulfo J Acid 20

Page 20 of 52


Page 20 of 52



• The project proponent along with their expert /consultant M/s. Satva Environ Consultancy attended

the meeting and made presentation before the committee


Sr. no.

Particulars Details


5.0 Crores

B Total Plot area ( sq. meter) 3978 Sq. m.

Green belt area ( sq. meter)

800 Sq. m.

C Employment generation Direct: 20 Indirect : 10 Total : 30

D Water

i


GIDC Supply

Status of permission from the concern authority.


Category Water Consumption KLD Remarks

(D) Domestic 4.0

Out of total Water requirement of 120 KLD, 53.5 KLD Water reuse in process and washing and 66.5 KLD Water received through GIDC

(E) Gardening

(F) Industrial

Process *50.5 (R) + 43.5 (F)

Washing *3.0 (R)

Boiler 20.0

Cooling 10.0

Industrial Total 116.0

Total (A + B + C) 120.0

Note: *53.5 KLD Reuse From MEE Condense Water

4) Total water requirement for the project: 120 KLD 5) Quantity to be recycled: 53.5 KLD 6) Total fresh water requirement: 66.5 KLD


Category Waste water generation KLD Remarks (C) Domestic 1.8 (D) Industrial

Process 63.0 69.0 KLD waste water send to

Washing 3.0

Boiler 2.0

3. 2-Pyridone 10

4. OVAS 10

5. K acid 5

6. G Salt 20

7. Bromamine Acid 5

Page 21 of 52


Page 21 of 52

Cooling 1.0 primary, secondary and tertiary ETP plant followed by MEE

Scrubber spent Acid 0.08


69.0

Total [A + B] 72.0

-

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

Sr. No. Name of Unit Capacity

1 Collection Tank 100 KL

2 Primary Settling Tank 25 M3

3 Aeration Tank 100 M3

4 Secondary Settling Tank 25 M3

5 Sludge Drying Bed 15 M3

6 Filter Feed Tank 5 M3

7 Activated Carbon Filter 5 M3

8 Multi Effect Evaporator 10 M3/Hour


Domestic:

Domestic 1.8 KLD sewage generated will be disposed through soak pit/septic tank.

Industrial:

Total Waste Water generation 69.0 KLD from manufacturing activity and other ancillary operation Waste Water treated Primary and secondary and tertiary Effluent treatment. After than it will be send In House MEE. The Condensate of MEE will reuse in Process and Washing to achieve Zero liquid Discharge. We will maintain Zero Liquid Discharge till CETP of Saykha will commission. After commissioning of Saykha CETP, we will discharge wastewater to CETP after obtaining requisite permission from concern Authority. We assure you that we will operate adequate treatment technology to achieve norms prescribed by CETP

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

We will obtain necessary permission to discharge generated wastewater to CETP Saykha and till then we will maintain Zero Liquid Discharge.

Membership of Common facility (CF) (For waste water treatment)

Unit will achieve Zero liquid Discharge. We will maintain Zero Liquid Discharge till CETP of Saykha will commission. After commissioning of Saykha CETP, we will discharge wastewater to CETP after obtaining requisite permission from concern Authority. We will obtain membership of common facility for disposal of Hazardous waste after before obtaining CC&A from State PCB

vii Simplified water balance diagram with reuse / recycle of waste water

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Page 22 of 52

viii Reuse/Recycle details (KLD)

Total reuse 53.5 KLD

Source of waste water for reuse with quantity in KLD

Application area with quantity in KLD

Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.)

Condensate of MEE 53.5 KLD

Process 50.5 KLD COD : 200 – 300 mg/L BOD: 50-70 mg/L TDS: 1200-1500 mg/L Washing 3.0 KLD

E Air

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

-

Sr. no.

Source of emission

With Capacity


Type of Fuel

Quantity of Fuel MT/Day

Type of emissions

i.e. Air Pollutants


Measures (APCM)

1

Industrial steam

Boiler (4 TPH)

11.00 Imported Coal OR

Agro waste

17 MT/Day

OR 20

MT/Day

PM SO2

NOx

Multi cyclone

Separator followed by Bag Filter with water scrubber

2 Hot Air

Generator (2 Nos.)

11.00 Imported Coal OR

Agro waste

13 MT/Day

OR

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Page 23 of 52

15 MT/Day

3 D. G. Set 5.00 HSD 10 L/hr Acoustic Enclosure

-


-

Sr. no. Source of emission Type of

emission



(APCM)

1 Spray Dryer (1000

LPH) PM 11.00

Multi cyclone Separator followed by water scrubber 2

Spray Dryer (1500 LPH)

3 Reactor (NMJ product) SO2 7.00 Alkali scrubber

4 Reactor (OAVS) HCl 7.00 Two Stage Water

scrubber

5 Reactor (K Acid) SO2 7.00 Alkali scrubber

6 Reactor (G Salt) HCl SO2

7.00 Water scrubber

followed by Alkali Scrubber

7 Reactor (Bromamine

Acid ) HCL 7.00

Two Stage Water scrubber

-

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

� The entire manufacturing activities will be carried out in the closed reactors and regular checking and maintenance of reactors will be carried out to avoid any leakages.

� The tank vents will be equipped with either a carbon filter or an oil trap to prevent water vapor from entering the tank as it breathes.

� All the motors of pumps for the handling of hazardous chemicals will be flame proof and provided with suitable mechanical seal with stand-by arrangement

� Control of all parameters on a continuous basis will be done by adequate control valves, pressure release valves and safety valves etc.

� All the flange joints of the pipe lines will be covered with flange guards. � All the raw materials will be stored in isolated storage area and containers tightly

closed. � There will also be provision of adequate ventilation system in process plant and

hazardous chemical storage area. � A regular preventive maintenance will be planned to replace or rectify all gaskets,

joints etc. � The unit will also develop green belt within the factory premises to control the

fugitive emission from spreading into surrounding environment

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

i

Page 24 of 52


Page 24 of 52

Sr. No

Types of Hazardous

Waste

Specific Source of generation

Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Management of HW

1 ETP

Sludge ETP Area 35.3

108.0 MT/Year

Collection, storage, Transportation and Dispose to Active

TSDF Site

2 Used Oil Plant

Machinery 5.1

5 lit/year

Collection, storage, Reuse within premises in

maintenance work.

3 Discarded Container/

Bags

Material storage and

Handling 33.1

42 MT/Year

Collection, storage, Transportation and

Dispose to Registered Recycler

4 Process Waste Sludge

Dyes Intermediates

26.1 24

MT/Year


Dispose to TSDF Site

5

Spent Sulphuric Acid (30-

35%)

Dyes Intermediates

(OAVS, K Acid, NMJ

Acid )

26.3 4800

MT/Year

Collection, storage and partially reuse

(3550 MT/Annum) in OAVS, Supho J Acid,

NMJ Acid, G Salt Transportation and

remaining will sell to Rule-9 Authorized

Units

6 Spent HCl

Acid (18-25 %)

Reactive Blue Dyes, OAVS G

Salt, Bromamine

Acid

26.3 2400

MT/Year

Collection, storage and partially reuse

(1500 MT/Annum) in reactive dyes with

fresh HCl and remaining will sell to Rule-9 Authorized

Units

7 Acetic Acid (70 % to 75

%)

Dyes Intermediates

OAVS 26.3

120 MT/Year


sell to Rule-9 Authorized parties

8 Solvent Residue

Distillation Unit

26.1 12

MT/Year


Dispose by sending to common facility

9 Spent

Solvent Bromamine

Acid 26.4

260.4 MT/Year

Collection, storage and Reuse With in

Plant Premises after in house Distillation in

solvent dyes

Page 25 of 52


Page 25 of 52

10 Glauber Salt/ Salt

from ATFD

MEE Operation,

ATFD Operation &

OAVS

26.1 300

MT/Month


Dispose by sending to common facility

11.

SBS (20 To 25%)

K Acid 26.3 80

MT/Annum

Collection, storage and Partially (72

MT/Annum Reuse With in Plant

Premises in OAVS and remaining will be

sell to units having permission of Rules 9

ii Membership details of TSDF, CHWIF etc. (For HW management)

We will obtained after getting NOC from GPCB

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

Not applicable



• Types of Solvent : ODCB

• Spent solvents will be recovered through in-house distillation column with double condenser system with chilling water to achieve optimum recovery

• 95-98% recovery will be carried out.

• Recovered solvents will be collected in receiver and transferred to reaction vessel through vaccum and completely reused within process.

ii VOC emission sources and its mitigation measures • Sources of fugitive emissions include storage of chemicals, solvents storage, loading

and unloading section, raw material handling and, hazardous waste storage area

Measures : • The fugitive emissions in terms of handling losses will get reduced by proper storage

and handling.

• Hazardous chemicals will be stored as per standard criteria. • Periodically monitoring will be carried out as per the post project monitoring plan.

• Proper ventilation in storage & production area shall be ensured

• All materials must be stored in suitable packing to prevent contamination of air .

• Enclosed system & efficient procedures for materials charging shall be ensured.

• Procedures for start-up shut down, operation & maintenance procedures shall be established & maintained.

• The coverage of greenbelt around the plant also acts as natural barrier to stop carrying of dust along with the wind current



Observation:

• This proposal is for a new synthetic organic chemical product.

• Total water consumption will be 120.0 KLD. Total wastewater generation will be 69.0 KLD. 69.0 KLD

waste water send to primary, secondary and tertiary ETP plant and then treated effluent will be sent

to four stage evaporator and thus maintain complete zero liquid discharge.

• They will maintain Zero Liquid Discharge till CETP of Saykha will commission. After commissioning of

Saykha CETP, they will discharge wastewater to CETP after obtaining requisite permission from

Page 26 of 52


Page 26 of 52

concern Authority. They assure you that we will operate adequate treatment technology to achieve

norms prescribed by CETP

• Imported coal and agro waste will be used as fuel for boiler and Hot air Generator.

• Adequate APCM will be provided commonly with boiler and hot air generator.

• Separated adequate APCM will be provided with reactors.

• Hazardous waste management will be as per the HW Rules 2016.


Committee deliberated on area adequacy, waste water management, waste streams, APCM, Hazardous

waste, safety aspects for handling of all the proposed raw materials, products and hazardous waste to be

handled during manufacturing activities.

Considering the above project details, after detailed discussion, the terms of reference (ToR) were

prescribed as below and as per the standard TOR for the Synthetic Organic Chemical projects

recommended by SEAC vide letter no. EIA-10-GEN-21/1480 dated 14/09/2017 and approved by SEIAA

in its 12th meeting dated 16/09/2017 for the EIA study to be done covering 10 Km radial distance from

the project boundary.

1. Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment

Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be

made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities

therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP

report.

2. Adequacy of proposed area with respect to plant machineries , EMS, green belt , safety aspect,

raw material & product storage considering worst case scenario. Submit proper lay out plan

clearly demarcating all activities with scale.

3. Segregation of waste water streams based on characteristics and its proper management and

detailed treated waste water management after ETP with qualitative analysis.

4. Treatability & adequacy report for complete ZLD system. Feasibility report for complete reuse

condensate waste water for industrial purpose.

5. Explore the use of renewable energy to the maximum extent possible. Details of provisions to

make the project energy-efficient through of energy efficient devices and adoption of modes of

alternative eco-friendly sources of energy like solar water heater, solar lighting etc. Measures

proposed for energy conservation.

6. Selling of hazardous waste like spent acid to units having permission under Rule-9 of HWR 2016

and also submit MoU with them with quantity.

7. Qualitative and quantitative analysis of hazardous waste streams like Spent Sulphuric Acid (25-

30%), Spent HCl Acid (18-20 %) from the manufacturing process (Product wise) with their

proposed use within premises with feasibility and adequacy.

8. Qualitative and quantitative analysis of hazardous waste streams like Process Waste Sludge

Page 27 of 52


Page 27 of 52

(26.1) and solvent residue generation from the manufacturing process (Product wise).

9. To Explore the possibility to reuse such waste streams within premises as raw materials for other

products or to convert it into valuable products instead of selling out side. Sound management of

such waste streams as per the HW Rules 2016 as amended time to time. Feasibility report for

utilization of hazardous waste shall be incorporated in EIA report.

10. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard &

Occupational health hazards during unloading, storage, transportation, handling and processing

of hazardous chemicals like solvents, Toluene etc.

11. Safety precautions for solvents as per the PESO standards.

12. Submit Narcotics department permission for use of acetic anhydride and its management of

handling.

13. Justification for water consumption and waste water generation not in proportion with the product

quantity

The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs

available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be

considered as generic TORs for preparation of the EIA report in addition to all the relevant information as per

the generic structure of EIA given in Appendix III in the EIA Notification, 2006.

The project proponent shall have to apply for Environmental clearance through online portal http://environmentclearance.nic.in/ along with final EIA report.

11. SIA/GJ/IND2/28468/2018 M/s. Uma Pharma Chem Plot No. : 111, GIDC Gozaria, Taluka: Mehsana, District: Mehsana, Gujarat.

Screening and scoping


Project status: New




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

Sr. No.

Name of the Products

CAS no. /CI no.

Quantity MT/Month

End-use of products

1 Metallic Stearate (Zinc, Magnesium, Lead, Calcium)

557-05-01, 557-04-01, 1072-35-1, 1592-23-0

800 Use in Polymers & Rubber, Pharmaceutical & Cosmetics, Building & Construction.

2 Metallic Octoate (Zinc, Lead, Cobalt)

557-09-5, 7319-86-0, 13586-82-8

600 Use in Polymers & Rubber industries.

3 PVC Stabilizer 26636-01-1 300 Use in Construction application.

Page 28 of 52


Page 28 of 52



• The project proponent along with their expert /consultant M/s. Enviro Fluid Consultants., Ahmedabad attended the meeting and made presentation before the committee

• Salient features of the project are as under :

Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 0.95 Crores

B Total Plot area ( sq. meter) 1088 Sq. m.

Green belt area ( sq. meter) 360 Sq. m. (33%)

C Employment generation 12

D Water

i


GIDC water supply

Status of permission from the concern authority. Permission obtained from GIDC


Category KLD Remarks

(G) Domestic 4 Fresh water (H) Gardening 1.8 Fresh water (I) Industrial

Process 0.0

Washing 0.2 Fresh water

Boiler 0.0

Cooling 0.0

Others 0.0


Total (A + B + C) 6.0

7) Total water requirement for the project: 6.0 KLD 8) Quantity to be recycled: 0.0 KLD 9) Total fresh water requirement: 6.0 KLD


Category Waste water KLD

Remarks

(E) Domestic 3.0 Septic tank followed by soak pit

(F) Industrial

Process 0.0

Washing 0.2 To ETP

Boiler 0.0

Cooling 0.0

Others 0.0


0.2

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

Page 29 of 52


Page 29 of 52

ETP – Neutralization followed by Sludge separation followed by Evaporation (50 L/Hr capacity Thermic Evaporator).


Domestic: Domestic: Soak pit

Industrial: Industrial: Zero liquid discharge

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

Not applicable

Membership of Common facility (CF) (For waste water treatment)

Not applicable


Source of Water Supply: GIDC Supply

Total: 6 KL/day

Domestic

4.0 KL/day

Sewage to septic tank & Soak Pit

3.0 KL/day

Washing

0.2 KL/day

Industrial

0.2 KL/day

Wastewater

0.2 KL/day

Gardening

1.8 KL/day

ETP followed by

Evaporator

Zero liquid discharge

Page 30 of 52


Page 30 of 52

Effluent Quality:

Particular Unit Untreated Effluent

Treated Effluent

(Completely evaporated)

pH -- 6.0 - 6.5 7.0 - 7.5

Total Suspended Solids mg/l 150 - 200 < 50

Chemical Oxygen Demand mg/l 300 - 400 < 100

Total Dissolved Solid mg/l 2500 – 3000 2500 - 3000

viii Reuse/Recycle details (KLD)

Total reuse 0.0 KLD

Source of waste water for reuse with quantity in KLD

Application area with quantity in KLD

Remarks regarding feasibility to reuse i.e. w/w characteristics (COD, BOD, TDS etc.)

Not Applicable

E Air


-Sr. no.

Source of

emission With

Capacity


Type of Fuel

Quantity of Fuel MT/Day

Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 Thermic

Fluid Heater

15 Briquettes/

Coal 65 Kg/Hr

Particulate Matter ≤ 150 mg/Nm

3,

SO2 ≤ 100 ppm, NOx ≤ 50 ppm

Multi Cyclone Separator

followed by Adequate

Stack height


-

Sr. no.

Specific Source of emission

(Name of the Product & Process)

Type of emission



Measures (APCM)

Page 31 of 52


Page 31 of 52

Not Applicable

-

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

Standard handling practices are adopted for powdered chemical. Proper storage, charging system, handling system and online monitoring systems are provided and same will be taken care for proposed project.

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

i

Sr. no.

Type/ Name of

Hazardous waste

Specific Source of generation (Name of the

Activity, Product etc.)

Category and

Schedule as per

HW Rules.

Quantity (MT/Annum)

Management of HW

1 Used/spent

Oil Plant & Machineries 5.1 0.01

Collection, storage,

Transportation and reuse

within premises for lubrication or disposal to registered recycler.

2 Discarded

Containers/ bags

Raw materials and products

33.1 6


Transportation & sell to

authorized vendor

3 ETP Sludge

and Wastewater treatment

systems 35.3 9.7


Transportation and Disposal

at TSDF 4

Evaporation Salt

Treated water evaporation

35.3 0.3

-

ii Membership details of TSDF, CHWIF etc. (For HW management)


Not applicable



• There is not any Solvent use as raw material in manufacturing process.

ii VOC emission sources and its mitigation measures • Due to Manufacturing process chances of VOC emissions. Entire process and

material charging has been carried out in closed loop. Regular work place monitoring will be done. Standard SOP will be followed to handle powder and liquid raw materials.

Page 32 of 52


Page 32 of 52



Observation:


• Total water consumption will be 5.0 KLD. Total wastewater generation will be 0.2 KLD. 0.2 KLD

waste water send to Neutralization followed by Sludge separation followed by Evaporation (50 L/Hr

capacity Thermic fluid Evaporator).

• Briquette/coal will be used as fuel for thermic fluid heater.

• Adequate APCM will be provided commonly with thermic fluid heater.



• Committee deliberated on area adequacy, waste water management, ,APCM, Hazardous waste,

safety aspects etc.






1. To address treated waste water quality and evaporation salt generation in consonance to each

other. Feasibility and Adequacy of operation of thermic fluid based evaporator.

2. Adequacy of proposed area with respect to plant machineries , EMS, green belt , safety aspect,

raw material & product storage considering worst case scenario. Submit proper lay out plan clearly

demarcating all activities with scale.

3. Explore the use of renewable energy to the maximum extent possible. Details of provisions to




4. Safety precautions including flame proof electric fittings to be taken to avoid fire hazard &

Occupational health hazards during unloading, storage, transportation, handling.

The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model ToRs

available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical Industry’ shall be

considered as generic TORs for preparation of the EIA report in addition to all the relevant information as per

the generic structure of EIA given in Appendix III in the EIA Notification, 2006.

The project proponent shall have to apply for Environmental clearance through online portal

Page 33 of 52


Page 33 of 52

http://environmentclearance.nic.in/ along with final EIA report.

12. SIA/GJ/IND2/28481/2018 M/s. Gulshan Polyols Ltd . Plot No. 762, 762/1, 762/2, 762/3, 769/1 & 769/2, GIDC Jhagadia, Dist.: Bharuch, Gujarat

Screening & Scoping

+Project / Activity No.: 5(f)





• This is an expansion unit and proposes for expansion of Synthetic Organic Chemicals manufacturing

plant as tabulated below:

Sr. No.

Products Capacity, TPM*

End-use E P T

1. Starch Slurry Powder (90.0 %) 3750 2250 6000 Textile & Food industry

2. Sorbitol (70 %) 6000 6000 12000 Gel toothpaste and ingredient to pharmaceutical products

3. Dextrose Mono–hydrate (98.5 %)

1250 750 2000 Food industry

4. Mannitol Powder (99.5 %) 416 Nil 416 As excipient to Pharmaceutical industries

5. Glucose (99.0 %) 1250 Nil 1250 Food industry

6. Sorbitol Powder (98.5 %) 215 Nil 215 As excipient to pharmaceutical industries

7. Calcium Carbonate (GCC/Wet/ACC), (98.0 %)

1250 Nil 1250 As a filler for PVC, Rubber and Paint

Total 14131 9000 23131

8. Co-Gen power 3.0 MW 1.5 MW 4.5 MW Captive consumption

Sr. No.

By- Products Generation, TPM*

E P T

1. Maize Germ Oil Cake 440 270 710

Used for Cattle feed 2. Maize Germ Oil (88 %) 550 330 880

3. Maize Germ -- 1350 1350

4. Wet Fiber (92 %) 2,750 2500 5250

5. Gluten (90 %) 915 550 1465 Used for poultry food

6. Filter Cake 150 1500 1650 Used for Brick manufacturing

7. Lime Stone Grit (10 %) 150 Nil 150 As a filler for PVC, Rubber and Paint

8. Mud Lime Clay (5 %) 100 Nil 100 Used for Brick manufacturing

*E: Existing, P: Proposed, T: Total

Page 34 of 52


Page 34 of 52



• The project proponent along with their expert / consultant M/s. Envisafe Environment Consultants

attended the meeting and made presentation before the committee


Sr. No.

Particulars Details

A Total cost of the proposed project (Rs. in Crores)

Existing: 122.29 Proposed: 28.43 Total: 150.72

B Total Plot area (sq. meter) 1,27,503

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

Existing: 32,593 Proposed: 9,507 Total: 42,100

C Employment Generation Existing: 246 Proposed: 534 Total: 280

D Water

i

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

GIDC

Status of permission from the concerned authority.: Permission obtained from GIDC

ii Water consumption (KL/day)

-

Category Existing KL/day

Proposed (Additional)

KL/day

Total after Expansion

KL/day Remarks

(J) Domestic 17.5 7.5 25.0 Fresh (K) Industrial

Process

Fresh 260.0 1,680.0 1,940.0 Fresh

Reuse 480.0 280.0 760.0 Reuse

Boiler 340.0 760.0 1,100.0 Fresh

Cooling 246.0 480.0 725.0 Fresh

Washing 40.0 160.0 200.0 Fresh

Total (A+B) 1,383.5 3,367.5 4,750 Fresh: 3,990 Reuse: 760

1) Total water requirement for the project: 4,750 KLD 2) Quantity to be recycle: 760 KLD 3) Total Fresh water requirement: 3,990 KLD

iii Waste water generation (KL/day)

Category Existing KL/Day

Proposed (Additional)

KL/day

Total after Expansion

KL/day Remarks

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Page 35 of 52

(G) Domestic 17.5 2.5 20.0

(H) Industrial

Process 690.0 1,650.0 2,340.0

Boiler 100.0 720.0 820.0

Cooling 30.0 370.0 400.0

Washing 40.0 160.0 200.0


860 2,900.0 3,760.0 Generation: 3,760 Reuse: 760 Discharge: 3000

-

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

Unit Status

Hydraulic Load, KLD Design

Capacity, KLD Existing

After Proposed Expansion

ETP-1

Existing

325 670 1150

ETP-2 540 3090 4200

RO 325 760 1100

MEE-1 480 670 850

MEE-2 Proposed -- 190 350


Domestic: 20 KLD, To soak pit through septic tank

Industrial: 3,000 KLD, After treatment in ETP, discharge into NCTL through GIDC drainage system

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

Narmada Clean Tech (NCT)

Membership of CF

Obtained membership from NCT for discharge of 380 KLD industrial effluent. Unit has booked for additional discharge of 2571 KLD. Unit will apply for additional discharge for proposed expansion.


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viii Reuse/Recycle details (KL/day)

Total Reuse: 760 KLD

Source of waste water for reuse with quantity in

KLD

Application area with

quantity in KLD

Remarks regarding feasibility to reuse i.e. w/w characteristics

(COD, BOD, TDS etc.)

TDS COD BOD

RO – ETP (Permeate): 570 Process & APCM: 760

275 67 17 MEE Condensate: 190

E Air


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Details of Flue Gas Stacks

Sr. No.

Source of emission

with capacity

Status Ht &

Dia, m

Fuel Name & Qty.

Type of Emission & Permissible

limit

APCM

1. Steam Boiler-1 (20TPH)

Existing

40 & 1.2

(Com-mon

Stack)

Coal/ Lignite

300 MT/day

PM ≤ 150 mg/Nm

3

SO2 ≤ 100

ppm

NOx ≤ 50

ppm

Electrostatic Precipitator-1

2. Steam Boiler-2 (30 TPH)

Proposed Electrostatic Precipitator-2

(Common)

3. Steam Boiler -3 (30 TPH)

Proposed

4. DG Set (1450 KVA)

Existing (Standby -

To Be Dismantled)

8.0 & 0.25

HSD 200

Lit/Day



Existing (Standby -

To Be Dismantled)

8.0 & 0.25



Proposed (Stand-By)

3.0 & 0.10


ii Process gas i.e. Type of pollutant gases (Existing and Proposed)

Details of Process Gas Stacks

Sr.

No. Stack attached to

Ht &

Dia

Meter

Air

Pollutant


Equipment

Type of Emission & Permissible

limit 1st Stage 2nd Stage

1. Absorption tower of

SO2 water plant (Existing)

12*0.3 Sulphur Dioxide

Water Scrubber-A

Absorption Tower-B

SO2≤ 40 mg/NM3

2. Absorption tower of

SO2 water plant (Proposed)

12*0.3 Sulphur Dioxide

Water Scrubber-C

Absorption Tower-D

iii Fugitive emission details with its mitigation measures. (Existing and Proposed)

There will be a chance of fugitive emission and odor nuisance during manufacturing process as well as due to storage & handling of raw materials and products. The unit takes following precaution for the control of fugitive emission and will implement the

Page 38 of 52


Page 38 of 52

same for the proposed expansion.

Probable Sources Control Measures

Manufacturing activities during charging into reactors

• Liquid raw materials are charged by pumping & closed

loops.

• Dosing is done by metering system to avoid fugitive

emissions.

• Dedicated measuring tanks are provided to each reactor.

• Usage of closed handling system for odorous chemicals

/solvents as far as possible.

Chemical vapor from wet cake in filtration and drying area

• Covered transfer systems will be adopted, workers shall be provided PPE.

• Fume extraction systems will be provided, wherever required

Emission from bulk storage tanks during storage, loading, unloading

• Breather valves, PSVs, Rupture disc, Vapor recovery

system are installed for process/storage tank vents.

• Unit adopts bulk handling of odorous chemicals and avoid

usage of drums/carboys for such materials

Hazardous chemical storage area

• Dedicated storage area is provided

• Adequate ventilation systems are provided

• All the containers are kept tightly closed

• Trolley/Forklift is used for transfer of drums and containers

• Transfers of odorous waste is preferably during day time.

Transfers during odd hours is avoided.

Pump and compressor Emissions

• Mechanical seals are provided in pumps and agitators

• Standby arrangement for critical equipment and parts is

ensured.

• Drip trays will be placed for each pump to collect leakages

and spillages.

Pressure relief valve emission from pipelines

• For highly pressurized lines, vent pipes of PRVs are

connected in case of toxic gases.

Valves, Flanges, plugs and instrument connections

• Welded pipes are used wherever feasible.

• Suitable gasket materials are used.

• Suitable glad packing is used in valves.

• Periodic inspection and maintenance of pipes and pipe

fittings is carried out.

Release from sampling lines

• Closed loop system is used.

Hazardous chemical storage area

• Provision of dedicated storage area

• Adequate ventilation system to be provided

• All the containers will be kept tightly closed

• Trolley/Forklift will be used for transfer of drums and containers

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

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Page 39 of 52

i Type of waste

Source Catego-

ry

Quantity per Annum

Method of Disposal Existing

Proposed

Total

ETP Sludge

ETP Sch - 1

35.3 700 MT 1344 MT

2044 MT

Collection, Storage, Transportation and Disposal at TSDF of M/s. Bharuch Enviro Infrastructure Ltd.

Filter Acid Mfg of Prod.2

Sch - 1 35.1

40 MT 70 MT 110 MT


Off. Sp. Product

Mfg of Prod.

Sch - 1 28.4

38 MT 70 MT 108 MT


Spent Resin

Mfg of Prod.

Sch - 1 35.2

2.0 KL 5 KL 7 KL

Collection, Storage, sent to manufacturer /authorized regenerator

Spent Catalyst

Mfg of Prod2 & 4

Sch - 1 28.2

33.0 MT 72 MT 105 MT

Collection, Storage, Transportation to Registered Recycler

Discarded Containers

Raw Material Storage & Handling

Sch - 1 33.1

1120 Nos.

2100 Nos. 3220 Nos.

Collection, Storage, Décontamination, reuse/sell Bags/

Liners Sch-1 33.1

10 Nos. 25 Nos. 35

Nos.

Spent Oil/ Used Oil

Plant & Machineries

Sch - 1 5.1

0.10 KL 0.20KL 0.30 KL

Collection, Storage, Transportation, Disposal by selling to Registered Rerefiners OR Reused as Lubricant within premises

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

Unit has obtained membership from BEIL for disposal of hazardous waste from existing plant. Unit will obtain permission for disposal of additional hazardous waste generated from GPCB approved CHWIF/TSDF.


Not applicable

G Solvent management, VOC emissions etc

i Types of solvents, Details of Solvent Recovery, % Recovery. Reuse of recovered solvents

Not Applicable


Page 40 of 52


Page 40 of 52

As mentioned in section E (iii) above



Observation:


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

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 4,750 KLD. Total wastewater generation will be 3,760 KLD. Waste

water will be treated in full fledged primary, secondary and Tertiary ETP units and RO plant and

MEE. After full-fledged treatment, 760 KLD will be reused back in process while 3000 KLD will be

discharged into GIDC underground drainage.

• Unit have applied for additional quantity of discharge of effluent.

• Coal/Lignite will be used as fuel for proposed steam boilers.

• Adequate APCM will be provided with boilers.

• Adequate APCM will be provided with absorption SO2 tower plant.



• Committee deliberated on area adequacy, waste water management etc. It is noted that PP indents

to discharge 3000 KLPD treated waste water. Referring to the quality of treated waste water, PP was

asked to explore reuse of the treated waste water.






1) To address requirement of additional water considering proposed expansion with details of

process advancement used for existing and proposed product.

2) To explore quality of treated waste water of 3000 KLPD intended for discharge and its reuse with

revised water balance diagram.

3) Compliance of MoEFCC’s OM dated 01/05/2018 regarding “Corporate Environment

Responsibility” (CER). Fund allocation for Corporate Environment Responsibility (CER) shall be

made as per MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 for various activities

therein. The details of fund allocation and activities for CER shall be incorporated in EIA/EMP

report.

Page 41 of 52


Page 41 of 52

4) Adequacy of proposed area with respect to plant machineries , EMS, Reuse of treated

wastewater, green belt , safety aspect, raw material & product storage considering worst case

scenario. Submit proper lay out plan clearly demarcating all activities with scale.

5) Explore the use of renewable energy to the maximum extent possible. Details of provisions to




6) Details of the treatability and feasibility of waste water to be disposed off by means of MEE and

its impact on Environment and Human Health. Submit Adequacy of MEE alongwith quantity of

MEE condensate generation and evaporation of waste water in MEE.

7) Submit certificate regarding additional discharge of waste water into GIDC underground drainage

leading to NCTL.

8) Submit EC order compliance verification report from RO-Ankleshwar for existing plant.

• The TOR prescribed as above and as per the standard TOR approved by SEIAA and the model

ToRs available in the MoEFCC’s sector specific EIA Manual for ‘Synthetic Organic Chemical

Industry’ shall be considered as generic TORs,for preparation of the EIA report in addition to all the

relevant information as per the generic structure of EIA given in Appendix III in the EIA Notification,

2006.

• The project proponent shall have to apply for Environmental clearance through online portal

http://environmentclearance.nic.in/ along with final EIA report.

13. SIA/GJ/IND2/28110/2018 M/s. Kenrik Polymers Pvt. Ltd. Survey No: 160, Village: Rayaniya, Tehsil: Talod, Dist.: Sabarkantha

Screening & Scoping

Project Proponent could not attend the meeting. Committee decided to defer the proposal in one of

the upcoming SEAC meeting.

14. SIA/GJ/IND2/28501/2018 M/s. Pravin Industries Plot No: C1-6118, Phase IV, Notified Industrial Area, GIDC-Vapi, 396195, Tal.: Pardi, Dist.: Valsad (Gujarat)

Screening & Scoping



• This office has received an application vide their online proposal no.

SIA/GJ/IND2/28501/2018 dated 10/08/2018 regarding grant of Terms of Reference [ToR] for

preparation of EIA/EMP report.


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

tabulated below:

Page 42 of 52


Page 42 of 52

Sr.No. Product CAS No. Capacity, TPM


1.1 Direct Scarlet 4 BS 3441-14-3 8.0 0

8.0

1.2 Direct Red 12 B 5001-72-9

1.3 Acid Scarlet MOO 5413-75-2

1.4 Basic Bismarck Brown 8005-77-4

1.5 Chroysidine 4438-16-8

1.6 Acid Orange-II 633-96-5

1.7 Basic Auramine-O (Basic Yellow-2)

2465-27-2 17.0 25.0

2.0 Methyl Violet Liquid OR

Malachite Green Liquid OR

Diamond Green Liquid OR

Victoria Blue Liquid OR

Auramine Liquid

8004-87-3

569-64-2

18015-76-4

2580-56-5

492-80-8

0 25.0 25.0

3.0 Methyl Violet Crystal (Crude)

OR Malachite Green Crystal

(Crude) OR

Diamond Green Crystal (Crude)

OR Victoria Blue Crystal (Crude)

OR Auramine-OF (Solvent

Yellow-34)

8004-87-3

569-64-2

18015-76-4

2580-56-5

492-80-8

0 25.0

25.0

Total 8.0 67.0 75.0

• 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. Eco Chem Sales & Services,

Surat attended the meeting and made presentation before the committee


Sr.no.

Particulars Details


Existing: 112.33 Lakhs Proposed: 51.50 Lakhs Total: 163.83 Lakhs

(1) Capital cost for EMS (Environmental Management System): 10.00 Lakhs (2) Recurring cost towards the environmental protection measures: 17.25 Lakhs per Annum.

B Total Plot Area ( sq. meter)

Existing: 806.00 sq. meter Proposed: 0.00 sq. meter (development on open land of existing plant) Total: 806.00 sq. meter

Page 43 of 52


Page 43 of 52

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

Existing: 150 sq. meter Proposed: 00 sq. meter Total: 150 sq. meter

C Employment Generation:

1. Direct Existing: 10 Nos. Proposed: 10 Nos. Total: 20 Nos.

2. Indirect Existing: 4 - 7 Nos. Proposed: 5 - 9 Nos. Total: 9 - 15 Nos.

D Water:

i

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

GIDC, Vapi Water Supply

Status of permission from the concern authority Water Permission Letter Vide Letter No.: GIDC/DEE/(W/S)/NA/VAPI/1582 dated 18/07/2018.

ii Water consumption (KLD):

# Particulars

Water Consumption, KLD


A. Domestic 2.0 0 2.0

B. Industrial

1. Processing, Washing & Scrubber 8.0 21.58 29.58

2. Boiler 1.0 2.0 3.0

3. Cooling 2.0 1.0 3.0

4. Floor/Container Washing 1.0 0.5 1.5

Total Industrial 12.0 25.08 37.08

C. Gardening 1.0 0 1.0

Grand Total (A+B+C) 15.0 25.08 40.08

D. Recycle as MEE Condensate 0 26.46 26.46

Net Fresh Water (A+B+C-D) 15.0 -1.38 13.62

1) Total water requirement for the project: 40.08 KLD 2) Quantity to be recycle: 26.46 KLD 3) Total fresh water requirement: 13.62 KLD

iii Wastewater generation (KLD):

# Particulars

Effluent Generation, KLD


A. Domestic 1.8 00 1.80

B. Industrial

1. Processing, Washing & Scrubber 8.00 25.66 33.66

2. Boiler 0.00 0.50 0.50

3. Cooling 0.00 0.50 0.50

4. Floor/container washing 1.00 0.50 1.50

Total Industrial 9.00 27.16 36.16

C. Gardening 0.00 00 00

Grand Total (A+B+C) 10.80 27.16 37.96

Septic Tank/Soak Pit 1.80 00 1.80

To CETP 9.00 00 9.00

To MEE/Centrifuge 00 27.16 27.16

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

ETP: 10 KLD MEE: 30 KLD

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v Mode of Disposal & Final meeting point Domestic Effluent: Domestic waste water (1.80 KLD) is being/will be passed through Septic Tank.

Industrial Effluent: Total Industrial Waste Water Generation will be 36.16 KLD, 27.16 KLD process effluents will be treated in proposed MEE Plant and 9.00 KLD will be treated in existing primary, & tertiary effluent treatment plant and finally treated effluent will be disposed off into CETP Vapi for further treatment and disposal into Arabian Sea.

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

CETP, Vapi.

Membership of Common facility (CF) CETP Membership Certificate Vide Letter No.: REF:CETP_Member.Certi/150/18282 dated:01/12/2012

vii Reuse/Recycle details (KLD) 26.46 KLD of MEE Condensate will be reused.

E Air [Existing & Proposed]:


Existing: There is no flue gas as well as process gas emission from existing plant. Unit is not used any D.G. set also, hence no emission from D. G. set is expected.

#

Source of Emission

With Capacity e.g. Boiler (8 TPH)


Name of the Fuel

Quantity of Fuel MT/h & MT/Day

Type of emissions

i.e. Air Pollutants

APCM Emission Standard

EXISTING

1. Steam Boiler (300 kgs/hr)

11

Natural Gas

20 SCM/hr

PM SOx NOx

Adequate Stack Height

<PM: 150 mg/Nm3,

<SOx:100 ppm <NOx: 50 ppm

2. Thermopack

(2 Lacs K Cal) 11 20 SCM/hr

3. Hot Air Generator

(4 Lacs K Cal) -- 50 SCM/hr

PROPOSED

1. Steam Boiler (600 kgs/hr)

11 Natural

Gas 60 SCM/hr PM

SOx NOx

Adequate Stack Height

<PM: 150 mg/Nm3,

<SOx:100 ppm <NOx: 50 ppm

2. DG Set

(82.5 KVA) 11 HSD 15 Lit/hr

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

# Particulars

Details

Remarks Existing

After proposed Expansion

1.0 Stack attached to Reactor Reactor

Existing will be Modified

APC Provided Three Stage Alkali

followed by Water and Acid Scrubber

Three Stage Alkali followed by Water and

Acid Scrubber

Height of Vent 11 meters 11 meters

Expected Emission NH3: <175 mg/Nm3

Page 45 of 52


Page 45 of 52

H2S : < 10 mg/Nm3

2.0 Stack attached to Spin Flash dryer Spin Flash dryer

Existing

APC Provided Cyclone Separator

followed by Bag Filter Cyclone Separator

followed by Bag Filter

Height of Vent 11 meters 11 meters

Expected Emission PM: <150 mg/Nm3

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

• Concrete road is already developed within plot premises to avoid fugitive dust due to vehicle movement.

• Manufacturing activity is/will be carried out in closed reactors/vessels and

• Regular checking and maintenance of the same is/will be carried out to avoid any leakages. All the raw materials are/will be stored in closed containers and in sealed bags and will be handled through closed system to avoid the handling losses.

F Hazardous Waste: (As per the Hazardous and Other Wastes (Management and Trans boundary Movement) Rules 2016. [Existing & Proposed]

i

Quantity of discarded containers must be in MT/Annum.

# Type Quantity, TPA

Disposal Existing Proposed Total

1. Process Residue (Auramine Sludge)

(Sch: I/26.1) 18.00 391.57 409.57

Sell to actual/authorized users or Dispose off into TSDF, Vapi

2 Process Residue

(Sch: I/26.1) 0.00 199.90 199.90

Dispose off into TSDF, Vapi

3. ETP Waste/MEE Salt

(Sch:I/35.3) 1.80 194.8 196.60

Dispose off into TSDF, Vapi

4. Used Oil

(Sch: I/5.1) 0.01 0.01 0.02

Collection, storage & sell to register recycler

5. Discarded Containers

(Sch:I/33.1) 2.00 1.00 3.00

Collection, storage & sell to register recycler

6. Sludge from Wet Scrubber

(Sch:I/37.1) 0.00 1.00 1.00

Dispose off into ETP along with scrubbing water

ii Membership details of TSDF, CHWIF etc.

VWEMCL certificate for CETP for acceptance of additional effluent vide letter No. CETP_Member.Certi/150/18282 dated: 01/12/2012 & Common Solid waste disposal membership No. 87 dated 01/12/2012


Nil


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

No Solvents are being/will be used

ii VOC emission sources and its mitigation measures NIL



Page 46 of 52


Page 46 of 52

Observation:

• This proposal is for expansion of unit proposes for a synthetic organic chemical product.

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

• Total Water consumption will be 40.08 KLD. Total Waste Water generation 36.16 KLD from

manufacturing activity and other ancillary operation in which 27.16 KLD process effluent will

be treated in proposed MEE Plant and 9.00 KLD will be treated in existing primary, & tertiary

effluent treatment plant and finally treated effluent will be disposed off into CETP Vapi for

further treatment and disposal into Arabian sea.

• Natural gas will be used as fuel for proposed boiler, thermopack and hot air generator.

• Separate Adequate APCM will be provided to control process gas emission with existing and

proposed reactor.


• As the proposal is for expansion, compliance of action taken by the GPCB was deliberated. It

is noted that three subsequent show cause notices have been issued to the unit which was

not satisfactorily addressed by the PP. Committee felt a latest status on compliance of CCA

conditions verified by the GPCB. It is further noted that plot area is 806 M2 and unit is

intending to expand from 8 MTPM to 75 MTPM with provision of green belt. Hence PP was

asked to submit area adequacy in context to storage of the raw materials, erection of new

equipments, area for storage of finished goods etc. for the existing and proposed products

with proposed green belt. Detailed water consumption and waste water generation was

deliberated and Committee asked PP to readdress water balance with detailed treatability and

adequacy of treated waste water management.

• Committee also deliberated on hazardous waste management, process gas emission, Safety

aspects etc.



meeting.

1. Certified compliance report of CCA conditions validated by GPCB along with details status of reasons

mentioned in show cause notices issued by GPCB.

2. Area adequacy in context to storage of the raw materials, erection of new equipments, area for

storage of finished goods etc. for the existing and proposed products with proposed green belt.

3. To readdress water balance with detailed water consumption, waste water generation, its treatability

and adequacy of reuse.

15. SIA/GJ/IND2/28513/2018 M/s. Rishabh Dye Chem Industries

Plot No. 223, GIDC Industrial Estate, GIDC Ankleshwar, Dist-Bharuch.

Screening & Scoping

Page 47 of 52


Page 47 of 52


Project status: New

• This office has received an application vide their online proposal no. SIA/GJ/IND2/28513/2018

dated 10/08/2018 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.


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

Sr. No.

Name of the Products CAS no. Quantity

MT/Month End-use of products

1 2 Amino 2' Methyl Di Phenyl Crysyl Ether

3840-18-4

36.00

In Dyes Intermediates & Pharmaceuticals Industry

2 2,4 Di-Chlro O-Amino Di Phenyl Ether

26306-64-9 In Dyes Intermediates & Pharmaceuticals Industry

3 2 Amino 4 Chloro Diphenyl Ether


4 Amino Resorcinol Di O Crysyl Ether


5 Ortho Amino Di Phenyl Ether


6 Pera Amino Di Phenyl Ether 139-59-3 In Dyes Intermediates & Pharmaceuticals Industry

7 2 Amino 4 Chloro 2'4' Di Chloro Di Phenyl Ether


8 4,4' Di Chloro 2 Amino Di Phenyl Ether


• 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. Earthcare Enviro Solutions Pvt.

Ltd.,Surat attended the meeting and made presentation before the committee


Sr. no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores): Rs. 3.16 Crores

B Total Plot area ( sq. meter) 704.00 Sq. m.

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

70.00 Sq. m.

C Employment generation Male: 21 + Female: 02 = 23

D Water

Page 48 of 52


Page 48 of 52

i

Source of Water Supply

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

GIDC, Ankleshwar

Status of permission from the concern authority.

Unit has got permission from GIDC for water supply.


Category KLD

(A) Domestic 1.00

(B) Gardening 0.28

(C) Industrial

Process 3.00

Washing 1.50

Boiler 22.00

Cooling 2.50

Others --


Total (A + B + C) 30.28

1) Total water requirement for the project: 30.28 KLD

2) Quantity to be recycle: Nil

3) Total fresh water requirement: 30.28 KLD


Category Waste water

KLD

(A) Domestic 0.80

(B) Industrial

Process --

Washing 1.20

Boiler 1.00

Cooling 0.10

Others --


2.30

Total [A + B] 3.10

iv

Treatment facility within premises with capacity

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

In-house ETP (Capacity: 5.0 KLD) having primary treatment will be installed.


Page 49 of 52


Page 49 of 52

Domestic: Domestic effluent shall be disposed in to Septic tank / Soak pit system.

Industrial:

There shall be no any process wastewater generation from manufacturing process activity. Wastewater generated from other ancillary industrial operations shall be allowed into in-house ETP for primary treatment. Primary treated water will be sent to the Common MEE facility of M/s. BEIL.

vi

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

Common MEE Facility: M/s. BEIL, Ankleshwar.


Unit has got NOC from M/s. BEIL.


--

E Air

i

Flue gas emission details

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

Sr. no.

Source of emission

With Capacity

Stack

Height (meter)

Type of

Fuel

Quantity of Fuel

MT/Day

Type of emissions

i.e. Air Pollutants


(APCM)

1 Steam Boiler

(Capacity: 1 TPH) 12.00 m

Natural Gas

400.00 m3/day

PM

SO2

NOx

Adequate stack height will be provided

2

Thermic Fluid Heater (2 Nos.) (Capacity: 2 Lac Kcal/hr each)

12.00 m Natural

Gas 300.00 m3/day

3

D. G Set

(Stand By)

(Capacity: 300 KVA)

6.00 m HSD 81.00

Lit/hr


Not Applicable


As below:

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

manufacturing process and from vehicle movement on internal road.

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

while liquid material will be charged through pipeline.

• Transportation of raw materials & products will be carried out by trolley within premises and

minimum manual material handling will be carried, so the fugitive emission due to process

activity and material handling will be minimized.

F

Hazardous waste

(As per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016.

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 Sludge Effluent

Treatment Plant

35.3 (Sch-I)

2.00 MT/year

Collection, Storage,

Transportation and Disposal at

TSDF site – for secured landfill

2. Used Oil D. G Set &

Thermopack 5.1

(Sch-I) 0.25

MT/year


Transportation and Disposal by

selling to Registered Re-refiners

approved by GPCB / CPCB OR

reuse for lubrication

3. Discarded Containers / Bags / Liners

Raw material & Finished

product packing material

33.1 (Sch-I)

75 MT/year


Transportation and Disposal by

selling to registered recycler

approved by GPCB / CPCB OR

reuse within premises.

4. Distillation Residue

Process (All products)

20.3 (Sch-I)

98.18 MT/year


Transportation and Disposal for

co-processing/incineration

5. Inorganic

Salt Process

(All products) 28.1

(Sch-I)

375.27

MT/Year



TSDF site for secured landfill

6. Iron Sludge Process

(All products) 28.1

(Sch-I)

218.16

MT/Year



TSDF site for secured landfill

7.

Sodium

Acetate/

Potassium

Acetate

Process (All products)

28.4 (Sch-I)

728.73

MT/Year


Transportation & Disposal by

selling to Authorized end user

as per Haz. Waste Rule-9 and

after getting prior permission

from GPCB.

ii Membership details of TSDF, CHWIF etc. Unit has got NOC from M/s. BEIL for receiving Landfilling waste and Incinerable waste.

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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



Not Applicable

ii

VOC emission sources and its mitigation measures

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

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



Observation:


• Total water consumption will be 30.28 KLD. Total wastewater generation will be 2.30 KLD.

Wastewater generated from other ancillary industrial operations shall be allowed into in-house

ETP for primary treatment. Primary treated water will be sent to the Common MEE facility of M/s.

BEIL

• Natural gas will be used as fuel for boiler after expansion.

• There will be no process gas emission.



Committee deliberated on the all the eight products with proposed manufacturing quantity of 36 MTPM and

asked PP to address worst case scenario based on pollution potential with subsequently break up of

individual production quantity for all the products. It is also noted that there is no process wastewater

generation from manufacturing process activity. Wastewater generated from other ancillary industrial

operations will be sent to ETP for primary treatment. Primary treated water will be sent to the Common MEE

facility of M/s. BEIL. Committee deliberated on area adequacy, waste water management, and safety

aspects of the raw material storage , process operations etc.

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meeting.

1. Adequacy of hazardous waste storage facility proposed/available based on quantum of

hazardous waste generation.

2. To submit break up of individual product with its proposed production.

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

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

5. Shri Rajesh I Shah, Member, SEAC

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

Documents

Minutes of the 438 meeting of the State Level Expert ... Minutes of the 438th I.pdf · Page 1 of 52 438 th meeting of SEAC-Gujarat, Dated 03.10.2018 Page 1 of 52 Minutes of the 438th