minutes of the 454th 28/11/2018 at committee room, geer ... minutes of the 454th i.pdf · removed...

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454th meeting of SEAC-Gujarat, Dated 28.11.2018

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Minutes of the 454thmeeting of the StateLevelExpertAppraisalCommittee held on

28/11/2018 at Committee Room, GEER foundation, Gandhinagar

The 454thmeeting of the StateLevel ExpertAppraisalCommittee (SEAC) was held on 28th

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

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

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

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

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

PFR, EIA-EMP reports and other reports.

1 SIA/GJ/IND2/26041/2017 M/s Lycos Chemtech

Plot. No. 1032/3, GIDC, Panoli-394 116, Tal:

Ankleshwar, Dist. Bharuch, Gujarat

Appraisal

Project / Activity No.5(f) Project status: New

• PP has submitted online application vide no. SIA/GJ/IND2/26041/2017 dated 27/09/2018 for

obtaining Environmental Clearance.

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

11011/208/2017-IA.II vide dated 10th-July-2017.

• Project proponent has submitted EIA Report prepared by Aqua – Air Environmental

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

• This is a new engaged in synthetic organic chemicals and now proposes as tabulated below:

Sr. No.

Name of the Products CAS no. / CI no.

Quantity MT/Month

End-use of products

1 Diethylcarbamazine Citrate 1642-54-2

15

Treatment of filariasis

2 1-[2‐(2‐Hydroxyethyl) Ethoxy] Piperazine (99%)

13349-82-1 Pharmaceutical Intermediate

3 1-(2, 3‐Dichlorophenyl) Piperazine HCl


4 1-Benzylpiperazine (99%) 2759-28-6 Pharmaceutical Intermediate

5 1-(2-Methoxyphenyl) Piperazine HCl (98%)


6 PiperazineHexahydrate 142-63-2 Anthelmintic

7 Piperazine Citrate 144-29-6 Anthelmintic

8 PiperazineAdipate 142-88-1 Anthelmintic

9 PiperazineDihydrochloride 142-64-3 Anthelmintic

10 Piperazine Phosphate 14538-56-8 Anthelmintic

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11 Povidone Iodine 25655-41-8 Treatment of skin infection on

the skin

12 N-Phenyl Piperazine (NPP) 92-54-6 Pharmaceutical Intermediate

13 N-Methyl Piperazine 109-01-3 Pharmaceutical Intermediate

14 1-Amino-4-Methyl Piperazine 6928-85-4 Pharmaceutical Intermediate

15 1- BOCPiperazine 57260-71-6 Pharmaceutical Intermediate

16 Sodium Barbital 144-02-5 Pharmaceutical Intermediate

17 Methoxsalen 298-81-7 Pharmaceutical Intermediate

18 5-Methyl Nicotinic Acid 3222-49-9 Pharmaceutical Intermediate

19 Ciprofloxacin Lactate 97867-33-9 Antibiotic

20 Ciprofloxacin Base 86483-48-9 Antibiotic

21 Mecobalamin 13422-55-4 0.5 Dietary Supplement

Total 15.5

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

Notification 2006.

• PP was called for presentation in the SEAC meeting dated 28/11/2018.

• Salient features of the project are as under:

Sr.

no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 2 Crores

B Total Plot area( sq. meter) 1040 Sq. m.

Green belt area ( sq. meter) 300 Sq. m.

C Employment generation 8

D Water

i

Source of Water Supply(GIDC Bore well,

Surface water, Tanker supply etc...)

GIDC Water Supply

Status of permission from the concern authority. Unit has obtained permission from GIDC

for water supplyvide letter no

NO/GIDC/DEE/PNL/1498 dated

01/04/2017.

ii Water consumption (KLD)

Category

Quantity

KLD

Remarks

(A) Domestic 2.7

(B) Gardening 0.8

(C) Industrial

Process 2.86

Washing 0.4

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Boiler 6.0

Cooling 5.0

Others Nil

Industrial Total 14.26

Total (A + B + C) 17.76

1) Total water requirement for the project: 17.76 KLD

2) Quantity to be recycled: 0 KLD

3) Total fresh water requirement: 17.76 KLD

iii Waste water generation (KLD)

Category Waste water

KLD

Remarks

(A) Domestic 2.7

(B) Industrial

Process 1.73

Washing 0.4

Boiler 0.6

Cooling 0.5

Others Nil

Total Industrial

waste water

3.23

Total [A + B] 5.93

-

iv Treatment facility within premises with capacity

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

M/s. Lycos Chemtech proposes Effluent Treatment Plant (ETP) to be contained Primary and Tertiary Treatment Facilities. Treated effluent will be sent to Common MEE of M/s. Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwar for further treatment and disposal. Details of ETP are as follows. First all non-toxic and biodegradable streams of wastewater shall pass through Oil & Grease Trap (OGT-01) where floating oil, grease and other floating material shall be manually removed from top and collected in O & G Collection Tank(OGCT-01). Thereafter effluent shall be collected in Equalization cum Neutralization Tank (ENT-01) where the continuous addition and stirring of Lime solution is done to maintain neutral pH of wastewater from Lime Dosing Tank (LDT-01) as per requirement by gravity. Pipe grid will be provided at bottom of the ENT-01 to keep all suspended solids in suspension and to provide proper mixing by air supplied through air blowers (B-01). Thereafter, neutralized wastewater shall be pumped to Flash Mixer (FM-01). Alum and Polyelectrolyte shall be dosed from Alum Dosing Tank (ADT-01) and Polyelectrolyte Dosing Tank (PEDT-1) respectively by gravity into FM-01 to carry out coagulation by using a Flash

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Mixer. Thereafter, coagulated wastewater shall be settled in Primary Settling tank (PST-01). Clear supernatant from PST-01 shall be collected in Intermediate Sump(IS-01). Treated effluent from IS-01 then passed through Dual Media Filter (DMF-01) to remove remaining SS from effluent. Then clear water shall be collected in treated effluent Sump (TES-01) before sent toCommon MEE of M/s. Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwarfor further treatment and disposal. Sludge settled in PST-01 shall be sent to Sludge Drying Beds (SDBs-A/B) where, dewatering shall be carried out before storage in HWSA and ultimate disposal to TSDF. Leachate from SDBs-A/B shall be pumped back to ENT-01 for further treatment.

v Mode of Disposal & Final meeting point

Domestic:

2.7 KL/Day domestic wastewater will be disposed through Septic Tank/Soak

Pit.

Industrial:

3.23 KL/Day Industrial waste water will be sent to Common MEE of M/s.

Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwar for

further treatment and disposal after treatment in ETP within premises.

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

Name of CF

CMEE membership of M/s. ACPTCL, Ankleshwar

Membership of Common facility (CF)

(For waste water treatment)

Unit has obtained membership of CMEE membership of M/s. ACPTCL, Ankleshwar dated

22/01/2018 vide letter no. ACPTCL/1300000169/2017-18/138

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

Total Water Requirement

17.76

Process

2.86

Boiler

6.0

Cooling

5.0

Gardeni

ng

0.8

Domestic

2.7

Domestic

wastewate

r: 2.7�

Septic

Tank/Soak

ProcessW/W

1.73

Boiler

W/W

Cooling

W/W

0.5

ETP

(Primary Treatment)

Common MEE of M/s. ACPTCL, Ankleshwar

(For further Treatment & Final Disposal)

3.23

Washing

0.4

Washing

W/W

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viii Reuse/Recycle details (KLD)

Total reuse 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

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions i.e.

Air Pollutants

Air Pollution

Control Measures

(APCM)

1 Boiler-I (1 TPH)

12 Agro Wast

e

1250 Kg/Day

SPM SO2 NOx

Multicyclone Separator with bag

filter

2 Thermic Fluid

Heater (1 Lac KL/hr.)

12 Agro Wast

e

500 Kg/Day

SPM SO2 NOx

3 D.G. Set* (125 KVA)

5

Diesel

25 Liter/hr.

SPM SO2 NOx

Adequate stack height

--* To be used in emergency only.

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

- No process gas emissions from the proposed project.

iii Fugitive emission details with its mitigation measures.

As below:

Following measures will be adopted to prevent and control fugitive emissions?

1. Airborne dust at all transfers operations/ points will be controlled either by spraying

water or providing enclosures.

2. Raw materials loading and unloading will be done in covered area

3. Care will be taken to store construction material properly to prevent fugitive

emissions, if any.

4. Regular maintenance of valves, pumps, flanges, joints and other equipment will be

done to prevent leakages and thus minimizing the fugitive emissions of VOCs.

5. Entire process will be carried out in the closed reactors with proper maintenance of

pressure and temperature.

6. Periodic monitoring of work area will be carried out to check the fugitive emission.

7. Breather valves will be provided on solvent tanks.

8. To eliminate chances of leakages from glands of pumps, mechanical seal will be

provided at all solvent pumps.

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9. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank

vents will be connected to vent chillers.

10. Minimum number of flanges, joints and valves in pipelines.

11. Enclosures to chemical storage area, collection of emission from loading of raw

materials in particular solvents through hoods and ducts by induced draft, and

control by scrubber / dust collector to be ensured.

12. Adequate ventilation will be provided.

13. Periodic monitoring of work area will be carried out to check the fugitive emission

as per the norms of Gujarat Factory Rules.

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.

Quantit

y

(MT/An

num)

Management of HW

1 ETP Sludge ETP Sch-I/ 35.3

48

Collection, Storage, Transportation and sent to common TSDF site of M/s. BEIL, Ankleshwar for disposal.

2 Process Waste

Process (5-

Methyl Nicotinic

Acid)

Sch-I/ 28.1

60

Collection, Storage, Transportation and sent to common TSDF siteof M/s. BEIL, Ankleshwar for disposal.

3 Used Oil Equipment and

Machinery

Sch-I/ 5.1

3.6

Collection, Storage, Transportation and sell to GPCB registered reprocessor/refiner

4 Discarded Drums/ Bags

Raw Material &

Storage

Sch-I/ 33.1

2.7

Collection, Storage, Decontamination, Transportation & given to GPCB authorized Vendor

5 Distillation Residue

Distillation Unit Sch-I/ 20.3

32.4

Collection, Storage, Transportation and sent for co-processing in cement industries or to CHWIFof M/s. BEIL, Ankleshwar.

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6 Manganese

Dioxide

Process (5-

Methyl Nicotinic

Acid)

Sch-I/ 28.1

11

Collection, Storage and sell to end user/s having permission under rule-9.

7 Ammonium

Chloride Process(Ciproflo

xacin Base)

Sch-I/ 28.1

9

8 Zinc

Hydroxide

Process (1-Amino-4-

Methyl Piperazine)

Sch-II/ B-32

550

9 N-Methyl

Piperazine

Process (1-Amino-4-

Methyl Piperazine)

Sch-I/ 28.1

28

10 Sodium Chloride solution

Process (1-(2-Methoxyphenyl) Piperazine HCl

(98%))

Sch-I/ 28.1

600

Collection, Storage, and sent to ETP.

11 Spent Solvent Process Sch-I/ 28.6

600 Collection, Storage, Distillation and Reuse within premises.

-

ii Membership details of TSDF, CHWIF etc.

(For HW management)

Company has membership of TSDF of

M/s. BEIL dated 11/02/2017.

iii Details of Non-Hazardous waste & its disposal

(MSW and others)

No such waste will be generated.

G Solvent management, VOC emissions etc.

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

Name of Solvent

Boiling

Point (°C)

Vapor Pressure (kPa@20

0C)

Total Solvent

Input Kg

Qty of Solvent

Recycled Kg

Qty of Losses

Kg

% Recove

ry

% Los

s

Toluene 110.6 3.8 kPa @ 250C

10500 9950 550 94.76 5.24

o-Xylene 144.4 0.9 10000 9600 400 96 4

Acetone 56.2 24 20000 18700 1300 93.5 6.5

IPA 82.5 4.4 5000 4750 250 95 5

Methanol 64.5 12.3 20000 18650 1350 93.25 6.75

Ethanol 78.5 5.7 10000 9700 300 97 3

ii VOC emission sources and its mitigation measures

During operation stage, leakage through valves/pumps, leakage and emission from open drum containing chemicals, open feeding, storage tanks, etc. will be major sources of fugitive emissions and VOCs. Excess use of solvent/s may also results fugitive emission from the process vessels.

• Solid raw material charging will be done through closed system.

• Entire process will be carried out in the closed reactors with proper maintenance of

pressure and temperature.

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• Emphasis will be given to solvent management/solvent loss prevention.

• Control by having proper scrubbing system.

• Condenser to trap VOC.

• Proper maintenance schedule will be adhered to avoid emissions through flange joints,

pump seals etc.

• Minimum number of flanges, joints and valves in pipelines.

• Proper gland packing will be maintained for pumps and valves and to the extent possible

pumps with mechanical seal.

• A regular preventive maintenance schedule will be in place to replace or rectify all

gaskets and joints etc. as a part of ISO systems to ensure no fugitive emissions take

place.

• Periodic monitoring of work area will be carried out to check the fugitive emission.

• Solvent tank vents will be connected to vent chillers.

• Adequate ventilation will be provided.

• Airborne dust at all transfers operations/ points will be controlled either by spraying water

or providing enclosures.

• Breather valves will be provided on solvent tanks.

• During the meeting dated 28/11/2018, technical presentation made by project proponent.

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

Observation:

• This proposal is for new synthetic organic chemical products.

• Total water consumption will be 17.76 KLD. Total wastewater generation will be 3.23 KLD. 3.23 KL/Day Industrial waste water will be sent to Common MEE of M/s. Ankleshwar Cleaner Process Technology Centre Limited, Ankleshwar for further treatment and disposal after primary and tertiary treatment in ETP within premises.

• Agrowastewill be used as fuel in boiler.

• Adequate APCM like MCS and Bag filter will be provided for proposed boiler.

• There shall be no process gas emission from process.

• 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 March to May, 2017. Ambient Air Quality monitoring was carried out

for PM10, PM2.5, SO2, NOx, NH3, CO and VOC etc at ten locations including the project site.

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

Level Concentration (GLC) has been computed using ISCST3 Model. The resultant

concentrations are within the NAAQS. The PM10values at all the locations in residential/rural

areas ranged between 72.54 – 95.94 µg/m3 respectively in pre-monsoon season. Similarly,

the values of PM2.5 varied in the range of 42.61 – 51.28 µg/m3. The PM10 and PM2.5

concentrations at all the AAQM locations were primarily caused by local phenomena including

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vehicular activities and natural dust getting air borne due to manmade activities and blowing

wind.. 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 waste water management, area adequacy, BAT, Baseline study,

green belt development, environmental policy, SOP for safety aspects etc.

• There is no waste water generation from the products at sr. no. 1, 2 & 3. Entire quantity of

waste water will be sent to M/s: ACPTCL, Ankleshwar.

• Committee suggested to plant local trees with broad leaf and good canopy for green belt

development.

• Compliance of the ToR was found satisfactory.

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

of Environmental Clearance.

2. SIA/GJ/IND2/19767/2017 M/s Greeva Plot No. C-1/5513-5514, Phase III, GIDC-Vatva, Taluka Ahmedabad, District Ahmedabad, Gujarat

Appraisal

Project / Activity No.: 5(f)

Project status: Expansion

• PP has submitted online application vide no. SIA/GJ/IND2/19767/2017for obtaining

Environmental Clearance.

• SEIAA has issued TOR to PP vide letter : SEIAA/GUJ/TOR/5(f)/876/2017 vide dated 28th

September, 2017

• Project proponent has submitted EIA Report prepared by Kadam Environmental

Consultants, Vadodara based on the TOR issued by MoEF& CC.

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

manufacturing plant as tabulated below:

Sr.

no. Name of the Products

CAS

no.

Quantity (MT/Month) End-use of

product Existing Proposed Total

1 Textile Auxiliary Chemical (Blending & Mixing)

- 2000 0 2000 Used in Textile processing

2

Textile Auxiliary Chemical (Synthesis)

Such as;

Washing off Agent, Soaping Agent, Binders, Sizing Agent, Alkali Buffer

Acid Buffer, Bleaching Agent, Loop

- 0 3000 3000 Used in Textile processing

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Accelerator, Peroxide Killer, Lubricant

Carrier, Defoamer, Scroping Agent, Yarn Lubricant, Sequestering Agent, Stain Remover, Wax emulsion, Dyefixer-1

Dyefixer-2, Cationic Softener, Mercerising Agent, Retarding Agent, Wetting Agent – 1, Wetting Agent – 2, Resin, Fatty Ester, Adhesive, Silicon Oil, Bleaching Agent (Powder)


Notification 2006.



Sr.

no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Cr.):

Existing: 1.5 Proposed: 3.10 Total: 4.6

B Total Plot area

( sq. meter)

Existing: 1737 Sq. m.

Proposed: 314 Sq. m.

Total: 2051 Sq. m.

Green belt area,/Tree Plantation area

( sq. meter)


Proposed: 84 Sq. m.

Total: 309 Sq. m.

C Employment generation Existing: 23

Proposed: 27

Total: 50

D Water

i

Source of Water Supply (GIDC Bore well,


Water is sourced from GIDC water

supply i.e. Vatva Industrial Estate

Infrastructure Development Limited

(SPV) of Vatva Industries Association.

Status of permission from the concern authority.

Permission of Vatva Industrial Estate

Infrastructure Development Limited

(SPV) OF Vatva Industrial Association

is given.

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Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1 1 2

(B) Gardening - - -

(C) Industrial

Process 28 40 68

Washing 21 -1 20

Boiler 15 11 26

Cooling 5 4 9

Others - - -

Industrial Total 69 54 123

Grand Total

(A+B+C) 70 55 125

1) Total water requirement for the project: 125 KLD

2) Quantity to be recycle: 0 KLD

3) Total fresh water requirement: 125 KLD


Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 0.5 0 0.5 to Soak pit

(B) Industrial

Process 0 0 0 CETP after primary,

secondary&tertiary

treatment

Washing 21 -1 20

Boiler 0.5 0.5 1

Cooling 0.5 0.5 1

Others - - -

Total Industrial

waste water

22 0 22

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

[In-house ETP (Primary, Secondary, Tertiary).

The industrial effluent is treated in ETP of capacity 75 KLD & treated water is going to

CETP for further treatment.

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Domestic: To Soak Pit

Industrial:

The industrial effluent is treated in ETP of capacity 75 KLD & treated water

is going to CETP for further treatment.

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

etc.

Name of Common facility:

We are discharging treated effluent to M/s. The Green Environment services Co.-Op. Society Ltd.

Phase-II, GIDC estate, Vatva, Ahmedabad for further treatment.


Membership Certificate of M/s. The Green Environment Services Co-op. Society Ltd. For

Effluent Treatment.

vii Reuse/Recycle details (KLD)

-

E Air


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

etc.

Existing & Proposed

-

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

Existing

1 Boiler (1

TPH) 12

Natural Gas from

Adani Pipeline

70 SCM/Hr.

Particulate Matter,

SO2, NOx N/A

Proposed

1 Boiler (2

TPH) 12

Natural Gas from

Adani Pipeline

140 SCM/Hr.

Particulate Matter,

SO2, NOx N/A

2 D.G Set

(250 kVA) 12 Diesel 40 Lit/Hr.

Particulate Matter,

SO2, NOx N/A

-

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

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Existing & Proposed

There is no Process vent


There is no any kind of fugitive emission in present products as well as proposed products.

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

Existing Propose

d Total

1 ETP

Sludge ETP 35.3 60 MT - 60 MT

Packed in HDPE

Bags, and Dispose to

TSDF

2 Used Oil Machinery 5.1 - 0.1 KL 0.1 KL

Disposal by selling to register recycler

3 Discarded

Container/Liners

Production 33.1 120000

Nos./Annum

30000 Nos./Ann

um

150000 Nos./Ann

um

Disposal by selling to registered recycler

-


Membership Certificate of M/s.

SaurastraEnviro Projects Pvt. Ltd. For

Hazardous Waste.

iii Details of Non-Hazardous waste & its

disposal(MSW and others)

Not Applicable



List of solvents to be used:

Sr. No. Material description Storage Location Quantity in KL

1. Iso Amyl Alcohol Barrel 200

2 Acrylic Acid Barrel 200

3 Benzyl Chloride Barrel 200

4 Butyl Acrylate Barrel 180

5 Di Methyl Amine Barrel 170

6 Epichlorohydrin Barrel 230

7 Formaldehyde Barrel 230

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8 Formic Acid Barrel 35

9 Iso Propyl Alcohol Barrel 200

10 Styrene Barrel 200

11 Butyl Cello solve Barrel 200

12 Poly Vinyl Alcohol Bags 25 kg

• Solvent recovery system is not feasible as all solvents are going with products.


• -



• This proposal is for an expansion of synthetic organic chemical product and having CCA for

existing products.CCA compliance report submitted. PP informed that no public complaints

and Litigation against unit.

• Total water consumption will be 125 KLD. Total wastewater generation will be 22 KLD.

• The industrial effluent is treated in primary, secondary and tertiary ETP & treated water is

going to CETP of M/s GESCSL, Vatva for further treatment.

• Natural gas will be used as fuel for proposed boilers

• There is no process gas emission from process.





project site for the period October- 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 AERMOD.

• At various locations, average concentration of PM10 was observed to be varying from 127-

161µg/Nm3,which is more than the permissible limits for all locations.

• An average concentration of PM2.5 levels was observed to be in range of 41-50 µg/Nm3

which is withinthe permissible limits for all locations.

• An average concentration of SO2 and NOX is observed to be within the specified limit of

CPCB.

• 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).

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• It is further noted that ambient air quality for PM10 at all stations is not as per the NAAQ 2009

and PP could not satisfactorily addressed the compliance of NAAQ 2009 at these stations.

Committee asked PP to address the said reason in detail and also asked to conduct source

apportionment study to identify PM10 contributors.




• Committee deliberated on specific ToR regarding nearby habitation, CPCB directions to

CETP, Baseline data, project specific SOP & Safety measures, CER, EMP etc.

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

consideration only after satisfactory submission of the following:

1. Compliance of specific ToR no. 1 regarding provisions of barriers if any proposed towards

residential flats on back side and measures proposed for control of VOCs and noise to

ensure that nearby residents are not affected due to plant operation.

2. Action plan for waste water generation considering 18 (1) (b) directions under the Water Act

1974 imposed by CPCB on CETP. Compliance of the said directions keeping in view quantity

as well as quality of the effluent. Justification regarding how there is no increase in waste

water generation after proposed expansion.

3. Technical details as well as justification regarding higher values of PM10 and other

parameters in baseline study. Mitigation measures for the same shall be incorporated.

4. To address compliance status of NAAQ 2009 at all the AAQM stations detailed source

apportionment study to identify PM10 contributors.

5. Compliance of ToR no. 62 & 64 regarding project specific SOP & Safety measures

respectively.

6. Compliance of MoEFCC’s O.M. No. 22-65/2017-IA.III dated 01/05/2018 regarding Corporate

Environment Responsibility (CER). Fund allocation based on need based analysis for CER

shall be made as per the said OM dated 01/05/2018 for various activities therein.

7. Action plan for handling, storage and processing of Liq. Ammonia to avoid any fugitive

emissions and consequent complaints from the surrounding area.

3. SIA/GJ/IND2/25948/2017 M/s Krishna Chemtech

Plot No. 2213, G.I.D.C., Panoli, Tal: Ankleshwar,

Dist: Bharuch, Gujarat.

Appraisal


Project status: New

• PP has submitted online application vide no. SIA/GJ/IND2/25948/2017 dated 27/09/2018 for


• SEIAA has issued TOR to PP vide letter: IA-J-11011/332/2017-IA-II(I) vide dated :

17/08/2017.

of 76


Page 16 of 76

• Project proponent has submitted EIA Report prepared by Aqua-AirEnvironmental

Engineers Pvt.Ltdbased on the TOR issued by SEIAA.

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

tabulated below:

Sr. No

Proposed Products CAS No.

Production

Capacity

(MT/Month)

End Use Of All Products

1 1,4-di bromo Butane , 99% 110-52-1

50

Pharma Intermediate

2 1-(4-fluoro phenylepiperazine) , 99% 2252-63-3 Pharma

Intermediate

3 1-benzylepiperazine 2759-28-6 Pharma

Intermediate

4 N,N-Bis 2-chloro ethyle amine 821-48-7 Pharma

Intermediate

5 Cyclo propyl methyl ketone 765-43-5 Pharma

Intermediate

6 Chlorozoxanone 95-25-0 To treat mucular

Pain

7 Aceclofenac 89796-99-6 Anti-inflammatory

Drug

8 Fluconazole 86386-73-4 Antifungal Drug

9 Niclosamide 50-65-7 Anthelmintic Drug

10 1-(4- Methoxyphenyl)-1-(4-nitrophenyl) piperazine

74852-61-2 Pharma

Intermediate

11 1-(4-Methoxyphenyl) piperazine

38212-30-5 Pharma

Intermediate

12 6-Methyl pyridine-3 yl-2,4-Methylsulfonyl phenyl Etanone (Ketosulfone)

221615-75-4

Pharma Intermediate

13 4 Bromo methyl 2 Cyano biphenyl (Bromo OTBN)

114772-54-2 Pharma

Intermediate

Total 50


Notification 2006.



Sr.

no

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 2.0 Crores

(1) Capital cost for EMS (Environmental Management System): 0.371 Crores

(2) Recurring cost towards the environmental protection measures: 0.99 Crores per

Annum.

of 76


Page 17 of 76

B Total Plot area ( sq. meter) 1500 Sq. m.

Green belt area,/Tree Plantation area ( sq. meter) 532 Sq. m.

C Employment generation 12 persons approx.

D Water

i

Source of Water Supply

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

GIDC, Ankleshwar

Status of permission from the concern authority. Yes, granted. GIDC Water Supply letter No/GIDC/DEE/PNL/1611 dated: 02/06/2017


Category

Water Consumption KLD

(A) Domestic 1.0

(B) Gardening 1.0

(C) Industrial

Process 8.3

Washing 0.5

Boiler 3.5

Cooling 2.0

Scrubbing 0.5


Total (A + B + C) 16.8


2) Quantity to be recycle: 0 KLD



Category KLD Remarks

(A) Domestic 0.8

(B) Industrial

Process 9.0 Scrubbing media (0.8 KL/day) will be sold to authorized end user registered under Rule-9.

Washing 0.5

Boiler 0.2

Cooling 0.3

Scrubbing 0.8

Total Industrial waste water

10.8

-Worst case scenario for both water consumption & wastewater generation is based on

considering N,N-Bis 2-chloro ethyle amine



In-house ETP (Primary treatment): 10 KLD

of 76


Page 18 of 76


Domestic: Domestic: Domestic Waste water (0.8 KL/Day) will be disposed by septic tank or soak pit.

Industrial:

Industrial:

�Total 11.6KL/day (10.8KL/day Industrial + 0.8 KL/day domestic) of

effluent shall be generated. 10.0 KL/day will be given primary treatment

in ETP and then sent it to Common MEE of ACPTCL, Ankleshwar for

further treatment and disposal.

�Scrubbing media (0.8 KL/day) will be sold to authorised end user

registered under Rule-9.


Name of CF

Common MEE of M/s. ACPTCL, Ankleshwar


Common MEE of M/s. ACPTCL membership- Ref No: ACPTCL/1300000114/2017-18/78,

date of issue: 13/11/2017


vii Reuse/Recycle details (KLD) Not proposed.

Total reuse??.KLD

Source of waste water for reuse with quantity in KLD

Application area with quantity in KLD

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

E Air



-

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. Steam Boiler

(Capacity-1.5

MT/Hr)

30 m

Agro

Waste

4 MT/Day

PM ≤ 150 mg/Nm3

SO2 ≤ 100 ppm

NOX≤ 50 ppm

Multicyclone Separator, Bag

Filter

2. Thermic Fluid

Heater

(Capacity-2

Lakh Kcal/Hr)

30 m Agro

Waste

2 MT/Day Multicyclone

Separator, Bag Filter

3. D.G. Set

(Capacity-100

KVA) in

emergency

11 m HSD 5 LIT/hr


of 76


Page 19 of 76

only

-


-

Sr. no.

Specific Source of emission

(Name of the Product & Process)

Type of emission

Stack/Vent Height (meter)

Air Pollution Control Measures

(APCM)

1

Process Vent – 1 (N,N-Bis 2-chloro ethyle amine&Chlorination process)

SO2 -40 mg/Nm3 11 m Two Stage Alkali

Scrubber

2

Process Vent – 2 (4 Bromo methyl 2 cyano biphenyl &Bromination process)

HBr-30 mg/Nm3 11 m Two Stage Alkali

Scrubber

-


As below:

1. Airborne dust at all transfers operations/ points will be controlled either by spraying water or providing enclosures.

2. Care will be taken to store construction material properly to prevent fugitive emissions, if any.

3. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.

4. Entire process will be carried out in the closed reactors with proper maintenance of pressure and temperature.

5. Periodic monitoring of work area will be carried out to check the fugitive emission. 6. Breather valves will be provided on solvent tanks. 7. Solvent tank vents will be connected to vent chillers. 8. To eliminate chances of leakages from glands of pumps, mechanical seal will be

provided at all solvent pumps. 9. Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents

will be connected to vent chillers. 10. Minimum number of flanges, joints and valves in pipelines. 11. Enclosures to chemical storage area, collection of emission from loading of raw

materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.

12. Nitrogen blanketing will be provided, besides special care needs to be taken for control in respect of odorous chemicals, if any.

F Hazardous waste


Rules 2016.

i

-

Sr. no.

Type/Name of Hazardous waste

Source of generation

Category and Schedule asperHW Rules.

Quantity (MT/Annum)

Disposal Method

of 76


Page 20 of 76

1 Discarded Containers/

Bags/ Liners

Storage & handling of

Raw Materials

SchI/

33.1

2400 Nos/ye

ar

Collection,Storage,Transportation, reuse/ sale to authorize vendor.

2 Used oil

Equipment &

Machineries

SchI/

5.1

120

lit/year

Collection,Storage,Transportation, reuse/ sale to authorize vendor.

3

ETP Sludge ETP Sch-I/

35.3

60

MT/year

Collection,Storage,transportation and disposal common TSDF site (BEIL, Ankleshwar).

4

Distillation Residue

Distillation

Sch-I/

20.3

120

MT/yea

r

Collection,Storage,

Transportation and sent for co-processing in cement industries or Disposal at common incineration site

(BEIL, Ankleshwar).

5

Organic Waste

Mfg. Process of N,N-Bis 2-

chloro ethyle amine

Sch-I/

28.1

60

MT/year

6

Spent Carbon

Mfg. Process of

1-(4- Methoxyphe

nyl)-1-(4-nitrophenyl) piperazine

Sch-I/

28.3

15.6 MT/yea

r

7

Inorganic Salt

Mfg. Process of 1-

benzylepiperazine

Sch-I/

28.1

204

MT/year

Collection,Storage,transportation and disposal common TSDF site (BEIL, Ankleshwar).

8 Waste Cake

(KCl)

Mfg. Process of 1-(4

fluoroPhenylePiperazine)

Sch-I/

20.4

744

MT/ year

Collection,storage, transportation and sell to end user registered under Rule-9.

9 Sodium Bisulfite (20%) Scrubber

Sch-I/

28.1

108

MT/ year

Collection, storage, transportation and sell to end user registered under Rule-9.

10 Sodium Bromide sol. (25%)

Scrubber

Sch-II-

Class- B(5)

180

MT/ year

Collection,storage, transportation and sell to end user registered under Rule-9(Dwarkesh Chemical, Ahmedabad).

of 76


Page 21 of 76

11

Spent Solvent Mfg.

Process

Sch-I/

28.6

200

MT/ year

Collection,storage, transportation and sell to end user registered under Rule-9 (Omkar Chemicals, Panoli)or collection, Storage, management & recovery within the premises and will reuse in plant premises.


Membership of TSDF / Common Hazardous Waste Incineration Facility (CHWIF) that is M/s BEIL, Ankleshwar. Ref. No. BEIL/ANK/2018, dated: 05/02/2018


(MSW and others)

There is no generating any non-hazardous waste.


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

SOLVENT MANAGEMENT PLAN

• All the solvents shall be directly distilled from product mixes and; if required shall be

purified in packed column with the help of reflux.

• The solvent distillation system shall be designed so as to achieve minimum 95.0 %

recovery of solvent.

• Wherever required, the solvents shall be directly pumped into day tanks from the

storage tanks and shall be charged into the reactors without involving any manual

handling.

• All the pumps shall be mechanical seal type to avoid any leakage of solvent.

• All necessary fire fighting systems shall be provided with alarm system. Flame proof

wiring and flame proof electrical accessories shall be provided to avoid any mishap.

• All the storage tank and day tank shall be connected to a vent system through chilled

water condensers to prevent loss of solvents in the atmosphere.

• All the distillation column vents are also connected to cooling water/ chilled brine

condensers for maximum possible recovery of the solvents.

• All the vents will be connected to a common carbon Adsorber for removing traces of

solvent from vent gases.

• Residue generated from the distillation will be sent to BEIL incinerator site.

• Two condenser will install with cooling water and chilled brine to recover the solvent.

• Primary Condenser HE-01:Cooling Tower water or Chilled water (at 10 0C) will be used

to condense the solvents depend on the vapor pressure at its operating conditions and

the non condensed vapors will be condensed in a Secondary Condenser

• VOC Trap Condenser HE-02: Chilled Brine at -05 0C will be used to trap any traces of

Solvent which is slipped from Secondary condenser

SOLVENT RECOVERY PATTERN

Sr. No.

Name of Solvent

Total Solvent

Input (Kg)

Qty of Solvent

Recycled (Kg)

Qty of Losses

(Kg)

% Recovery

% Loss

of 76


Page 22 of 76

1. IPA 20 19.1 0.9 95.5 4.5

2. Toluene 800 760.2 39.8 95.03 4.97

3. DMF 101.5 98.1 3.4 96.6 3.4

4. Methanol 203.3 192.2 11.1 94.5 5.5

5. Acetone 205.7 200.2 5.5 97.3 2.7

6. MDC 3250 3240 10 99 1

7. Ethyl acetate 1240 1185 55 95.6 4.4


Volatile Organic Content Measures: To prevent losses of these solvents in atmosphere, following infrastructure shall be used in addition to LDAR program

• Leak Free Pumps for transfer of solvents • MSW Gaskets in solvent pipelines to prevent leakage from flanges • Minimum number of flanges, joints and valves in pipelines. • To eliminate chances of leakages from glands of pumps, mechanical seal will be

provided at all solvent pumps. • All the rotating equipments like pumps will be installed with Mechanical Seals to

arrest any sort of emissions. • Condenser and scrubber post Reactor with cooling arrangement • Enclosures to chemical storage area, collection of emission from loading of raw

materials in particular solvents through hoods and ducts by induced draft, and control by scrubber / dust collector to be ensured.

• In case the small spillage or leakage observed, first pour the china clay (vermiculate) on material and collect the contaminated china clay (vermiculate) and send to ETP.

• If the spillage is of inflammable liquid, switch off all the power supply in the area to prevent Electric Spark.

• Flanges will be sealed so less losses will be there. • Two condenser will install with cooling water and chilled brine to recover the solvent. • Primary Condenser HE-01: Cooling Tower water or Chilled water (at 50C) will be

used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser

• VOC Trap Condenser HE-02: Chilled Brine at -15 0C will be used to trap any traces of Solvent which is slipped from Secondary condenser



Observation:

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

• Total water consumption will be 16.8 KLD. Total wastewater generation will be 10.8 KLD.

• 10.0 KL/day will be given primary treatment in ETP and then sent it to Common MEE of

ACPTCL, Ankleshwar for further treatment and disposal.

• Scrubbing media (0.8 KL/day) will be sold to authorised end user registered under Rule-9.

• Agro waste will be used as fuel for proposed boiler and thermopack.

• Adequate APCM MCS and Bag filter will be provided with boiler and thermopack separately.

• Two stage alkali scrubber will be provided as APCM with each process reactor stack.


of 76


Page 23 of 76




project site for the period March 2017 to May 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 ISCST3. The

resultant concentrations are within the NAAQS. The Value of PM10 is higher in Panoli Region

due to location near GIDC Estate Area. For Kosamdi, the value of PM10 is higher due to

excess vehicle moment. Preventive measures to reduce the PM10 in Kosamdi village will be

covered in CER Activities. The ambient air quality around the proposed project site will remain

within the National Ambient Air Quality Standards (NAAQS).




• Committee deliberated on waste water management, area adequacy, BAT, Baseline study,

green belt development, environmental policy, SOP for safety aspects etc.

• Entire quantity of waste water will be sent to M/s: ACPTCL, Ankleshwar.

• Committee suggested to plant local trees with broad leaf and good canopy for green belt

development.

• Compliance of the ToR was found satisfactory.

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

of Environmental Clearance.

4. SIA/GJ/IND2/29128/2018 M/s. Shree Chemopharma Ankleshwar Pvt. Ltd. (Unit-3) Plot No. 313/10, 11, G.I.D.C. Estate, Ankleshwar, Dist.: Bharuch, Gujarat – 393 002

Screening and scoping


Project status: New

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

SIA/GJ/IND2/29128/2018dated 05/10/2018regarding 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 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

of 76


Page 24 of 76

GROUP 1

1. PARA CHLORO BENZOIC

ACID

74-11-3 100 Used in manufacturing of bulk

drug – Mebendazole.

2. ORTHO CHLORO

BENZOIC ACID

118-91-2 Used in manufacturing of bulk

drug – Mefenamic Acid and

Mesalamine.

3. META CHLORO BENZOIC

ACID

535-80-8 Active Pharmaceutical

Intermediate.

4. PARA NITRO BENZOIC

ACID


drug – Folic Acid. Also used in

Manufacturing of high

performance pigments.

5. META NITRO BENZOIC

ACID


Intermediate.

6. 2,3 DI CHLORO BENZOIC

ACID


drug – Lamotrigine.


ACID


drug – Lasamide.


ACID


Intermediate.


ACID


Intermediate.


ACID


Intermediate.


ACID


Intermediate.

12. ORTHO TOLUIC ACID 118-90-1 Application in manufacturing

high performance pigments.

13. DI NITRO TOLUIC ACID 28169-46-2 Application in manufacturing


14. 4 CHLORO 3 NITRO

BENZOIC ACID


drug – Mebendazole.


BENZOIC ACID


Intermediate.


BENZOIC ACID


drug – Mesalamine.

17. 2 HYDROXY 5 NITRO

BENZOIC ACID

(5 NITRO SALICYLIC ACID)


drug – Mesalamine.

18. PARA AMINO BENZOIC

ACID


drug – Benzocaine. Also used in

manufacturing of high

performance pigments.

19. 3 AMINO 4 CHLORO

BENZOIC ACID

2840-28-0 Application in manufacturing


20. 3 AMINO BENZOIC ACID 99-05-8 Application in manufacturing


of 76


Page 25 of 76

21. 3,5 DIAMINO BENZOIC

ACID



22. 4 NITRO BENZAMIDE 619-80-7 Application in manufacturing


23. 4 AMINO BENZAMIDE 2835-68-9 Application in manufacturing


24. 3 NITRO BENZAMIDE 645-09-0 Application in manufacturing


25. 3 AMINO BENZAMIDE 3544-24-9 Application in manufacturing



BENZAMIDE



27. 3 AMINO 4 CHLORO

BENZAMIDE



28. META PHENOXY BENZYL

ALCOHOL


Intermediate.

GROUP 2

29. MEFENAMIC ACID 61-68-7 30 Active Pharmaceutical

Intermediate.

30. MESELAMINE 89-57-6 Active Pharmaceutical

Intermediate.

31. LAMOTRIGINE 84057-84-1 Active Pharmaceutical

Intermediate.

32. FOLIC ACID 59-30-3 Active Pharmaceutical

Intermediate.

33. MEBENDAZOLE 31431-39-7 Active Pharmaceutical

Intermediate.


BENZOPHENONE


Intermediate.

35. 4 AMINO 3 NITRO

BENZOPHENONE


Intermediate.

36. 3,4 DIAMINO

BENZOPHENONE


Intermediate.

37. LASAMIDE 2736-23-4 Active Pharmaceutical

Intermediate.

38. FUROSEMIDE 54-31-9 Active Pharmaceutical

Intermediate.

39. BENZOCAINE 94-09-7 Active Pharmaceutical

Intermediate.

40. DABIGATRAN 211915-06-9 Active Pharmaceutical

Intermediate.

41. ALBENDAZOLE 54965-21-8 Active Pharmaceutical

Intermediate.

42. 4 THIOCYNO 2 NITRO

ANILINE


Intermediate.

TOTAL 130

of 76


Page 26 of 76


• The project proponent along with their expert /consultant Aqua-Air Environmental

Engineers Pvt. Ltd., Surat attended the meeting and made presentation before the

committee.

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

• The project falls under Category B of project activity5(f) as per the schedule of EIA Notification

2006


Sr.

no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 2.0 Crores

B Total Plot area( sq. meter) 1408 Sq. m.

Green belt area ( sq. meter) 444 Sq. m.

C Employment generation 20

D Water

i

Source of Water Supply(GIDC Bore well, Surface

water, Tanker supply etc...)

GIDC Water Supply

Status of permission from the concern authority. Permission will be taken after

getting NOC from GPCB


Category

Quantity

KLD

Remarks

(A) Domestic 4.0

(B) Gardening 2.0

(C) Industrial

Process 33.5

Washing 1.0

Boiler 12.0

Cooling 3.0

Others


Total (A + B + C) 55.5


2) Quantity to be recycled: 0.0 KLD


of 76


Page 27 of 76


Category Waste water

KLD

Remarks

(A) Domestic 3.7

(B) Industrial

Process 24.0

Washing 1.0

Boiler 2.0

Cooling 0.3

Others 0.0

Total Industrial

waste water

27.3

Total [A + B] 31.0

-



In-house ETP consisting of Primary Treatment facility @ 27.3 KL/Day


Domestic: Domestic waste water (3.7 KL/Day) will be sent to Septic Tank & Soak Pit.

Industrial:

Treated industrial effluent (27.3 KL/Day) will be sent to Common MEE, M/s.

BEIL, Ankleshwar after primary treatment for further treatment and disposal.


Name of CF

Common MEE Facility of M/s. ACPTCL, Ankleshwar



REF No. : BEIL/ANK/2018 for Common MEE of M/s. BEIL, Ankleshwar

vii Simplified water balance diagram with reuse / recycle of waste water All figures are in KL/ Day.

of 76


Page 28 of 76

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.)

No Reuse/Recycle

E Air


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

etc.

-

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1. Boiler (1 TPH)

18 Natural

Gas or

500

M3/day or

SPM SO2 NOx

Multi cyclone + bag filter

Domesti

c

Process

33.5

Water

Consumption

3.7

Boiler

12

Wastewater to

ETP

24

Washing

1

1

Septic

Tank/

Gardeni

ng

2

Common MEE of M/s. BEIL,

Ankleshwar for further

Cooling

3

0.3

of 76


Page 29 of 76

Briquettes 3 MT / day

2. Thermic Fluid Heater (2 Lac

Kcal/ Hr) 18

Natural

Gas or

Briquettes

200

M3/day or

1 MT / day

SPM SO2 NOx


3. Thermic Fluid Heater (2 Lac

Kcal/ Hr) 18

Natural

Gas or

Briquettes

200

M3/day or

1 MT / day

SPM SO2 NOx


4. D.G. set (125 KVA)

12 Diesel 10 Liter/ hr SPM SO2 NOx

Adequate Stack Height

-


-

Sr.

no.

Specific Source of

emission

(Name of the

Product & Process)

Type of

emission

Stack/Vent

Height

(meter)


Measures

(APCM)

1

Process Vent- 1* (Product Name:

Ortho Chloro Benzoic Acid)

NOx 11 4 Stage caustic scrubbers in series

2

Process Vent- 2** (Product Name: 4

chloro 3 nitro benzophenone)

SO2 11

2 stage scrubbers in series. 1st column having water and 2nd column having caustic solution.

3 Process Vent- 3***

(Product Name: Mebendazole)

NH3 11

2 stage scrubbers in series having chilled water

* Stack attached to Oxidation & Nitration reactor ** Stack attached to Thionyl Chloride Reaction *** Stack attached to Reaction generating Ammonia


As below:

• Enclosed Processed

• Minimum joints/flanges

• Auto handling for charging Raw Materials

• Pumps with double mechanical seals

• Proper Ventilation

• PPEs

F Hazardous wastes


of 76


Page 30 of 76

Rules 2016.

i

Sr.

no.

Type/Name

of Hazardous

waste

Source of

generation

Category

and

Schedule

as per HW

Rules.

Quantity

(MT/Annu

m)

Disposal Method

1 Used/Spent Oil

Equipment and machinery

Sch-I/ 5.1

120 Litres Collection, Storage, Transportation & sent GPCB approved recyclers/reused as lubricant.

2 ETP sludge

ETP Sch-I/ 35.3

600 MT Collection, Storage, Transportation and disposal at TSDF site of M/s BEIL, Ankleshwar.

3 Discarded Drums/ Bags

Raw material and storage

Sch-I/ 33.1

30 MT Collection, Storage, Transportation & sent back to supplier/ approved recycler.

4 Iron Sludge Process (3,5 Diamino

Benzoic Acid)

Sch-I/ 28.1

2000 MT Collection, Storage, Transportation and disposal at TSDF site of M/s BEIL, Ankleshwar.

5 Sodium Nitrite solution

Scrubber Sch-I/ 28.1

800 MT Collection, Storage & Sold to re-processors or end users having permission under Rule-9.

6 Aluminium Hydroxide Solution

Process (Mebendazol

e)

Sch-I/ 28.1

1800 MT

7 Sodium Bromide Solution

Process (Albendazole

)

Sch-II/ B-15

300 MT

8 Ammonium Chloride Solution

Process (Lasamide)

Sch-I/ 28.1

1600 MT

9 Sodium Sulphite Solution

Scrubber Sch-I/ 28.1

800 MT

10 Liq. Ammonia (20 – 25 %)

Scrubber Sch-II/ A-10

675 MT

11 Distillation Residue

Distillation Sch-I/ 36.1

144 MT Collection, Storage, Transportation & sent to cement industries for co-

of 76


Page 31 of 76

processing or common incineration facility of M/s BEIL, Ankleshwar.

12 Spent Catalyst

Process (Folic Acid)

Sch-I/ 28.2

18 MT Collection, Storage, Transportation and sent to registered regenerator

13 Spent Carbon

Process (Mebendazol

e)

Sch-I/

28.3

19 MT Collection, Storage, Transportation & co-processing in cement industries or Send to TSDF of M/s. M/s. BEIL, Ankleshwar

14 Spent Solvent

Process Sch-I/

28.6

3600 MT Collection, Storage, Re-process and Reuse within premises

15 HCl Process (Albendazole)

Sch-II/ B-15

320 MT Collection, Storage and sent to ETP for further treatment.

16 Sulphuric Acid (60%)

Process (Lasamide)

Sch-II/ B-15

2450 MT Collection, Storage & Sold to re-processors or end users having permission under Rule-9.

17 Recovered Nitric Acid

Process (Para Chloro Benzoic

Acid)

Sch-II/ B-15

1200 MT Collection, Storage and Reuse within premises (Reqd. Qty.:- 2400 MT)

-


(For HW management)

TSDF : BEIL- Ankleshwar


(MSW and others)

No such wastes generate.


• All the solvents shall be directly distilled from product mixes and; if required shall be

purified in packed column with the help of reflux and therefore there is no generation of

any distillation residue from the solvent distillation.

• The solvent distillation system shall be designed so as to achieve minimum 94.0 %

recovery of solvent.

• Pure solvent, crude solvent and distilled (recovered) solvent shall be stored only in

storage tanks and we shall not be using drums at any stage in the Solvent

Management System.

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Page 32 of 76

• Wherever required, the solvents shall be directly pumped into day tanks from the

storage tanks and shall be charged into the reactors without involving any manual

handling.

• All the pumps shall be mechanical seal type to avoid any leakage of solvent.

• All necessary fire fighting systems shall be provided with alarm system. Flame proof

wiring and flame proof electrical accessories shall be provided to avoid any mishap.

• All the storage tank and day tank shall be connected to a vent system through cooling

water and chilled brine condensers to prevent loss of solvents in the atmosphere.

• All the distillation column vents will be also connected to cooling water/chilled brine

condensers for maximum possible recovery of the solvents.

• All the vents will be connected to a common carbon Adsorber for removing traces of

solvent from vent gases.

• Residue generated from the distillation will be incinerated in-house or sent to BEIL

incinerator site.

• Coolant to be used

Primary Condensers Cooling Water

Secondary Condensers Chilled Brine up to -50C


LIST OF SOLVENTS ALONGWITH TOTAL RECOVERY

Name of Solvent Total Input (Kg)

Qty. of Recovered

Solvent (Kg)

Qty. of Losses

(Kg)

% Recovery

% Losses

Acetone 2521.5 2345.3 176.2 93.01 6.99

Benzene 960 912 48 95.00 5.00

Ethanol 175 159.5 15.5 91.14 8.86

Furfuryl Amine 1564 1410 154 90.15 9.85

Iso Propyl Alcohol 5920 5820 100 98.31 1.69

Methanol 15904 15674 230 98.55 1.45

n-Propoanol 1000 990 10 99 1.00

ODCB 10000 9750 250 97.5 2.5

Toluene 4594 4536.6 57.4 98.75 1.25


• Enclosed Processed

• Minimum joints/flanges

• Adequate Condenser

• Brine will be utilised as chilling agent

• Pumps with double mechanical seals

• Proper Ventilation

• PPEs


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Page 33 of 76

• This proposal is for a new synthetic organic chemical product. PP has proposed to achieve

ZLD by means of Treated industrial effluent (27.3 KL/Day) will be sent to Common MEE, M/s.

BEIL, Ankleshwar after primary treatment for further treatment and disposal..

• Natural gas or briquette will be used as fuel for boiler and thermic fluid heaters.

• MCS and Bag filter as APCM attached separately with boiler and TFH.

• Four stage alkali scrubber in series will be as APCM with each reactor stack.

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. Details with respect to justification for proposed expansion: (1) To address

proportionate availability of space for production plant. (2) To address proportionate

availability of storage area for raw materials, finished goods, utilities and goods carrier

movement within premises. (3) To address proportionate captive/common

infrastructure available to accommodate additional load due to proposed expansion.

(4) Environment impact and its mitigation measures for common/ captive infrastructure

due to proposed production.

3. 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.

4. Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent

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

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

5. Qualitative and quantitative analysis of hazardous waste streams generation from the

manufacturing process (Product wise). 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 shall be incorporated in EIA report.

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Page 34 of 76

6. 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 Chlorine gas, Hydrogen gas, Sulphuric acid,

various solvents etc.

7. Complete details regarding project specific safety aspects of Hydrogenation, Nitration

& Chlorination as per the prevailing norms.

8. Submit status of compliance of Environmental norms of M/s: BEIL, Ankleshwar

common MEE.

• 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.

5. SIA/GJ/IND2/29154/2018 M/s. MAKSONS FINE CHEM. PVT LTD

Plot No. 324, 325, 326 & 327, GIDC Industrial Estate, Ankleshwar – 393002, Dist – Bharuch, State: Gujarat.





SIA/GJ/IND2/29154/2018dated 05/10/2018 regarding grant of Terms of Reference [ToR] for



• This is an expansion unit proposes for Synthetic Organic Chemicals expansion in


Sr. no.

Name of the Products

CAS no. / CI no.

Quantity (MT/Month) End-use of the

products Existing Proposed Total

Group A

1. Ibefone (Phthalide) 87-41-2 3.00

12.00 12.00

Drug Intermediate,

API Industry

2. Bromasil

(Bromophthalide)

6940-49-4 1.00 Drug Intermediate,

API Industry

3. 1 – Bromo-4-Cyano

Acetophenone


API Industry

4. 2,6-Dichloro 24966-39-0 1.00 Drug Intermediate,

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Page 35 of 76

Thiophenol API Industry

5. 2-Phenyl

Thioethanol


API Industry

6. 3,4,5-Trimethoxy

Aniline


API Industry

7. 3,5-Dimethoxy

Aniline


API Industry

8. Diethyl Phenyl

Acetamide

2431-96-1 2.00 Pharma Drug, API

Industry

9. Pentoxyphyline 6493-05-6 1.00 Pharma Drug, API

Industry

10. Pyridyl Acetic Acid&

HCl

501-81-5

6419-36-9

2.00 Drug Intermediate,

API Industry

11. 1-(2 – Chloro-

(Chlorophenyl)-

Butyl)-Imidazole HCl

68055-81-2 -- Drug Intermediate,

API Industry

12. 1-Bromo,2,6-

Dimethoxybenzene

16932-45-9 Drug Intermediate,

API Industry

13. 1 – Bromo, 3,4, 5 -

Trimethoxy Benzene


API Industry

14. 2 – Amino-(2,5-

Dimethoxy Phenyl)-

Ethanone


API Industry

15. 2-

Carboxybenzaldehy

de


API Industry

16. 3,5-Dimethoxy

Bromo Benzene


API Industry

17. 3,5-Dimethyl Bromo

Benzene


API Industry

18. 3-Bromoaniline 591-19-5 Drug Intermediate,

API Industry

19. 3-Methoxyphenol 150-19-6 Drug Intermediate,

API Industry

20. 4-(Methylthio)-

Phenol


API Industry

21. 4-Acetylbenzoic Acid 586-89-0 Drug Intermediate,

API Industry

22. 4-Acetylbenzoic Acid

Methyl Ester


API Industry

23. 4-Chloro Phenoxy

Aniline


API Industry

24. 4-Nitrophenol MSA

Ester


API Industry

25. 4-Phenoxy Benzoic

Acid


API Industry

26. 6 – Bromo – 2- 5773-80-8 Drug Intermediate,

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Page 36 of 76

Naphoic Acid and

Ester

33626-98-1 API Industry

27. 6-Chloro Tetralone 26673-31-4 Drug Intermediate,

API Industry

28. Butoconazole and

Butoconazole Nitrate

64872-77-1 Pharma Drug, API

Industry

29. Methyl Sulfonyl

Acetic Acid


API Industry

30. Risedronic Acid and

Sodium Salt

105462-24-6

115436-72-1

Drug Intermediate,

API Industry

Group B

31. 2, 4 - Dimethyl

Thiophenol

13616-82-5 1.00

15.00 15.00

Drug Intermediate,

API Industry

32. 3-Methoxy

Thiophenol


API Industry

33. 4-Chlorophenoxy

Aniline


API Industry

34. 4-Cyano

Acetophenone


API Industry

35. Doxepinone 4504-87-4 2.00 Drug Intermediate,

API Industry

36. 1,3,5-Trimethoxy

Benzene


API Industry

37. 1-Benzyl Imidazole 4238-71-5 Drug Intermediate,

API Industry


Benzene


API Industry

39. 2-AcetylPyridine 1122-62-9 Drug Intermediate,

API Industry

40. 2-Phenyl

Thioethanol


API Industry

41. 3,5-Dimethoxy

Benzoic Acid Methyl

Ester

1132-21-4

2150-37-0

Drug Intermediate,

API Industry


Benzene


API Industry

43. 3-Amino Thioanisole 1783-81-9 Drug Intermediate,

API Industry

44. Doxepin HCl 1668-19-5 Pharma Drug, API

Industry

Group C

45. 2-Bromo Aniline 615-36-1 1.00

20.00 20.00

Drug Intermediate,

API Industry

46. 2-Iodo Aniline 615-43-0 1.00 Drug Intermediate,

API Industry

47. 1 – Bromo – 2- 583-55-1 -- Drug Intermediate,

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Page 37 of 76

Iodobenzene API Industry

48. 3-Acetylpyridine 350-03-8 Drug Intermediate,

API Industry

49. Pyridine – 2-

Aldehyde


API Industry

50. Pyridine – 4-

Aldehyde


API Industry

Group D

51. N,N-Diethyl

Cyanoacetamide

26391-06-0 1.00

25.00 25.00

Drug Intermediate,

API Industry

52. 2 – Bromo – 5-

Chlorotoluene


API Industry

53. 5 – Bromo – 2-

Chlorotoluene


API Industry

54. Ciprofloxacin Lactate 97867-33-9 Pharma Drug, API

Industry

55. Entacapone 130929-57-6 Pharma Drug, API

Industry

Group E

56. Bromoacetaldehyde

Dimethyl Acetal

7252-83-7 -- 25.00 25.00 Drug Intermediate,

API Industry

57. R & D Products -- -- 2.00 2.00 All Chemical

Industries

Total 3.00 99.00 99.00

Note:The unit will manufacture any of the above products as mentioned in group A to E in group wise in either / or basis as per mentioned quantity. But, total production capacity after expansion shall not exceed 99.00 MT/month.


Notification 2006.


• The project proponent along with their expert /consultant M/s. Earthcare Enviro Solution

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


Sr. no.

Particulars Details


(Rs. in Crores):

Existing: Rs. 6.50 Crore

Proposed: Rs. 12.00 Crore

Total: Rs. 18.50 Crore

B Total Plot area

( sq. meter)

Existing: 3615.00 Sq. m.

Proposed: 6920.55 Sq. m.

Total: 10,535.55 Sq. m.

Green belt area

( sq. meter)



Total: 3500.00 Sq. m.

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Page 38 of 76

C Employment generation Existing: 40 (Male-38, Female 02)

Proposed: 150 (Male-140, Female-10)

Total: 190 (Male-178, Female)

D Water

i

Source of Water Supply(GIDC Bore well,


GIDC, Ankleshwar


Unit will get permission from GIDC for

additional water requirement.

ii

Water consumption (KLD)

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1.00 7.10 8.10 --

(B) Gardening 2.00 12.00 14.00 --

(C) Industrial

Process 11.50 60.77 72.27 --

Washing 1.50 3.00 4.50 --

Boiler 2.00 100.00 102.00 --

Cooling 3.00 7.00 10.00 --

Others (Scrubber) -- 5.64 5.64 --

Industrial Total 18.00 176.41 194.41 --

Total (A+B+C) 21.00 195.51 216.51 --





Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1.00 5.68 6.68 --

(B) Industrial

Process 11.00 48.18 59.18 --

Washing 1.50 2.50 4.00 --

Boiler 0.30 5.00 5.30 --

Cooling 0.20 0.35 0.55 --

Others (scrubber) -- 5.64 5.64 --

Total Industrial

waste water 13.00 61.67 74.67 --



� Proposed in-house ETP (Capacity:80.00 m3/day) having PrimaryTreatment.

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Page 39 of 76

� MEE capacity: 5.0 KL/hr


Domestic:

Septic Tank / Soak Pit system.

Industrial:

After expansion, industrial effluent generated from manufacturing process and

other ancillary operation shall be allowed into in-house ETP for primary

treatment. Primary treated water (13.00 KLD) will be sent to CETP of M/s. ETL

for further treatment & final disposal as unit has already valid CTO for

wastewater disposal to CETP (M/s. ETL) and balance quantity (61.67 KLD) will

be sent to Stripper followed by MEE from where water will be concentrated to

recover mixed solvent, salt and condensed water will be reused for washing,

scrubber & process.

Note: At present, unit has planned to install in-house MEE for additional

wastewater. However, in future as & when function of CETP in this area

will improved / installed & if GPCB will grant permission to discharge

effluent into CETP, mode of disposal will be CETP after getting prior

permission.

vi

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

Name of Common facility

--


--



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Page 40 of 76


[Source of reuse & application area]

Total reuse: 56.15 KLD

Source of waste

water for reuse with

quantity in KLD


quantity in KLD

Remarks regarding feasibility to

reuse i.e. w/w characteristics

(COD, BOD, TDS etc.)

MEE recovered water

– 56.15 KLD

Process – 48.65 KLD Washing – 4.50 KLD Scrubber – 3.00 KLD

COD : 300 – 400 mg/l

BOD : 100 – 150 mg/l

TDS : 300 – 500 mg/l

E Air



Existing & Proposed

SR. No.

Source of emission

With Capacity

Stack

Height (meter)

Type of Fuel

Quantity of Fuel

MT/Day

Type of emissions

i.e. Air Pollutants


Measures

(APCM)

Existing

1

Steam Boiler

(Capacity: 600 kg/hr)

12.00 Natural

Gas 6.250

SCM/Hr

PM

SO2

NOX

Adequate stack height is

provided 2

Thermic Fuel Heater

(Capacity: 1 Lac Kcal/hr)

12.00 Natural

Gas 6.250

SCM/Hr

3 D. G. Set – 01 No. (Capacity: 90 KW)

5.0 HSD 23 Lit/hr

Proposed

4

Steam Boiler

(Capacity: 5 TPH)

12.00 Briquettes

of Bio Coal

600 kg/Hr

PM

SO2

NOX

Multi Cyclone Separator &

Water Scrubber

5

Thermic Fluid Heater

(Capacity: 3 Lac Kcal/hr)

12.00 Natural

Gas 18.75

SCM/Hr


will be provided

6

D. G Set – 02 Nos. (Stand By)(Capacity: 500 KW in single / multiple DG Sets)

5.00 HSD 135 Lit/hr


will be provided

-


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Page 41 of 76

Existing & Proposed

-

Sr. No.

Specific Sourceof emission(Name of

theProduct &Process)

Type of emission

Stack/Vent

Height (meter)


Measures(APCM)

Existing

1 Ammoniation NH3 12.0 Scrubber

2 Reaction Vessels-1 HBr 10.0 Alkali Scrubber

3 Reaction Vessels-2 HCl 10.0 Alkali Scrubber

Proposed

4 Reaction Vessel-1 HCl

SO2 10.0

Two stage

Alkali Scrubber 5 Reaction Vessel-2 H2S 10.0

6 Reaction Vessel-3 HBr 10.0

7 Reaction Vessel-4 NH3 10.0 Acid Scrubber

-


� 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.

Existing & Proposed

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

Existing Proposed Total

1 Process Residue and Wastes

Process

28.1 (Sch. I)

1.20 -- 1.20 Collection, Storage, Transportation & Disposal for incineration in common incinerator of BEIL, Ankleshwar

2 Spent Solvents

Process (many

products)

28.6 (Sch. I)

120.00 30.00 150.00 Collection, Storage, Reuse within

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Page 42 of 76

&Stripper premises OR Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste

3 Empty Barrels / Containers / Liners Contami-nated with Hazardous Chemicals / Wastes

Raw Materials &

finished Products packing material

33.1 (Sch. I)

3.00 87.00 90.00 Disposal by send it to authorized decontamination facility / recycler or reuse or send back to supplier

4 Chemical Sludge from Waste Water Treatment

Effluent Treatment

Plant

35.3 (Sch. I)

10.80 56.00 66.80 Collection, Storage, Transportation and Disposal by send it to TSDF – BEIL, Ankleshwar

5 Used or Spent Oil

D G Set &

Thermopack

5.1 (Sch. I)

0.04 0.16 0.20 Reuse in plant & machinery as lubricant OR sell it to authorized re-refiners / recycler

6 Sulphide (as H2S) (Sodium Sulphide / Sodium Hydrogen Sulphide) (55-60%)

Scrubber A13 (Sch. II)

33.76 3.68 37.44 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste

7 Oxides and Hydroxides except those of hydrogen, Carbon,

Process (Product No.

01)

B32 (Sch. II)

17.10 322.90 340.00 Collection, Storage, Transportation & Disposal by sell out to

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Page 43 of 76

Silicon, Iron, Aluminum, Titanium, Manganese, Magnesium, Calcium (Zn(OH)2) (90-95%)

authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste

8 Bromates (Hypo - Bromites) (Sodium Bromide) (90-95%)


45 & 56)

B6 (Sch. II)

30.00 3141.00 3171.00 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste

9 Ammonium Sulphate Solution (60-70%)

Scrubber 35.1 (Sch. I)

-- 15.00 15.00 Collection, Storage, Transportation & Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste

10 Sodium Sulphate (92-95%)

Process (Product No. 10, 29, 47)

28.4 (Sch. I)


11 Copper Solution (95-97%)

Process (Product No. 12, 13, 16,

28.4 (Sch. I)

-- 5820.74 5820.74 Collection, Storage, Transportation

of 76


Page 44 of 76

17, 27, 38, 42, 52, 53)

& Disposal by sell out to authorized users who is having authorization with valid CCA and rule 9 permission to receive this waste

12 Sodium Acetate Solution (92-95%)


52, 53)

28.4 (Sch. I)


13 Inorganic Salt

Scrubber 35.1 (Sch. I)

-- 3.00 3.00 Collection, Storage, Transportation and Disposal by send it to TSDF – BEIL, Ankleshwar

14 Spent Carbon

Process (Many

Products)

28.3 (Sch. I)

-- 98.40 98.40 Collection, Storage, Transportation & Disposal for co-processing

15 Spent Catalyst


49, 50)

28.2 (Sch. I)

-- 60.00 60.00 Reuse within premises OR Collection, Storage, Transportation and Sell to Registered Recyclers.

16 Iron Sludge Process (Product No.

43)

28.1 (Sch. I)

-- 322.20 322.20 Collection, Storage, Transportation & Disposal at TSDF site for secured landfill

17 Distillation residue

Process (Many

20.3 (Sch. I)

-- 88.32 88.32 Collection, Storage,

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Page 45 of 76

Products) Transportation and Disposal for co-processing

18 MEE salt MEE 35.3 (Sch. I)

-- 548.00 548.00 Collection, Storage, Transportation & Disposal at TSDF site for secured landfill

-


(For HW management)

Unit has got membership of M/s. BEIL for

landfilling and incinerable waste.



As below

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



In-house solvent recovery plant will be installed and recovered solvent will be again reused in

process and residue will be disposed for co-processing.


� 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


• This proposal is foran expansion of synthetic organic chemical product. Unit is having valid

CCA for existing products.

• Total water consumption will be 216.51 KLD. Total wastewater generation will be 74.67 KLD.

• Industrial effluent generated from manufacturing process and other ancillary operation will be

allowed into in-house ETP for primary treatment. Primary treated water (13.00 KLD) will be

sent to CETP of M/s. ETL for further treatment & final disposal as unit has already valid CTO

for wastewater disposal to CETP (M/s. ETL) and balance quantity (61.67 KLD) will be sent to

Stripper followed by MEE from where water will be concentrated to recover mixed solvent, salt

of 76


Page 46 of 76

and condensed water will be reused for washing, scrubber & process.

• 56.15 KLD MEE condensate will be reused back in process.

• Committee deliberated on waste water management, Compliance of CPCB directions to

CETP etc. Committee found that management of waste water is not convincing. Upon asking

about feasibility of treated waste water reuse, PP could not replied satisfactorily..

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

consideration only after satisfactory submission of the following:

1. Action plan for waste water generation considering 18 (1) (b) directions under the Water Act

1974 imposed by CPCB on CETP. Compliance of the said directions keeping in view quantity

as well as quality of the effluent.

2. Sound management of waste water keeping in view characteristics of waste water in worst

case scenario.

3. Feasibility report for reuse of waste water for industrial purpose.

6. SIA/GJ/IND2/21840/2018 M/s MayurDyechem Intermediates LLP. (Unit-I) Plot No. A1/108,91, A2/92 Phase-2, GIDC Estate, Vatva, Dist: Ahmedabad-382445.



Project status:Expansion


SIA/GJ/IND2/21840/2018dated 05/10/2018regarding grant of Terms of Reference [ToR] for



• This is an expansion unit proposes for Synthetic Organic Chemicals expansion in


Sr.

no.

Name of the

Products

CAS no. /

CI no.

Quantity

MT/Month

End-use of

the products

Existing

Proposed Total

1 Vinyl Sulphone

2494-89-5 150 75 225 In Reactive Dyes Manufacturing

2 H-Acid 5460-09-3 0 100 100

Total 150 175 325


Notification 2006.


of 76


Page 47 of 76

• The project proponent along with their expert /consultant Bhagwati Enviro Care Pvt. Ltd.

Ahmedabad attended the meeting and made presentation before the committee


Sr.

no

Particulars Details


(Rs. in Crores):

Existing: 7.84 Proposed: 10.98 Total: 18.82

B Total Plot area

( sq. meter) Existing –6375

(Plot No 91-1711 Plot No. 92-1887 Plot No. 108-2777) Proposed-0 Total: 6375 Sq. m

Green belt area

( sq. meter)

Existing: 1900 Sq. m. Proposed: 0 Sq. m. Total: 1900 Sq. m.

C Employment generation Existing:80 Proposed: 40 Total:120

D Water

i


(GIDC Bore well, Surface water, Tanker supply

etc...)

Bore well


Under Consideration (Please refer Annexure-IV)

ii

Water consumption (KLD)

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(D) Domestic 5 30 35

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Page 48 of 76

(E) Gardening

20 30 50

(F) Industrial

Process 122 112 234

Washing 24.3 22 46.3

Boiler 4.9 20 24.9

Cooling 23.2 20 43.2

Others 2.6 15 17.6

Industrial Total 177 189 366

Grand Total

(A+B+C)

202 249 451

4) Total water requirement for the project: 451 KLD

5) Quantity to be recycled:53 KLD


iii

Waste water generation (KLD)

Category Existin

g

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(C) Domestic

5 30 35

(D) Industrial

Dilute Stream- V.S. Concentrate Stream –V.S. Process Concentrate Stream –H-Acid

15 2.5 17.5

37 22.2 59.2

0 120 120

Washing 24.3 20 44.3

Boiler 0.2 7 7.2

Cooling 0.5 2 2.5

Total (Industrial) 77 173.7 250.7

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Page 49 of 76

Total Waste Water Generation

(M3/Day)

82 203.7 285.7


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

etc..

� Existing ETP: 150 KL/Day (Tertiary) Followed By spray dryer


Domestic:

To soak pit

Industrial:

- In the existing system dilute waste water stream of V.S. of 15 M3/Day is treated in our existing ETP and disposed to the CETP of The Green Environment Services Co operative Society Ltd.

- After expansion Dilute waste water stream of Vinyl Sulphone of 2.5 M3/Day will be disposed to CETP of The Green Environment Services Co operative Society Ltd. after the treatment in our existing ETP.

- In existing system concentrated waste water stream of Vinyl Sulphone of 37 M3/Day is treated in our own Spray Drying System and also disposing through the common MEE and Spray Drying System of The Green Environment Services Cooperative Society Ltd. & Chhatral Environment Management System Pvt. Ltd.

• After expansion Concentrated Waste Water stream of Vinyl Sulphone of 22.2 M3/Day and H-Acid of 120 M3/Day will be treated as per the existing treatment system of Vinyl Sulphone i.e. treated in our own Spray Drying System and will also be dispose through the common MEE and Spray Drying System of The Green Environment Services Cooperative Society Ltd. &Chhatral Environment Management System Pvt. Ltd.

• Concentrated waste water stream of H-Acid will be treated by our own MEE and Spray Drying system and will also be disposed through the common MEE and Spray Drying System of The Green Environment Services Cooperative Society Ltd. &Chhatral Environment Management System Pvt. Ltd And 53 m3/Day will be reuse in H-acid Manufacturing Process.

• Boiler and Cooling Blow Down Will be send to CETP.

• Washing effluent will be evaporate in in-House Spray Dryer.

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

CHWIF etc.


1. CETP, Vatva

2. Novel: Spent Acid, Vatva

3. Common Spray Dryer, Vatva

4. Common Spray Dryer Chhatral

5. CHWIF: Saurastra Enviro Projects Pvt. Ltd

6. TSDF: Eco Care Infrastructure Pvt. Ltd



CETP: Green Environment Services Co-Op. Society Ltd

Spray Dryer: Green Environment Services Co-Op. Society Ltd

Spray Dryer: Chhatral Enviro Management System Pvt. Ltd


Please Refer Annexure-V



Total reuse 53 KLD

Source of waste water

for reuse with

quantity in KLD

Application area

with quantity in

KLD

Remarks regarding


w/w characteristics (COD,

BOD, TDS etc.)

53 KLD from H-acid Used in H-Acid

Manufacturing

COD:

BOD:

TDS:

-

E Air


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

KVA etc.

Existing & Proposed

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-

Sr. no.

Source of emission

With Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 Boiler-1 (Existing) (400 Kg/Hr)

12 Natural

gas 12 m3/hr

Particulate matter SO2 NOX

Not required

due to the utilization of Natural

Gas as Fuel

2 Thermic Fluid Heater (Existing) (150000 Kcal/Hr)

12

Natural gas

12 m3/hr

3 Boiler -2 (1.5 MT/Hr) Boiler-3 (1.5 MT/Hr) (Proposed)

20 Natural gas

600 m3/hr

4 Hot Air Generator (HAG) (Existing) (300000 Kcal/Hr)

12 Natural gas

30 m3/hr

5 Incinerator-1 (For Vinyl Sulphone) (Existing) (1200 Lit/Hr)

30 Natural

gas 300

m3/hr

Particulate matter

SO2

HF Cl

NOX CO

Total Dioxin &

Furan

Water scrubber

followed by Alkali

Scrubber Twin

Cyclones, One Water scrubber

followed by Alkali

Scrubber

6 Spray Dryer (Existing) (3300 Lit/Hr)

30

Natural gas

300 m3/hr

7 DG Set 11

Diesel 10

Lit/Day

Particulate matter SO2 NOX

----

-


Existing & Proposed

-

Sr.

no.

Specific Source of

emission

(Name of the Product

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution

Control

Measures

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&Process) (APCM)

1 CHLOROSULPHONATOR (Acetanilide addition in Vinyl Sulphone)

HCl SO2 Cl2

20

Total four stage scrubbing system Includes Two stage Water Scrubber followed by two stage Alkali Scrubber

2 CHLOROSULPHONATOR (Thionyl Chloride addition in Vinyl Sulphone)

HCl SO2 Cl2

20

Four Stage Alkali Scrubber

3 NEUTRALIZER (H-Acid)

NOX

20

Total four stage scrubbing system includes One stage Water Scrubber followed by three stage Alkali Scrubber

4 ISOLATOR (H-Acid )

SO2 20

Total four stage scrubbing system includesTwo stage Water Scrubber followed by two stage Alkali Scrubber

-


Fugitive emission from the proposed project activities shall be mainly the VOCs emissions, which results from uses of solvents. - This emission will be taken place only at storage and handling of solvent. - Storage is in closed area with a facility of condenser which will reduce the emission.

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

Specific

Source of

generation

Category

and

Schedule

Quantity

(MT/Annum)

Management

of HW

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Page 53 of 76

waste (Name of

the

Activity,

Product

etc.)

as per

HW

Rules.


1 ETP Sludge Effluent Treatment Plant

35.3 12 MT/ Year

900 MT/ Year

912 MT/ Year

Collection, Storage, Transportation, Disposal at TSDF

2 Used Oil Plant Machinery

5.1 1.2 KL/ Year

1.8 KL/ year

3.0 KL/ year

Collection, Storage, Transportation , Disposed by selling to Registered reprocessers /recycler

3 Discarded Carboys/ Barrels/ Bags/Liner

Raw Material Section

33.1 0.60 MT/ Year

30 MT/ Year

30.60

MT/ Year

Collection, Storage, Decontamination, Transportation, Disposal by selling to authorized recycler

4 Gypsum Sludge

From H-Acid Manufacturing Process

26.1 7200 MT/Yea

r

1050 MT/Year

8250 MT/Year

Collection, Storage, Transportation, Sell to Cement Manufacturing Units

5 Process Iron Waste

From H-Acid Manufacturing Process

26.1 NIL 2750 MT/ Year

2750 MT/ Year

Collection, Storage, Transportation, Sell to Cement Manufacturing Units

6 Incinerated Ash

From Incinerator

37.2 720 MT/ Year

NIL 720 MT/ Year

Collection, Storage, Transportation, Disposal at TSDF

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7 Spent Sulphuric Acid

From Vinyl Sulphone Manufacturing Process

26.3 19200 MT/ Year

14400 MT/ Year

33600

MT/ Year

Collection, Storage, Reuse in V.S. and H-Acid Plant. Treatment in ETP

8 Spray Dried Solid

From Spray Dryer

37.2 Nil 5000 MT/ Year

5000 MT/ Year

Collection, Storage, Transportation, Reuse, Sell and Disposal at TSDF

9 Spent Hydrochloric Acid

From Scrubber

26.3 2140 MT/ Year

1630 MT/ Year

3770 MT/ Year

Collection, Storage, and sell to actual users. Treatment in ETP

10 NaHSO3 From Scrubber

26.3 Nil 297

MT/Year

297

MT/

Year

Collection,

Storage, and

sell to actual

users.

Treatment in

ETP

11 Acetic Acid From Vinyl Sulphone

26.3 Nil 3285

MT/Year

3285

MT/

Year

Collection,

Storage, and

sell to actual

users.

Treatment in

ETP

-


(For HW management)

1. CHWIF: Saurastra Enviro Projects Pvt.Ltd

2. TSDF: Eco Care Infrastructure Pvt. Ltd



Not be any Non Hazardous Waste Generate.

G

Solvent management, VOC emissions etc.

Name Of Product

Product Quantity

Batch Size in Kg

No. Of Batch/ Month

Solvent to be used

Quantity Used KL/Batch

Quantity Recovered In KL/Batch

Quantity Loss in KL/Batch

H-Acid 100 1500 67 Methanol 1125 1020 105

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

Solvents

� Recovery Of Methanol 91 % and it reuse in process.


� We will assure that measure VOC level in our Manufacturing unit as well as

Raw material storage area. We will also do work place monitoring &

according implementation.


• This proposal is for expansion of Dyes Intermediate Vinyl Sulphone and addition of H-Acid.

• While discussing about compliance of the GPCB Circular dated 03/11/2018 regarding specific

products within PCPIR region as well as outside PCPIR region, Project proponent as well as

environmental consultant could not reply satisfactorily.

• Committee found that ratio of V.S and H-acid mentioned in proposed product profile is not as

per the said circular published by GPCB.

In view of the above stated facts, Committee unanimously decided to consider the project for

further consideration only after submission of the following:

1. Compliance of all the conditions stipulated in GPCB circular dated

03/11/2018regarding specific products.

2. Revised proposal considering compliance of GPCB Circular dated 03/11/2018.

7. SIA/GJ/IND2/28777/2018 M/s. Pharmex Healthcare

Plot No. A1-6104/5, GIDC Notified Industrial Estate, Ankleshwar– 393 002, Dist. Bharuch, State- Gujarat, India





SIA/GJ/IND2/28777/2018dated 21/09/2018 regarding grant of Terms of Reference [ToR] for



• This is an existing unit engaged in manufacturing of Synthetic Organic Chemicals and now

proposes for expansion as tabulated below:

Sr. No.

Name of Products CAS No./ Cl no.

Quantity MT/Month

End Use

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1. Benzoturane 2- Hydroxy Dimethyl Methanol Sulfonate (BHDMS)

-- 30 -30 0 --

2. Hydrazide OR HS code: 28251020

45 -40 5 To cure Lower Blood

Pressure

Ganciclovir Intermediate (G.A.- 11) (Job Work)

-- 1.5 -1.5 0 --

3. 2,3 Dichloro 6 Nitro Aniline (DICONA)

65078-77-5

0 25 25 For the preparation of

Polymers

4. Nitro RF

(O, O, O-Tris (4 -

nitrophenyl) thiophosphate)

64131-85-7

0 5 5 For the preparation of

Amino RF

5. 2-Amino-4-chlorophenol 95-85-2 0 20 20 To manufacture

Chlorzoxazone

6. 4-Amino-2-chlorophenol 3964-52-1

Used for manufacturing 3-Chloro-4-

[(pyridin-2-yl)methyloxy]

aniline

7. 2, 4, 5-Trichloro Aniline 636-30-6 To manufacture

Pigment- Red 112

8. 1,8 Diamino Naphthalene 479-27-6 Used as Pigment

intermediate

9. Para Chloro Aniline Hydrochloride

20265-96-7

0 20 20 Chlor Hexidine

Base

10. 1,5 Dinitro Naphthalene 605-71-0 0 30 30 To manufacture 1,5 Diamino Naphthalene

11. 1,8 Dinitro Naphthalene 602-38-0 To manufacture 1,8 Diamino Naphthalene

TOTAL 75 (Max.) 105

NOTE:

• Total production capacity after proposed EC expansion shall be 105 MT/Month.

• Either individual or total production of products in Sr. No. 5 to 8 shall not exceed 20 MT/Month after proposed expansion.

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

tabulated below:


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Page 57 of 76

• The project proponent along with their expert /consultant Siddhi Green Excellence Pvt. Ltd

attended the meeting and made presentation before the committee.

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

Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: 0.8821 Crore

Proposed: 4.499 Crores

Total: 5.3811 Crores

B Total Plot area

( sq. meter)


Proposed: NIL

Total: 3182 Sq. m.

Green belt area

( sq. meter)


(~8.5%)


(~3.5%)

Total: 382.02 Sq. m. (~12%)

Balance greenbelt shall be

developed in the area

specified by GIDC.

C Employment generation Existing: 14 Nos. Company

employees + 6 Nos. on

Contract basis

Proposed: 20 Nos. Company

employees + 6 Nos. on

Contract basis

Total: 34 Nos. Company

employees +12 Nos. on

Contract basis

Locally employed manpower

shall be utilized.

D Water

i


(GIDC Bore well, Surface water, Tanker supply

etc...)

GIDC


Existing Quantity:

Industrial: 7.5 KLD +

Domestic: 0.5 KLD +

Gardening: 0.5 KLD


Existing KLD

Proposed

KLD

Total after

Expansion

KLD

Remarks Water Consumpti

on*

Water Consumption after

continuing one of the

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Page 58 of 76

existing product*

(G) Domestic 0.5 0 2 2 --

(H) Gardening 0.5 0 1 1 --

(I) Industrial

Process 1 0 8 8

Total fresh water requirement for Proposed Production is 8 KLD.

Washing 1.5 0 NIL NIL

Boiler blowdown of 0.9 KLD & Cooling tower blowdown of 2 KLD shall be reused for Washing purpose. So fresh water requirement for Washing shall be NIL.

Boiler 3 0.2 2.8 3 --

Cooling 2 0.1 6.9 7 --

Others (APCM)

0 0 2 2

Total fresh water requirement for Proposed APCM is 2 KLD.

Industrial Total

7.5 0.3 20 20

Grand Total (A+B+C)

8.5 0.3 23 23

*Production quantity of one of the existing products (i.eHydrazide) shall be reduced from 45 MTM to 5 MTM and rest of the existing products shall be discontinued after proposed expansion.





Cat

Existing KLD

Proposed

Total after

Remarks

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Page 59 of 76

egory

Waste

Water

Generation*

Waste Water

Generationafter

continuing one of

the existing product*

KLD Expansion KLD

(E) Domestic

0.5 0 1.5 1.5

Sewage shall be disposed to soak pit via septic tank.

(F) Industrial

Process

1.2 0 10 10

Low COD effluent stream (4 KLD) & High COD effluent stream (6 KLD) shall be treated separately in ETP. Primary treated effluent shall be sent to CMEE (Common Multi-Effect Evaporator) of M/s. ACPTCL (Ankleshwar Cleaner Process Technology Centre Private Limited), Ankleshwar.

Washing 1.6 0 2.9 2.9

Primary treated effluent shall be sent to CETP (Common Effluent Treatment Plant) of M/s. ETL (Enviro Technology Limited), Ankleshwar after conforming to their inlet norms through tankers for final disposal.

Boiler 0.1 0 Note 1 Note 1

Note 1: Boiler blow down of 0.9 KLD shall be reused for washing purpose and then shall be given Primary treatment in ETP (Effluent Treatment Plant).

Cooling 0 0 Note 2 Note 2

Note 2: Cooling tower blow down of 2 KLD shall be reused for washing purpose and then shall be given Primary treatment in ETP.

Others -- -- -- -- --

Total Industria

l waste water

2.9 0 12.9 12.9


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Presently, unit is a member of CETP of M/s. ETL, Ankleshwar for 2.9 KLD effluent disposal. Existing CETP load includes both Process & washing effluent. Existing COD load on CETP is between 5000 - 8500 mg/L. After proposed expansion, CETP hydraulic load will include only washing effluent. Therefore, COD load will be 1200 - 1500 mg/L. Because of proposed expansion, Pollution load on CETP will reduce.



For existing & Proposed expansion:

� ETP Capacity = 15 KLD (Consisting of Primary Treatment)


Domestic: Sewage shall be disposed to soak pit via septic tank.

Industrial: Process effluent: Primary treated process effluent shall be sent to CMEE of M/s. ACPTCL (Ankleshwar Cleaner Process Technology Centre Private Limited), Ankleshwar. Washing effluent: Primary treated washing effluent shall be sent to

CETP (Common Effluent Treatment Plant) of M/s. ETL (Enviro

Technology Limited), Ankleshwar after conforming to their inlet

norms through tankers for final disposal.

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

CHWIF etc.


� Name of Common facility:

1. CETP of M/s. ETL (Enviro Technology Limited), Ankleshwar

2. CMEE plant of M/s. ACPTCL (Ankleshwar Cleaner Process Technology Centre

Private Limited), Ankleshwar



Unit is member of CETP of M/s. ETL, Ankleshwar.

And for CMEE plant of M/s. ACPTCL, the unit is under process of obtaining

membership.


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Page 61 of 76



Total reuse: 3 KLD

Source of waste water

for reuse with quantity

in KLD


quantity in KLD

Remarks regarding


w/w characteristics

(COD, BOD, TDS etc.)

Boiler blowdown: 0.9

KLD &

Cooling tower blowdown:

2 KLD

Boiler blowdown of 0.9

KLD & Cooling tower

blowdown of 2 KLD shall

be reused for Washing

purpose.

COD: <100

BOD: <30

TDS: <500

E Air


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

KVA etc.

Existing & Proposed

Sr. no.

Source of emission

With Capacity


Type of

Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

Existing

1 Boiler: 600 Kg/hr

11 Natural gas

200 m3/ day

PM

SO2

NOX

Adequate stack height is provided

Proposed

2

Thermic Fluid

Heater: 2 Lakh

Kcal/hr

11 Natural gas

800 m3/ day

PM

SO2

NOX


shall be provided

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Page 62 of 76

3

D.G. set (standby): 250 KVA

11 Diese

l 40 L/h


shall be provided


Existing & Proposed

Sr. no.

Specific Source of emission

(Name of the Product & Process)

Type of emission

Stack/Vent Height (meter)

Air Pollution Control Measures

(APCM)

Existing

There is no process emission from the existing manufacturing process.

Proposed

1

From Two stage water scrubber attached to Reaction vessel of 2,3 Dichloro 6 Nitro Aniline (DICONA)

NH3 15 Two stage Water

Scrubber

Final solution obtained from scrubber and their disposal:

18 – 20 % Ammonia solution generated from scrubbing of NH3 emission emitted from

the production of 2, 3 Dichloro 6 Nitro Aniline (DICONA)shall be sold to authorized

actual end users.


� Fugitive emission shall remain within permissible limit as handling of chemicals

will be in closed system.

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

Specific Source of generation (Name of

the Activity, Product

etc.)

Category and

Schedule as per HW

Rules.

Quantity (MT/Annum)

Management of HW Exis

ting*

Haz. waste

qty after continuing one of the

existing product

s*

Proposed

Total

1 Used Oil

From Machinery

Category: 5.1 &

Sch: I

0.3 KL

0 1.8 KL

1.8 KL

Collection, Storage,

Transportation, Reuse & Disposal by

reusing within plant

and or selling it to

authorized

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Page 63 of 76

agency.

2

Discarded Containers/ Bags and Liners

From Raw material

containers / bags

Category: 33.1

& Sch: I

5.7 MT

(380 nos.) 0.06 MT

(300 nos.)

0

36 MT

(2400 nos.)

12 MT

(60000

nos.)

36 MT

(2400

nos.) 12 MT

(60000

nos.)


Transportation, Reuse,

Decontamination &

Disposal by reuse or selling to

registered re-processor.

3 Tarry Waste

During Production

of: Distillation process of Hydrzide;

2,3 Dichloro 6

Nitro Aniline

(DICONA); Nitro RF (O,O,O-Tris (4 -

nitrophenyl)

thiophosphate); 2, 4,

5-Trichloro Aniline; 1,8

Diamino Naphthalen

e; 1,5 Dinitro

Naphthalene & 1,8 Dinitro

Naphthalene

Category: 36.1

& Sch: I

3.6 0.3 87 87.3


Transportation &Disposal to CHWIF/

Co-processing at

M/s. BEIL, Ankleshwar.

4

Chemical sludge from waste water treatment

From ETP

Category: 35.3

& Sch: I

NIL NIL 60 60


Transportation&Disposal to common

TSDF facility at M/s. BEIL, Ankleshwar.

5 Spent Filter cloth

Filtration Process

Category: 36.2

NIL NIL 3 3 Collection, Stored in Bags in

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Page 64 of 76

& Sch: I

separate place (shed with RCC flooring),

Transportation & sent to CHWIF of M/s. BEIL,

Ankleshwar

6

Off- spec product / raw material OR failed batch

--

Category: 28.4

& Sch: I

NIL NIL 6 6

Collection, Stored in

drums / bags in separate place (shed with RCC flooring),

Transportation and sent

for co-processing

OR to CHWIF of M/s. BEIL,

Ankleshwar.

7

Iron oxide sludge

During Production

of: Through

filtration & Washing step of 2-Amino-4-

chlorophenol & 4-

Amino-2-chlorophen

ol; Distillation step of 2,

4, 5-Trichloro Aniline &

1,8 Diamino

Naphthalene

Category: 26.1

& Sch: I

NIL NIL 1020 1020


Transportation & disposed

to Co-processing

OR TSDF of M/s. BEIL,

Ankleshwar.

8 Spent Solvent

During production

of: Distillation

step of Hydrazide,

2,3 Dichloro 6

Category: 26.4

& Sch: I

NIL 49 1004 1053

Reused continuously in production

through distillation columns having

Primary and

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Page 65 of 76

Nitro Aniline

(DICONA); Nitro RF (O,O,O-Tris (4 -

nitrophenyl)

thiophosphate); 1,5 Dinitro

Naphthalene & 1,8 Dinitro

Naphthalene

secondary condensers inbuilt with reactors

without any storage in

the premises

9

Ammonia Solution (18 – 20 %)

From water Scrubber

attached to Reaction vessel of

2,3 Dichloro 6

Nitro Aniline

(DICONA)

Category: A-10

& Sch: II

NIL NIL 660 660


Transportation & Disposal by selling out to authorized

users who are having

authorization with valid

CCA and rule 9 permission

10

Sulphuric acid (70 - 72%)

During Production of: Nitration step of 1,5

Dinitro Naphthalen

e & 1,8 Dinitro

Naphthalene

Category: B-15

& Sch: II

NIL NIL 546 546


Transportation & Disposal by selling out to authorized

users who are having

authorization with valid

CCA and rule 9 permission



(For HW management)

For existing Hazardous waste quantity,

unit is having the Membership of

CHWIF & TSDF of M/s. BEIL,

Ankleshwar.

For proposed additional Hazardous

waste, unit is under process of

obtaining membership.



Not Applicable


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Page 66 of 76

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

Solvents

� There shall be a dedicated solvent recovery system consisting of re-boiler

vessels, packed columns and primary and secondary condensers having cooling

water and chilled water as cooling media. Distillation shall be carried out at

atmospheric as well as vacuum conditions to obtain approx. 95-98 % of solvent

recovery and shall be reused.

� Spent Solvent generated from production of Hydrazide, 2,3 Dichloro 6 Nitro

Aniline (DICONA), Nitro RF (O,O,O-Tris (4 -nitrophenyl) thiophosphate), 1,5

Dinitro Naphthalene & 1,8 Dinitro Naphthalene shall be reused continuously in

production through distillation columns having Primary and secondary

condensers inbuilt with reactors without any storage at the premises.


� Handling of chemicals will be in closed system. Primary and secondary

condensers are proposed.

• Unit is having CCA of the Board for existing products. Total water consumption will be 25.90

KLD. Total wastewater generation will be 12.9 KLD.

• Process effluent: Primary treated process effluent shall be sent to CMEE of M/s. ACPTCL

(Ankleshwar Cleaner Process Technology Centre Private Limited), Ankleshwar.

• Washing effluent: Primary treated washing effluent shall be sent to CETP (Common Effluent

Treatment Plant) of M/s. ETL (Enviro Technology Limited), Ankleshwar after conforming to

their inlet norms through tankers for final disposal.

• Committee deliberated on area adequacy, waste water management, storage & handling of

Hazardous chemicals, VOC & LDAR etc.

• While discussing about the product profile in context to expansion of the project, PP requested

to allow them to continue existing product Hydrazine with 5 MTPM with total production

capacity unchanged. PP submitted revised Form-1 with relevant details.

• Committee observed that there is no change in water consumption, waste water generation

etc. due to proposed change in product profile.

• Committee also observed that waste water pollution load on CETP will be reduced due to

proposed expansion.

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.

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

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

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Page 67 of 76

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.

• Details with respect to justification for proposed expansion: (1) To address proportionate

availability of space for production plant. (2) To address proportionate availability of storage

area for raw materials finished goods, utilities and goods carrier movement within premises.

(3) To address proportionate captive/common infrastructure available to accommodate

additional load due to proposed expansion. (4) Environment impact and its mitigation

measures for common/ captive infrastructure due to proposed production.

• 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.

• Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvent proposed

for use in-house with detailed chemical properties including vapor pressure. LDAR shall

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

• Feasibility report for reuse of process effluent for industrial purpose without proper treatment.

• Action plan for waste water generation considering 18 (1) (b) directions under the Water Act

1974 imposed by CPCB on CETP. Zero Liquid Discharge for waste water in addition to

consented quantity for discharge into CETP. Keeping in view quantity as well as quality of the

effluent

• Qualitative and quantitative analysis of hazardous waste streams generation from the

manufacturing process (Product wise). 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 shall be incorporated in EIA

report.

• 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 likeSulphuric acid, HCl, various solvents etc.

• Submit status of compliance of Environmental norms of Common Infrastructure.

• 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.

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

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

8. SIA/GJ/IND2/19749/2017 M/sRemik Chemicals Pvt. Ltd

Plot No. 3109 & 3110, GIDC – Panoli Dist.-Bharuch, Gujarat

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/19749/2017dated 06/05/2018 for


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

06/09/2017.

• Project proponent has submitted EIA Report prepared by M/s: Envisafe Environment

Consultants, based on the TOR issued by SEIAA.

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

as tabulated below:

Sr. No.

Name of Products CAS No. *Capacity (TPM) Use of

Product E P T

1. Aniline 2-4 Disulphonic Acid 137-51-9 Nil 50 – Real

base (71 As is)

50 – Real base

(71 As is)

Dyes Intermediate

2. Aniline 2-5 Disulphonic Acid 98-44-2 Nil 250 – Real

Base (313 As is)

250 – Real Base

(313 As is)

3. Tech. Sulphanilic Acid 121-57-3 100 400 500

4. Pure Sulphanilic Acid 121-57-3 Nil 200 200

5. Metanilic Acid 121-47-1 Nil 200 200

Total 100 1,100 1,200


Notification 2006.

• Earlier, PP was called for presentation in the SEAC meeting dated 13/06/2018.

• During the meeting dated 13/06/2018, technical presentation made during the meeting by

project proponent. During the meeting, the project was appraised based on the information

furnished in the EIA Report and details presented during the meeting.

• The proposal is for expansion. This unit is having valid CC&A for existing unit. Copy of CC&A,

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

public complaints against the project.

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

only after satisfactory submission of the following: (1) Certified Compliance Report (CCR)

from the Member Secretary, GPCB as per the MoEFCC’s Circular no. J-11011/618/2010- IA

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(II) (I) dated 30/05/2012 and Circular no. J-11013/6/2010-IA-II (Part) vide dated 07/09/2017.(2)

Exact source of Hazardous waste and its management as per the HW Rules 2016. (3)

Sources, quantification, APCM and management of bleed liquor for all type of process gas

emissions like SO3, Aniline, CO2 etc. (4) Adequacy of APCM for flue gas emission keeping in

view prevailing guidelines of GPCB. (5) Feasibility to reuse condensate waste water for

cooling purpose. (6) Adequacy of ZLD with quantitative and qualitative analysis of waste

water.

• PP submitted reply for the above mentioned additional details vide their letter dated

19/11/2018



Sr.

no. Particulars Details

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

Existing: 0.86

Proposed: 9.14

Total: 10.00

(1) Capital cost for EMS (Environmental Management System):2.51 Crore

Recurring cost towards the environmental protection measures: 1.18 Crore/Annum.

B Total Plot area (sq. meter) 3,000

Green belt area,/Tree Plantation area (sq.

meter)

Existing: 300

Proposed: 700

Total: 1,000

C Employment Generation Existing: 10

Proposed: 80

Total: 90

D Water[Existing & Proposed]

i


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

GIDC

Status of permission from the concern authority: Water is sourced from GIDC water supply

and the same source will be utilized after proposed expansion project.

ii Water consumption (KL/day)

-

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1.0 6.0 7.0 Fresh

(B) Gardening 0.5 2.5 3.0 Fresh

(C) Industrial

Process & APCM 2.4 24.6 27.0 Fresh

Nil 73.0 73.0 Reuse

Boiler Nil 54.0 54.0 Fresh

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Cooling 1.0 56.0 57.0 Fresh

Nil 23.0 23.0 Reuse

Washing Nil 5.0 5.0 Reuse

Total Industrial Water

Requirement (C)

3.4 235.6 239.0 Fresh + Reuse

3.4 134.6 138.0 Fresh

Total Water

Requirement(A+B+C) 4.9 143.1 148 Fresh

(1) Total Water Requirement for the Project: 249 KLD

(2) Quantity to be recycled/reused: 101 KLD

(3) Total Fresh water requirement: 148 0KLD

-

iii Waste water generation (KL/day)

-

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 1.0 4.0 5.0

(B) Gardening Nil Nil Nil

(C) Industrial

Process & APCM Nil 127 127

Boiler Nil 3.0 3.0

Cooling Nil 20.0 20.0

Washing Nil 5.0 5.0

Total Industrial

Effluent Generation Nil *155 *155 Generation

Total Industrial

Effluent Discharge Nil *Nil *Nil ZLD

*Difference of 54 KLD between Generation and Reuse is accounted as under:

Gypsum Sludge: 34.4 TPD, Sodium Sulphate Sludge: 1.1 TPD, MEE Salt: 0.5 TPD,

Solid Waste (Organic): 12 TPD. Atmospheric Loss: 6

-

iv Treatment facility within premise with capacity

(ETP, CETP, MEE, STP etc).

ETP: 35 KLD (Hy. Load: 28 KLD)

MEE: [3 Nos. x 50 KLD (Hy. Load: 120 KLD)]

ATFD: [3 Nos. x 103 kg/hr (Hy. Load: 248 kg/hr)]


Domestic: To soak pit through septic tank

Industrial: • Low COD/TDS stream from Utilities and washing will be treated in existing

ETP. Treated effluent from ETP will be sent to MEE for further treatment.

• High COD/TDS stream from process will be sent to MEE.

• Condensate from MEE will be re-used in manufacturing process, cooling

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and washing. Hence, unit will maintain 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) --


viii Reuse/Recycle details (KL/day)

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

MEE: 101

Process &

APCM: 96

Washing: 5

400 800 180

E Air (Existing & Proposed)

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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

Enission with

Capaity

Stack

Height &

Dia. (m)

Fuel Name

& Qty.

Type of

emission&

Permissible

Limit


Measures

1 Steam Boiler

(6 TPH)

25.0 &

Dia.1.0

Bio-fuel

(Agro waste)

&/OR

Coal

(17.5 TPD)

PM ≤ 150

mg/Nm3

SO2 ≤ 100

ppm

NOx ≤ 50

ppm

Multicyclone

Separator followed by

Bag filter

2

Thermic

Fluid Heater

(3 Lac Kcal/hr)

10.0 &

Dia.0.5

Natural Gas

(595 SCM/Day)

Stack of Adequate

height

3

DG Set

(300 KVA),

Stand-by

7.0&

Dia.0.15

Diesel

(65 Lit/hr)


as per CPCB

Guidelines

-


-

Sr.

No

.

Source of

Emission Status

Ht. &

Dia. (m)


Equipment

Type of

Emission

&Permissible

Limit 1st Stage 2nd Stage

1. Ball Mill Existing 9.0 &

Dia. 0.2

Wet/ Acid

Scrubber

(A)

-- PM ≤ 150

SO2 ≤ 40

2. All

Reactors Proposed

9.0 &

Dia. 0.2

Alkali

Scrubber

(B)

Alkali

Scrubber

(C)

SO2 ≤ 40

-

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

There are chances of fugitive emission and odour nuisance during manufacturing process as

well as due to storage & handling of raw materials and products in existing as well as

expansion phase.The unit has taken following precaution for the control of fugitive emission

and same will be adopted 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.

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• Dedicated measuring tanks will be provided to each

reactor.

• Usage of closed handling system for odorous

chemicals /solvents as far as possible.

Emission from bulk storage

tanks during storage, loading,

unloading

• Bulk storage of odorous chemicals will be adopted and

usage of drums/Carboys for such materials are avoided

as far as possible.

• PSVs, Rupture disc, Vapor recovery system will be

installed for process/storage tank vents.

Hazardous chemical storage

area

• Dedicated storage area will be provided

• Adequate ventilation systems will be provided

• All the containers will be kept tightly closed

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

containers

• Transfers of odorous waste are carried out preferably

during day time. Transfers during odd hours are

avoided.

Chemical vapor from wet

cake in filtration and drying

area

• Covered transfer systems will be adopted, workers will

be provided with PPE.

• Fume extraction systems will be provided, wherever

required.

Pump and compressor

Emissions

• Mechanical seals will be provided in pumps and

agitators

• Standby arrangement for critical equipment and parts

will be ensured.

• Drip trays will be placed for each pump to collect

leakages and spillages.

Valves, Flanges, plugs and

instrument connections

• Welded pipes will be used wherever feasible.

• Suitable gasket materials will be used.

• Suitable glad packing will used in valves.

• Periodic inspection and maintenance of pipes and pipe

fittings will be carried out.

Release from sampling lines • Closed loop system is used.

F Hazardous waste [Existing & Proposed]

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

Rules 2016.

i -

Type of

waste

Source of

generation Category

*Quantity per

Annum Method of Disposal

E P T

ETP

Sludge ETP

Sch-1

35.3

- 45

MT

45

MT Collection, Storage,

Transportation, Disposal by

landfilling at TSDF MEE Salt MEE - 155

MT

155

MT

Gypsum ETP - 10,725 10,725 Collection, storage and send to

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Sludge (Prod. 1 &

2)

MT MT cement industry for co-

processing on priority, if not

available Disposal by landfilling

at TSDF

Sodium

Sulphate

Sludge

MEE

(Prod. 5) -

355

MT

355

MT


Transportation, Disposal by Sale

to authorized end-user having

permission under Rule 9 on

priority, if not available Disposal

by landfilling at TSDF

Solid

Waste

(Organic)

MEE/ATFD

(Prod. 1, 2

& 5)

- 3,715

MT

3,715

MT Collection, storage and send to

cement industry for co-


available Disposal by

incineration at CHWIF

Spent

Carbon

Mfg.

(Prod 4)

Sch-1,

26.1 -

265

MT

265

MT

Solid

Waste

(Organic)

Mfg.

(Prod. 2)

Sch-1,

26.1 -

675

MT

675

MT

Iron

Sludge

Mfg.

(Prod. 5)

Sch-1,

26.1 -

1055

MT

1055

MT


Transportation, Disposal by

landfilling at TSDF

Crude

Sulphanilic

Acid

Mfg.

(Prod. 3)

Sch-1,

26.1 -

167

MT

167

MT

Collection, Storage and Captive

Re-use in Manufacturing of

Tech. Sulphanilic Acid

Sodium

Sulphate

[Avg 23%

(20-25%)]

Mfg.

(Prod. 4),

APCE (Prod

1, 2, 5)

Sch-1,

26.1 -

1,935

MT

1,935

MT


Transportation, Disposal by Sale

to authorized end user having

permission under Rule 9 on

priority, if not available Treated

along with effluent in MEE

Process

Waste

(Gypsum)

Mfg.

(Prod. 5)

Sch-1,

26.1 -

1,465

MT

1,465

MT

Collection, storage and send to

cement industry for co-


available Disposal by landfilling

at TSDF

Discarded

Drums /

Bags

RM Storage

& Handling

Sch-1,

33.1

4.50

MT

18.50

MT

23

MT


Decontamination and Disposal

by selling to scrap vendors

Spent Oil /

Used Oil

Plant &

Machineries

Sch-1,

5.1

0.01

KL

0.05

KL

0.06

KL


Transportation, sell to registered

Re-processor / MoEF&CC

approved recyclers on priority, if

not available Reuse as

Lubricant within premises

*E-Existing, P-Proposed, T- Total after Proposed expansion

-

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ii Membership details of TSDF, CHWIF etc. Unit will obtain membership from GPCB

approved TSDF / CHWIF


(MSW and others)

-

G Solvent management (If any)

I Details of Solvent recovery (As per respective

ToR)

Not applicable since, there is no solvent

requirement for the proposed expansion

project.

ii VOC emission sources and its mitigation

measures

As mentioned in section E (iii) above.


• Committee noted that there is no partially complied or non-complied conditions as per the

Certified Compliance Report (CCR) dated 05/10/2018 received from GPCB on 23/10/2018.

• Revised Hazardous waste management matrix is submitted. However, PP has not explored

environmental friendly method of disposal for Gypsum sludge.

• Complete details regarding APCM for flue gas & process gas emission with adequacy report

is submitted.

• PP now proposes to reuse condensate waste water for Process & APCM in place of cooling

tower. However, PP has not submitted feasibility report for reuse of waste water.

• Adequacy certificate for ZLD prepared by M/s. Darshan Institute of Engineering & Technology

is submitted along with the EIA Report.

• Total water consumption will be 16.8 KLD. Total wastewater generation will be 249 KLD.

• 155 KLD effluent will be given primary treatment in ETP and then sent it to MEE for further

treatment and disposal.

• 101 KLD MEE condensate will be reused back in process.Agro waste and or coal will be

used as fuel for proposed boiler.




project site for the period Nov ’17 – Jan ‘18. Ambient Air Quality monitoring was carried out for

PM10, PM2.5, SO2, NOx, HCl, Cl2, HBr, NH3, 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 ISCST3. The

resultant concentrations are within the NAAQS. Colour, turbidity, dissolved solid, alkalinity,

total hardness; calcium, magnesium, chlorides, Sulphate, and Boron were found above

desirable limits in some of Surface water and ground water samples. Turbidity was found

exceeding the permissible limit in 1 surface water sample whereas dissolved solids, total

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hardness, magnesium and chlorides were found exceeding the permissible limit in 3 ground

water samples.




• Committee deliberated on reply submitted & presentation made by PP.

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

only after satisfactory submission of the revised EIA report.

1. Unit shall explore the possibilities for environment friendly method for disposal of Gypsum

waste, Land-fillable wastes and Incinerable hazardous wastes.

2. Feasibility to reuse condensate waste water for Process & APCE. Give separate quantity of

water consumption and waste water generation.

Meeting ended with thanks to the Chair and the Members.

Minutes approved by:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

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

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

minutes of the 454th 28/11/2018 at committee room, geer ... minutes of the 454th i.pdf · removed...

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