minutes of the 432 meeting of the ... minutes of the 432th i.pdf · 1 common effluent treatment...

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432ndmeeting of SEAC-Gujarat, Dated 11.09.2018

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Minutes of the 432thmeeting of the StateLevelExpertAppraisalCommittee held on 11/09/2018 at

Committee Room, GEER Foundation, Gandhinagar.

The 432thmeeting of the StateLevel ExpertAppraisalCommittee (SEAC) was held on

11thSeptember2018 at Committee Room, GEER foundation, Gandhinagar. Following members

attended the meeting:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

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

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

6. Shri A. K. Mule, 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.

6. SIA/GJ/MIS/19756/2017 M/s. Ajrakhpur Hastkala Vikas Sangathan (CETP) Common Plot No. 1 of survey no. 694 of Paddhar-Ajrakhpur, Post: Kukma, Ta.:Bhuj, Dist.: Kutch.

Appraisal

Project / Activity No.: 7(h)

Project status: New

• PP has submitted online application vide no. SIA/GJ/MIS/19756/2017 dated 19/07/2018 for obtaining

Environmental Clearance.

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

28/09/2017.

• Project proponent has submitted EIA Report prepared by M/s: Shivalik solid waste management Ltd,

based on the TOR issued by SEIAA, Gujarat.

• Public Hearing was conducted by Gujarat Pollution Control Board on 08/05/2018 at project site of

M/s. Ajrakhpur HastkalaVikas Sangathan (CETP) at Common Plot No. 1 of survey no. 694 of

paddhar-Ajrakhpur, kutch.

• This is a new unit proposes for Common Effluent Treatment Plant as tabulated below:

Sr. no.

Treatment Facility Capacity

1 Common Effluent Treatment Plant (CETP) 150 KLD

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

2006.

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• PP was called for presentation in the SEAC meeting dated 11/09/2018.

• Salient features of the project are as under:

S.

No.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 1.46Crores

B Total Plot area (sq. meter) 1102.5 Sq. m.(CETP covered area)

Green belt area,/Tree Plantation area (sq. meter) 277 Sq. m.

C Employment generation During construction Phase: 6 persons

During Operational Phase: 4 persons

D Water

i

Source of Water Supply

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

Tankers

Status of permission from the concern authority.

ii Water consumption (KLD)

Category KLD

(A) Domestic 2

(B) Gardening --

(C) Industrial

Process --

Washing --

Boiler --

Cooling --

Others 3

Industrial Total 3

Total (A + B + C) 5

1) Total water requirement for the project:5 KLD

2) Quantity to be recycle: 3 KLD

3) Total fresh water requirement:2 KLD

iii Waste water generation (KLD)

Category Waste water KLD Remarks

(A) Domestic 1.6 Septic tank/ Soak pits

(B) Industrial

Process --

Washing --

Boiler --

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Cooling --

Others --

Total Industrial

waste water

--

Total [A + B] 1.6

-

iv Treatment facility within premises with capacity

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

1 Coarse Screen � 60 deg. Inclined to horizon � Made of PP flats of 6 x 30

mm. � Spacing 20 mm center to

center of the bars. � Size: 500 mm X 700 mm

01 Nos.

2 Bar Screen � 60 deg. Inclined to horizon � Made of PP flats of 6 x 30

mm. � Spacing 20 mm center to

center of the bars. � Covered with 10 size SS 304

mesh folding type � Size: 500 mm X 700 mm

01 Nos.

3. Effluent Withdrawal Pump

� Type: Centrifugal, non-clog � Flow rate: 15 m3 /hr � H.P.: 3.0

(1w+1s)=2 Nos.

4. Reaction Tank-1 � Size 2.0M x 1.0M x 1.5 M

01 No.

5. Reaction Tank-2 � Size 4.0M x 1.0M x 1.5 M

01 No.

6. Tube Settler � Dimension ø 4.0 m x 4.0 m height

02 No.

Civil items

S.No

ITEMS PARTICULARS QTY.

1 Equalization Tank-1

� Size: 4 M X 4 M X 3 M (SWD: 01 No

2. Equalization Tank-2

� Size: 7 M X 6 M X 6 M (SWD: 01 No

3. Storage Tank � Size: 6.0M X 4.0M X 3.0M 01 No

4. Sludge Sump � Size: 3.0 M X 3.0 M X 3.5M 01 No

5. Lab, Panel & Office Rooms

� Size: 5.0 M X 4.0 M X 5.5 M 01 No

6. Sludge Drying Beds

� Size: 5 M X 4 M X 1M

01 No

7. Foundation � For tube settlers 01 Lot

Electro-mechanical items

S.No. ITEMS PARTICULARS QTY.

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7. MBBR Cum Aeration Tank

� Size: 7.0M X 3.0M X 4.5 M 01 No.

8. Sludge (Screw) Pump

� Type: Screw pump � Flow rate: 5000 Ltr / hr. � HP: 3.0

01 No.

9. Blower � Type: Twin lobe type � Flow rate: 200 M3/hr � HP: 5.0/ 7.5

2 Nos.

10. Sec. Clarifier � Dimension: ø 4.5 m x 4.0 m height

01 No.

11. Sludge Recycling Pump

� Type: Centrifugal, non-clog type

� Flow rate: 7.5 M3/Hr � H.P.: 2.0

02 Nos.

12. Dosing Tanks � Agitator cum dosing tanks � Size: 2.0m x 1.0 m x 1.0 m

02 Nos.

13. Dosing Pumps � Type: Plunger/Diaphragm � HP: 0.5

4 Nos.

14. Lime Dosing Pump

� Type : Centrifugal � Flow rate : 1000-1500 LPH � Motor H.P. : 1.0

01 No.

15. Filtration Pump � Type centrifugal pumps. � Capacity: 15 M3 /Hr

(1w+1s)=2 Nos.

16. Multigrade Filter (Mgf)

� Dimension: Ø 1.0 X 2.2 M 01 No.

17. Iron Filter (Ir)

� Dimension: Ø 1.2 X 2.2 M 01 No.

19. Filter Press � Plate and frame type � Size = 600 mm x 600 mm

01 No.

20. D.G. Set � 10 KVA

01 No.

21. D.G. Diesel Storage Tank

� MOC: MS 01 No.

22. Lab Equipment Chemicals glassware’s & instrument for testing pH, BOD, COD, TDS & Total suspended solids etc

01 Lot.

23. INSTRUMENTATION

Level Controller

� Type : Fixed, � MOC : SS-316, � SIZE : 6 mm Rod

3 Sets

Electro-Magnetic Flow meter

� MOC : SS-316 flange mounted � Flow rate: 20 M3 /Hr � Dia : 40 mm � Make : Rose mount � With digital display LCD type � Instantaneous & Integral Flow meter

1 No

pH probe 1Nos

Pressure gauges

� Dia 4” dial � Make : H Guru/ waree � 0-5 Kg

6 Nos

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v Mode of Disposal & Final meeting point

Domestic: Septic Tanks

Industrial: The treated waste water proposed to be stored in overhead tank shall be supplied

for its use by member units for washing & flushing purpose.

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

CF

NA

Membership of Common facility (CF)

NA

Vii Reuse/Recycle details (KLD)

The treated waste water proposed to be stored in overhead tank shall be supplied for its use by

member units for washing purpose. Excess treated waste water shall be used for development

and maintenance of Green belt.

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.

S.

No.

Source of

emission

With Capacity

Stack

Height (meter)

Type of

Fuel

Quantity of

Fuel

MT/Day

Air Pollution

Control

Measures

(APCM)

Type of

emissions

i.e. Air

Pollutants

1

Proposed DG

set of capacity

10 KVA

As per CPCB

Norms <30 mts. Diesal

Depend upon

usage as

standby

Stack with

appropriate

ht.

PM,CO

Nox +HC

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

-

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

During Construction Phase: Dust will be generated and control by water sprinkling

F Hazardous waste

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

2016.

I S.

no.

Type/Name of

Hazardous

waste

Source of

generation

Category and

Schedule as

per HW Rules.

Quantity

(MT/Annum

)

Disposal Method

1 Chemical

Sludge

Physico-

chemical

treatment

35.5 37.5 kg/day TSDF site

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2 Bio Sludge Biological

treatment

4.5 kg/day To be used as

manure

3 Used oil DG Set 5.1 Depending

upon usage

Registered

recycler & for

lubrication

ii Membership details of TSDF, CHWIF etc.

M/s SaurashtraEnviro Projects Pvt. Ltd, which

is located in Kutch District may be the suitable

place for sludge disposal. A MoU for disposal

of waste will be done prior to start of operation

phase.

Iii Details of Non-Hazardous waste & its disposal

(MSW and others)

Non-Hazardous waste shall be disposed as per

MSW rules.

G Solvent management, VOC emissions etc.

NA

ii VOC emission sources and its mitigation measures

NA

• During the meeting dated 11/09/2018, technical presentation made by project proponent.

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

Observation:

• This proposal is for new CETP at proposed location.

• Total water consumption for CETP operation will be 5 KLD. The treated wastewater from CETP will

be stored in overhead tank and shall be supplied to member units for washing purpose Stand-by D.G.

Set is proposed and diesel will be used as fuel.There will be no process gas emission.

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

• Proposed CETP is for the treatment of waste water generated from 49 no.s of small & tiny textile

processing units who are engaged in this activity and are clustered around Ajrakhpur which is

popularly known as ‘Ajrakhpur Block Printing Cluster’.

• The proposed CETP is located within the cluster area. The effluent discharge from the participating

units will be taken to the CETP site through 150 mm dia. PVC Pipe, already laid down. The distance

from the nearest unit is 40 meters and 350 meters length is used to take the effluent from furthest

unit.

• This CETP will receive waste water generated from the small textile units. The treated waste water

proposed to be stored in overhead tank shall be supplied for its use by member units for washing

purpose.

• Online monitoring system in line with Central Pollution Control Board (CPCB) guidelines shall be

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installed to monitor flow and TDS.

• 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 Mid-

September 2017 to Mid-December 2017. Ambient Air Quality monitoring was carried out for PM10,

PM2.5, SO2, NOx, C6H6, O3 and CO at eight locations, including the project site. Values conform to

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

has been computed using AIRMOD. The resultant concentrations are within the NAAQS. The

modelling study proved that the air emissions from the proposed plant would not affect the ambient

air quality of the region in any significant manner. The ambient air quality around the proposed

project site will remain within the National Ambient Air Quality Standards (NAAQS).

• All the ground water parameter is well within permissible limit.

• 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.

• Public hearing was conducted at project site dated: 08/05/2018. The major points were discussed

during public hearing is water scarcity.

Discussions & Conclusion:

• Committee noted that the water source is existing bore well. However, they have not taken any

permission from CGWA. Upon asking, PP inform that they will apply to CGWA for ground water

withdrawal and till then they will fulfill their water requirement through tankers from paddhar gram

Panchayatborewell.

• PP has proposed to use excess treated waste water for development and maintenance of Green belt

which was not accepted by the Committee and asked to reuse treated waste water completely within

member units except utilization for green belt & plantation. PP agreed for the same. PP has

submitted characteristics of the combined effluent & treated waste water. CETP inlet norms are also

submitted by PP.

• PP has proposed primary, secondary and tertiary treatment units for treatment of waste water.

• PP has submitted legal undertaking regarding they will not allow any chemical units as a member of

this CETP.

• Committee deliberated on area break up of proposed site, CER, CETP inlet and outlet norms etc.

After deliberation, it was unanimously decided to recommend to SEIAA for grant of

EnvironmentalClearance (EC).

7. SIA/GJ/IND2/19513/2017 M/s. Black Rose Industries Limited

Plot No. 675, Notified GIDC Industrial Estate,

Appraisal

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Jhagadia, Dist – Bharuch, Gujarat, India.

Project / Activity No.: 5(f)

Project status: Expansion

• PP has submitted online application vide no. SIA/GJ/MIS/19513/2017 dated 19/07/2018 for obtaining


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

28/09/2017.

• Project proponent has submitted EIA Report prepared by Siddhi Green Excellence Pvt. Ltd.,

Ankleshwarbased on the TOR issued by SEIAA.

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

tabulated below:

Sr. No.

Name of Products

Existing quantity

Proposed quantity

Total after EC

expansion End Use CAS No. Remarks

MT / Month

1 Acrylamide Aqueous Solution (50%)

1666.66 -- 1666.66 Acrylamide

Polymers etc. 79-06-1 No change

2 Polyacrylamides (Powder)

-- 833.33 833.33

Water treatment,

oilfield chemicals etc.

25987-30-8, 25085-02-3, 69418-26-4, 9003-05-8

New Products

3 Polyacrylamides (Liquid)

-- 3333.33 3333.33 Water

treatment, binders etc.

25987-30-8, 25085-02-3, 33882-67-6, 26100-47-0

4 Polycarboxylates -- 416.67 416.67 Textiles, Paints

etc. 9003-01-4

5 N-Methylol Acrylamide

-- 166.67 166.67 Adhesives, etc. 924-42-5

Total 1666.66 4750.00 6416.66

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



Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): Proposed: 60 Crores (For expansion only)

(1) Capital cost for EMS (Environmental Management System): 65.2 lakh (2) Recurring cost towards the environmental protection measures: 90 lakh per Annum.

B Total Plot area ( sq. meter) Existing: 34075 Sq.m Proposed: 00 Sq. m. Total: 34075 Sq. m.

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

Existing: 12540 Sq.m Proposed: 00 Sq.m

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Total: 12540 Sq.m

C Employment generation

1. Direct Existing: 32 nos. company employees + 3 nos. on contract basis Proposed Additional: 45 nos. company employees + 5 nos. contract basis Total After Proposed Expansion: 77 nos. company employees and 8 nos. contract workers

2. Indirect

D Water

i

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

GIDC


As per CTO, Industrial = 93.5 KL/day Domestic = 7.5 KL/day

Letter from GIDC for supply of additional quantity of water required for expansion is received.


Type In KL / day Existing GIDC water

consumption granted as

per CTO

Actual additional water

requirement for expansion

Total water requirement

after expansion

1 2 3

(i) Domestic

: 7.500 0.000 7.500

(ii) Industrial

: (a)Process Plant

: 35.660 181.500 217.160

(b) Boiler : 6.380 193.000 199.380

(c) Cooling : 46.500 155.000 201.500

(d) Washing : 1.250 2.000 3.250

(g) Gardening : 16.275 19.900 36.175

Domestic : 7.500 0.000 7.500

Industrial : 106.065 551.400 657.465

Total : 113.565 551.400 664.965

Recycle water for Industrial 10.750 195.000 205.750

Recycle water for Gardening 1.815 4.900 6.715

Total GIDC Water Requirement 101.000 351.500 452.500

1) Total water requirement for the project: 664.965 KLD

2) Quantity to be recycle: Steam condensate recycle- 185.5 KLD to be returned to boiler, RO

permeate- 20.25 KLD to be used for process, washing and utility makeup, MEE condensate water- 6.715 KLD to be used for green belt development and / or utility makeup.

3) Total fresh water requirement: 452.500 KLD


Wastewater generation (KLD)

Existing As per CTO

Additional after

expansion

Total after proposed expansion

Disposal Method

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(i) Domestic

: 7.0 0.0 7.0 To Soak pit via Septic tank

(ii) Industrial

: (a) Processing

: 1.5 2.5 4 To ETP (Primary and secondary treatment) and

then to RO (b) Boiler : 0.85 12 12.85

(c) Cooling : 3.5 5 8.5 To RO & MEE plant

(d) Washing : 1.25 0.5 1.75

DOMESTIC : 7.0 0.0 7.0 To Soak pit via Septic tank

INDUSTRIAL : 7.1 20.0 27.1

20.25 (treated effluent from RO & MEE plant for recycling to process), 6.715 (MEE condensate recycling to gardening), 0.135 (MEE sludge to TSDF site)

TOTAL 14.1 20.0 34.1

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

ETP Capacity (Existing)= 5 KLD MEE Capacity (Existing)= 28.8 m3/day RO capacity (Existing)= 7.2 m3/day


Domestic: Disposed off through soak pit via septic tank

Industrial: Unit is ZERO liquid Discharge. 20.25 (treated effluent from RO & MEE plant for recycling to process), 6.715 (MEE condensate recycling to gardening), 0.135 (MEE sludge to TSDF site)

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

---

Membership of Common facility (CF) --- vii Reuse/Recycle details (KLD) Refer point no. D (ii) & (iii)

E Air [Existing & Proposed] i Flue gas emission details


Sr. No.

Stack PCB ID/

Stack Attached to

Capacity/ Remarks

Fuel used & rate of consumption

Air Pollution Control

Measures (APCM)

Stack Height

in meter (From G.L.)

Parameter

s

Permissibl

e Limit

s

Unit

As per Existing CTO

1 (Existi

ng)

54563-Baby

Boiler*

Baby Boiler-I (Cap: 0.4 TPH) & Baby Boiler-II standby ((Cap:

0.4 TPH)

H.S.D (400

Lit/Day)

Adequate Stack

Height with SMF

30 PM SO2

NOX

150

100 50

mg/ Nm

3

ppm ppm

2 (Existi

ng)

90941- D.G. set**

D.G Set (380 KVA)

H.S.D (100

Lit/Day)

Adequate Stack

Height with SMF

9

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Proposed additional

3 (New)

Boilers x 2 nos.

Boilers x 2 nos. (Capacity of Boiler no.1- 2500 kg/hr-.

& Boiler no.2 - 5000 kg/hr)

imported coal –

22 MT/day

Multi Cyclone

Separator, Bag Filter and Water Scrubber to each boiler

30

(common stack)

PM SO2

NOX

150

100 50

mg/ Nm

3

ppm ppm

4 (New)

D.G. Set

D.G. Set (500 KVA)

HSD – 900

lit/day

Adequate Stack

Height with SMF

11

*After proposed Expansion existing small industrial non IBR boiler will be stand by. ** D.G. sets are and shall be used as stand-by power only during power failure.

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

There is no process emission from existing manufacturing process and there shall be no process emissions from proposed new products also. However, as the process involves use of organic nitrogen compounds, as an additional measure towards controlling traces of Hydrocarbons and ammonia during process, it is proposed to install a water scrubber attached to all reactor vents at new production plant. Proposed process stacks

Stack No.

Stack PCB ID / Stack

Attached to

Name of Process / Plant

Air Pollution Control System

Height (m)

Air Emission

Pollutant Permissible

Limit

1 (New)

Reaction Vessels

Production plant -

new

Water Scrubber

15 HC

traces NH3

20 mg/Nm3

175 mg/Nm3

Scrubbing solution shall be sent to ETP for treatment and recycle by RO and MEE. iii Fugitive emission details with its mitigation measures.

[Existing & Proposed]..As below

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Sr. No.

Probable sources

Proposed Control measures

1 Pump glands and seals

All process pumps handling HAP chemicals with low V.Ps will be seal less, ensuring no emissions.

2 Emissions from Bulk Storage Tanks during storage, loading and unloading

Storage tanks storing acrylonitrile and acrylic acid are provided with Breather valve assembly. Set pressure of breather valves is kept above the vapor pressures of stored material to avoid fugitive emission. Tank Pressure equalization shall be applied wherever required Closed transfer system will be provided.

3 During reactions All reactors shall be closed and provided with condenser with required utility. Temperature and pressure conditions shall be stringently controlled as per the process requirement and optimized with low temperature and vacuum conditions wherever feasible.

4 Release from Sampling Lines

Shall be carried out using a closed loop sampling system.

5 Valves, Flanges, plugs and instrument connections

Welded pipes to be used wherever feasible Suitable gasket material to be used Suitable gland packing to be used in valves Periodic inspection and maintenance of pipes and pipe fittings

6 Emissions during filtration process

Closed filtration system to be provided. Workers shall be provided PPEs as per requirement.

7 Drum filling machinery

Closed transfer systems shall be adopted, workers shall be provided PPEs, minimum manual operations

8 Warehouse storing drums and bags

Spillages shall be strictly prevented, proper handling equipment. Roof top ventilators Spill control procedures and equipment shall be provided

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

i

Sr. No.

Type of Waste

Source of

Generation

Sch.

Category

(As per Sched

ule Rules-2016)

Quantity MT Per Annum

Facility Mode of

Treatment & Disposal

Existing

Proposed

Total

1

Empty barrels/containers/liners/bags with hazardous

chemicals/wastes

Raw material containers/ Bags

I 33.1 2.01 603.99 606.0

0

Collection, Decontamin

ation, Disposal, Reuse,

Storage, Transportati

on

Disposal by send It to authorized decontamination facility/recycler or

reuse or send back to supplier

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2

Waste Polyacrylam

ide

From producti

on of Polyacrylamides Liquides

& powder

I 34.2 40.1

5 319.85

360.00

Co-processing, Collection, Disposal,

Treatment, Storage,

Transportation

Send it to TSDF of BEIL, Ankleshwar Send for co-processing to RSPL

3

Spent ion exchange

resin containing

toxic metals

DM plant

I 35.2 0.50 5.50 6.00

Collection, Disposal,

Treatment, Storage,

Transportation

Disposal by send it to TSDF of BEIL, Ankleshwar

4

Sludge from ETP

From ETP

I 35.3 0.73

1.10

1.83

Collection, Storage,

Treatment, Transportation, Disposal

Disposal by sent it to TSDF site of M/s. BEIL, Ankleshwar.

5 Sludge from

MEE From MEE

I 35.3 12.7

8 352.23

365.00

Collection, Storage,

Treatment, Transportation, Disposal

Disposal by sent it to TSDF site of M/s. BEIL, Ankleshwar.

6

Spent Carbon or

filter medium

From production of Polyacrylamides Liquides&powde r

I 36.2 71.1

8 84.83 156

Co-processing, Collection,

Incineration, Disposal, Storage,

Transportation

Disposal by incineration in common incinerator of BEIL, Ankleshwar , send it for co-processing to RSPL

7 Used or spent oil

Machinery

I 5.1 1.10 10.905 12.00

Collection, Disposal, Reuse,

Storage, Transportati

on

Disposal by Reuse in plant & machinery as lubricant or sell it to authorized re-refiners/recycler.

Non Hazardous Waste Generation

Sr. No.

Type of Was

te

Category (As Per

Sc)-2016

Quantity (MT/Annum) Source of Generatio

n

Mode of Treatment & Disposal

As per Existing CTO

EC applied for Additional

Qty

Total After EC expansio

n

1 Ash --- --- 1210 1210 From coal combustio

n

To be sold to brick Manufacturers or manufacturers of Cement articles or products


Unit has obtained Letter of acceptance from M/s. Bharuch Enviro Infrastructure Ltd.

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(BEIL) for accepting landfill waste at their TSDF and incinerable waste at CHWIF site at Ankleshwar. Unit is having MoU with M/s. Recycle Solutions Pvt. Ltd., Panoli unit for sending spent carbon and polymer waste for co-processing. Letter of acceptance for additional quantities is also obtained from RSPL

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

Fly ash: 1210 MT/Annum shall be sold to brick manufacturers and manufacturers of Cement articles or products


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

Solvent Recovery - No solvent is used at site and proposed expansion also doesn’t involve any solvents.

ii VOC emission sources and its mitigation measures Refer point no. E (iii)


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

&CC&A from the concern authorities. The proposal is for expansion by addition of new Synthetic

Organic Chemicals.


Observation:

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

product. The earlier unit hasgot EC in 2012 and amended in 2016. Unit has gotCC&A for existing

unit. Copy of EC, EC amendment, CC&A, compliance reports of all is submitted. PP ensured that

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

• Total water consumption will be 664.965 KLD. Total wastewater generation will be 27.1 KLD.4 KLD

out of process wastewater and washing will be treated in ETP. Treated water from ETP, cooling and

washing will be goes through RO followed by MEE. The unit will maintain complete ZLD.

• Imported Coal will be used as fuel for proposed boilers.

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

• Hazardous waste management will be adequately provided.



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

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

NOx, C6H6, NH3, CO and VOC 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 AIRMOD. The resultant concentrations are within the NAAQS. The

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Page 15 of 49

modelling study proved that the air emissions from the proposed plant would not affect the ambient

air quality of the region in any significant manner. The ambient air quality around the proposed

project site will remain within the National Ambient Air Quality Standards (NAAQS).





• The Certified Compliance Report (CCR) is submitted by RO and it was discussed in detail. PP has

submitted compliance status with respect to non-compliance of CCR which was found satisfactory.

• Committee deliberated on product profile and its use, wastewater management, safety measures.

• Committee asked PP for management of Hazardous waste as per the HW Rules 2016.

• EMP, SCR & CER was discussed in details.

After deliberation, it was unanimously decided to recommend to SEIAA for grant of Environmental

Clearance (EC).

8. SIA/GJ/IND2/28507/2017 M/s. Robin Dyes and Intermediates Pvt. Ltd. Plot No. 810/2, GIDC Estate, Sachin, Ta. Chorasi, Dist: Surat – 394 221, Gujarat

EC Amendment


Project status: Amendment of EC

• SEIAA, Gujarat has accorded Environment Clearance to M/s. Robin Dyes and Intermediates Pvt. Ltd.

vide letter no. SEIAA/GUJ/EC/5(f)/460/2017 Dated: 29/04/2017

• Now, project proponent (PP) has applied online vide proposal no. SIA/GJ/IND2/28507/2017dated

18/07/2018 for Amendment in EC.

• The existing product profile is as per existing EC as tabulated below:

Sr. No.

Name of the Products

CAS no. /CI no.

Existing Quantity

MT/Month

Total Proposed Quantity

MT/Month

End-use of products

1 G-Salt 118-32-1 7.5 35 Dyes

2 R-Salt 148-75-4 -- 15 Dyes

3 Amido G-Acid 86-65-7 -- 35 Dyes

4 K-Acid 118-03-6 -- 30 Dyes

Total 7.5 115




Sr. no.

Particulars Details

A Total cost of Proposed Project

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Page 16 of 49

(Rs. in Crores): Existing: 2.0Crores Proposed: 2.0 Crores Total: 4.0 Crores

1. Capital cost for EMS (Environmental Management System):1.0 Crores

2. Recurring cost towards the environmental protection measures: 1.5 Crores per Annum.

B Total Plot area ( sq. meter) Existing: 4842.3 Sq. m. Proposed: 00 Total: 4842.3 Sq. m.

Green belt area,/Tree Plantation area ( sq. meter) Existing: 00 Proposed: 1600 Sq. m. Total: 1600 Sq. m.


1. Direct 15

2. Indirect 20

Total 35

D Water

i

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

GIDC Water Supply


Company is obtained the permission for water supply from GIDC


Category

Existing Water Consumption KLD

Total Proposed Water Consumption KLD

(A) Domestic 2.00 4.00

(B) Gardening 0.0 4.00

(C) Industrial

Process 2.00 12.0

Washing 0.00 1.00

Boiler 2.00 5.00 Cooling 0.50 10.00

Others 00 0.3

Industrial Total 4.5 28.3

Total (A + B + C) 6.5 36.3


2) Quantity to be recycle: 0.0 KLD

3) Total fresh water requirement:41.0 KLD


-

Category Existing Waste water generation KLD

Total Proposed Waste water generation KLD

(A) Domestic 2.00 4.00 (B) Industrial

Process 2 10

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Page 17 of 49

Washing 00 1

Boiler 00 0.5

Cooling 0.5 0.5 Others 0.25

Total Industrial waste water 2.5 12.75

-

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

ETP – 10 KL/Day (2 Nos.)


Domestic: 4.0 KL/Day

Industrial: 12.75 KL/Day Proposed Total: 6.114 KL/Day (As per EC Amendment) -> Primary treated effluent conforming to CETP inlet norms will be sent to CETP of Ms. GECL for further treatment and disposal. Proposed Total: 6.636 KL/Day (As per EC Amendment) -> Primary treated effluent conforming to CETP inlet norms will be sent to Common MEE facility of Ms. GECL for further treatment and disposal.


Common facility – CETP and Common MEE

Membership of Common facility (CF) CETP – GECL/18-19/11 dated: 06/06/2018

vii Reuse/Recycle details (KLD) 0.00

E Air

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

Existing:

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)

1 Baby Boiler 30

Agrowaste

2 MT/Month

SPM SO2 Nox

Adequate Stack Height/MCS

2 TFH (200 U)

30 Adequate Stack Height/MCS

3 D. G. Set - Stand By (Capacity: 125

KVA ) 11 LDO 100 Lit/Hr

SPM SO2 NOx

Adequate Stack Height

Additional

SR. no.

Source of emission

With Capacity


Type of Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 *Thermopack (600 U)

30

Agrowaste 60

MT/Month

SPM SO2 Nox

Cyclone Separator

2 Hot Air Generator

30 Cyclone

Separator

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Page 18 of 49

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

Existing:

Sr. no.

Source of emission

Type of emission

Stack/Vent Height (meter)

Air Pollution Control Measures (APCM)

1 Reactor - 1 SO2< 40 mg/Nm3

15.0 Two Stage Alkali

Scrubber

2 Reactor - 2 SO2< 40 mg/Nm3

12.0 Two Stage Alkali

Scrubber

-

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

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

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

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

and temperature.

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

connected to vent chillers.

• Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer

area, will be collected through hoods and ducts by induced draft and controlled by

scrubber/dust collector.

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

• Control by having proper scrubbing system.

• Condenser to trap VOC.

• Enclosures to chemical storage area, collection of emission from loading of raw materials in

particular solvents through hoods and ducts by induced draft, and control by scrubber/dust

collector to be ensured.

• Nitrogen blanketing will be provided, besides special care needs to be taken for control in

respect of odorous chemicals.

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

seals etc.

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

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

pumps with mechanical seal.

• All Flange joints of the pipe lines which carry solvents will be covered with flange guards.

• All rotating equipments like pumps will be installed with mechanical seals to arrest any sort of

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Page 19 of 49

emissions.

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

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

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

• Solvent tank vents will be connected to vent chillers.

• Stand by pumps will be provided on all scrubbers. Besides, scrubbers are equipped with on-

line pH meter with hooter system for better operational control.

• Regular inspection of floating roof seals and proper preventive maintenance of roofs and

seals for tanks.

• Adequate ventilation will be provided.

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

i

Sr. no.

Type of Hazardous waste

Source of generation

Category and Schedule as per HW Rules.

Existing Quantity (MT/Annum)

Total Proposed Quantity (MT/Annum)

Disposal Method

1 ETP Sludge ETP SCH-I/35.3

120 120 Collection, Storage Transportation and disposal at GPCB approved TSDF site.

2 MEE Salt MEE SCH-I/35.3

36 00

3 Gypsum ETP SCH-I/26.1

500 500

4 Discarded Drums/bags

Raw Material

Storage& Handling

SCH-I/33.1

9.72 9.72 Decontaminate and

Reuse/ Sell to Scrap Vendor

5 Used / Spent Oil

Plant and Machineries

SCH-I/5.1 0.36 0.36 Collection, storage and used as lubricant within the premises / sell to MoEF approved Recycler/

Reprocessors

6 Dil. Sulfuric Acid

Process SCH-I/26.3

3420 3420 Collection, Storage and sell to end user who is having Rules -9 Permission.

Quantity of discarded containers must be in MT/Annum.


Company has membership of TSDF/CHWIF

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

There is no generating the non-hazardous waste.

G Solvent management& VOC emissions etc.

i Details of Solvent recovery (As per respective ToR) Company will not use the solvent to

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Page 20 of 49

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

manufacturing dye intermediates.


Company will not use the solvent to manufacturing dye intermediates.



Observation:

• Total water consumption will be 41 KLD. Total Industrial wastewater generation will be 12.75

KLD.After amendment 6.114 KLD will be treated by primary treatment and sent to CETP as per the

existing EC condition and remaining 6.636 KLD will be treated by primary treatment and sent to

common MEE of GECL-Sachin.

• Agro waste will be used as fuel for Additional thermo pack and hot air generator.

• MEE will be removed from EC and hence, the MEE salt will be NIL.

• PP has proposed to amend EC conditions as below:

Sr. no.

Condition no. in which changes proposed.

As per EC As per proposed amendment

Justification

1 A.2 (Point No. 16)

Concentrated stream wastewater shall be subjected to MEE (500 Liter/hour) & centrifuge within the factory premises.

Company has obtained the permission to send the treated neutralized effluent into Common MEE facility, M/s. GECL, Sachin for concentrated wastewater. So now Company proposes Effluent treatment Plant (Primary treatment) to neutralize the effluent then neutralized effluent will send the treated neutralized effluent into Common MEE facility, M/s. GECL, Sachin.

Operation cost of own MEE is higher than common MEE.


In case of waste water treated with in house MEE, Condensate (5 KL/Day) will be reused for process and fresh water requirement shall not exceed 35 KL/Day in that case.

Company has obtained the permission to send the treated neutralized effluent into Common MEE facility, M/s. GECL, Sachin for concentrated wastewater. So now Company proposes Effluent treatment Plant (Primary treatment) to neutralize the effluent then neutralized effluent will send the treated

Operation cost of own MEE is higher than common MEE.

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Page 21 of 49

neutralized effluent into Common MEE facility, M/s. GECL, Sachin.


• Committee deliberated that existing CETP discharge will be continue as per existing EC and

additional quantity will be sent to common MEE instead of in-house MEE.

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

after satisfactory submission of the following:

1. Treatability and feasibility of the treated wastewater to be discharged to the common MEE.

2. Compliance status of Common MEE facility of M/s: GECL, Sachin w.r.t. existing environmental

conditions. Details of total capacity, spare capacity, compliance of written instructions issued by

GPCB etc. shall be incorporated in compliance report.

9. SIA/GJ/IND2/22382/2017 M/s. CHITANYA LIFE SCIENCE PVT. LTD. Plot No. D2/CH/215, GIDC Industrial Estate, Dahej-2, Tal: Vagra, Dist: Bharuch-392130

EC Amendment


Project status: Amendment of EC

• SEIAA, Gujarat has accorded Environment Clearance to M/s. CHITANYA LIFE SCIENCE PVT.

LTD.vide letter no. SEIAA/GUJ/EC/5(f)/234/2017 Dated: 24/04/2017

• Now, project proponent has applied online vide proposal no. SIA/GJ/IND2/22382/2017dated

18/07/2018 for Amendment in EC.

• The existing product profile is as per existing EC as tabulated below:

Sr. No.


CAS no. /CI no.

Quantity MT/Month

End-use of products

1 Oxyclozanide 2247- 92-1

150

Treatment and control of gastrointestinal and lung worm

infections in domestic animals like Cattle, Sheep and Goats

2 Pyroxicam 36322- 90-4 Used in veterinary medicine to treat certain neoplasias expressing

cyclooxygenase (COX) receptors, such as bladder, colon and

prostatecancers

3 Tizanidine 64461- 82-1 Used as a muscle relaxant

4 PiperazineHexahydrate

142-63- 2 Anthelmintic

5 Piperazine Citrate 41372- 10-5 Pharma

6 PiperazineAdipate 41372- 10-5 Pharma

7 PiperazineDihydrochloride

110-85- 0 Pharma

8 PiperazinePhosphate

-- Pharma

9 Povidone Iodine 25655- 41-8 Topical antiseptic and anti-infective

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Page 22 of 49

10 Potassium Citrate 6100- 05-6 Alkalinizing agent and antiurolithic

11 Potassium Iodide 7681 -11-0 10 Antifungal, Expectorant and Iodinesupplement

12 Sodium Iodide 7681- 82-5 Expectorant and Iodine supplement

13 Carvedilol 72956- 09-03 0.1 Medicine

14 Olanzapine -- 0.4 Medicine

15 Ondansetron Hydrochloride

99614-01-4 Medicine

16 Pregabaline 148553 -50-8 Medicine

17 Amlodipine Besylate

111470 -99-6 Medicine

18 Glimipride 93479- 97-1 1.0 19 Lacidipine 103890 -78-4 Medicine

20 Venlafaxin Hydrochloride

99300- 78-4 Medicine

21 Losarton Potassium

124750 -99-8 Medicine

22 Lidocaine Hydrochloride

73-78-9 Medicine

23 Glibenclamide 10238- 21-8 7.5 Medicine 24 Niclosamide 50-65-7 Medicine

25 Metaxalone 1665- 48-1 Medicine 26 Benzarone 1477- 19-6 Medicine

27 Benzbromarone 3562- 84-3 Medicine

28 Ethenzamide 2869- 83-2 Medicine 29 Aceclofenac 89796- 99-6 Medicine

30 Pentaprazole Sodium

138786 -67-1 Medicine

Total 169.0




Sr. no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 4.5Crores

1. Capital cost for EMS (Environmental Management System):1.0 Crores

2. Recurring cost towards the environmental protection measures: 1.5 Crores per Annum.

B Total Plot area ( sq. meter) 4842.3 Sq. m. Green belt area,/Tree Plantation area ( sq. meter) 1600 Sq. m.


1. Direct 12

2. Indirect 25

Total 37

D Water

i


GIDC Water Supply


Company is obtained the permission for water supply from GIDC

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Page 23 of 49


Category

Water Consumption KLD

(A) Domestic 2.00

(B) Gardening 3.00

(C) Industrial

Process 22.50 Washing 2.00

Boiler 5.00 Cooling 6.50

Others Industrial Total 36.00

Total (A + B + C) 41.00



3) Total fresh water requirement:41.0 KLD


-

Category KLD

(A) Domestic 1.50

(B) Industrial

Process 18.5

Washing 1.50

Boiler 0.50

Cooling 1.00

Others

Total Industrial waste water 21.50

-

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

ETP – 25 KL/Day MEE – 20 KL/Day

v Mode of Disposal & Final meeting point Domestic: 1.5 KL/Day

Industrial: 21.50 KL/Day


Common facility – CETP

Membership of Common facility (CF) CETP vii Reuse/Recycle details (KLD) 0.00

E Air


-

SR. no.

Source of emission

With Capacity


Type of Fuel


Type of emissions

i.e. Air Pollutants


Measures (APCM)

1 Steam Boiler (3.0TPH)

Common Stack-20

Natural Gas/Agro waste

650SCM/Day/2.0M

T/Day

SPM SO2 Nox


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Page 24 of 49

2 Thermic Fluid Heater(1.0 Lac Kcal/Hr.)

Natural Gas/Agro waste

600SCM/Day/1.5 MT/Day


3 D.G. Set(50 KVA, Standby) 9 Diesel 10 Lit/Hr

SPM SO2 Nox

Adequate Stack Height

-

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

Sr. no.

Source of emission

Type of emission



1 Reactor - 1 HCl

SO2 12.0

WaterScrubber Followed by Alkali Scrubber

2 Reactor - 2 NH3 12.0 Two Stage Water

Scrubber

- iii Fugitive emission details with its mitigation measures.

As below:

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

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

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

and temperature.

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

be connected to vent chillers.

• Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer

area, will be collected through hoods and ducts by induced draft and controlled by

scrubber/dust collector.

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

• Control by having proper scrubbing system.

• Condenser to trap VOC.

• Enclosures to chemical storage area, collection of emission from loading of raw materials in

particular solvents through hoods and ducts by induced draft, and control by scrubber/dust

collector to be ensured.

• Nitrogen blanketing will be provided, besides special care needs to be taken for control in

respect of odorous chemicals.

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

seals etc.

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

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Page 25 of 49

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

pumps with mechanical seal.

• All Flange joints of the pipe lines which carry solvents will be covered with flange guards.

• All rotating equipments like pumps will be installed with mechanical seals to arrest any sort of

emissions.

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

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

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

• Solvent tank vents will be connected to vent chillers.

• Stand by pumps will be provided on all scrubbers. Besides, scrubbers are equipped with on-

line pH meter with hooter system for better operational control.

• Regular inspection of floating roof seals and proper preventive maintenance of roofs and

seals for tanks.

• Adequate ventilation will be provided.

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

i

Sr. no.

Type of Hazardous waste


Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Disposal Method

1 ETP Sludge ETP 35.3 24 Collection, Storage Transportation and disposal at GPCB approved TSDF site.

2 MEE Salt MEE 35.3 187.2

3 Inorganic Process

Waste

Process 28.1 142.5

4 Spent Carbon

Process 28.2 32.4 Collection, Storage Transportation and disposal at Cement industries for Co-Processing or CHWIF

site.

5 Organic process waste

Process 28.1 3

6 Distillation Residue

Distillation 20.3 351

7 Spent Solvent

Process 28.5 7420 Collection, Storage and Reuse within premises/sell to end user who is having Rules -9 Permission.

8 Discarded Drums/bags

Raw Material

Storage & Handling

33.1 9 Decontaminate and

Reuse/ Sell to Scrap Vendor

9 Used / Spent Oil

Plant and Machineries

5.1 0.6 Collection, storage and used as lubricant within the premises / sell to MoEF approved Recycler/Reprocessors

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Page 26 of 49

10

Sodium Bisulphite

Process & Scrubber

28.1 1620 Collection, Storage and sell to end user who is having Rules -9 Permission.

11 Phthalyl Hydrazine

Process 28.1 6

12 Liquor Ammonia (20%)

Process & Scrubber

28.1 630


Company has membership of TSDF/CHWIF

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

There is no generating the non-hazardous waste.

G Solvent management& VOC emissions etc.

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

• 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 95% 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.

• 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


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

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Page 27 of 49

• 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. • Two condenser will install with cooling water and chilled brine to recover the solvent. • Primary Condenser HE-01: Cooling Tower water or Chilled water 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



Observation:

• Total water consumption will be 41 KLD. Total Industrial wastewater generation will be 21.5 KLD.

After amendment will be treated by effluent treatment plant followed bysolvent stripper and MEE. The

treated effluent will be discharged through GIDC pipeline into the deep Sea.

• Unit has proposed amendment in EC conditions as below:

Sr. no.

Condition no. in which changes proposed.

As per EC As per proposed amendment

Justification


Final Treated effluent (30 KLD) shall be sent to RO for further treatment. RO

Company has obtained the permission to discharge the treated effluent into deep sea through GIDC pipeline,

Reuse of treated effluent is not suitable in pharma process due to

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Page 28 of 49

Permeate 21.1 KLD shall be reused in industrial activities and RO reject shall be sent to MEE.

So now Company proposes Effluent treatment Plant (Primary, Secondary and tertiary treatment), Solvent Stripper and MEE to treat the effluent then treated effluent will dispose off into deep sea through GIDC pipeline after achieving GPCB norms.

contamination.


Unit shall provide adequate ETP along with RO & MEE system for the treatment of industrial wastewater and to maintain Zero Liquid Discharge (ZLD).

Company has obtained the permission to discharge the treated effluent into deep sea through GIDC pipeline, So now Company proposes Effluent treatment Plant (Primary, Secondary and tertiary treatment), Solvent Stripper and MEE to treat the effluent then treated effluent will dispose off into deep sea through GIDC pipeline after achieving GPCB norms.

Reuse of treated effluent is not suitable in pharma process due to contamination.


• Committee deliberated that existing effluent will be treated in ETP followed by solvent stripper and

MEE as per existing EC and now the treated effluent will be discharge to deep Sea through GIDC

pipeline instead of recycle by RO system.



1. Detailed technical justification for proposed EC amendment in mode of disposal. Revised water

balance diagram considering proposed EC amendment.

2. Adequacy report of proposed ETP to achieve discharge norms for GIDC drainage prescribed by

GPCB. Stage wise characteristic shall be incorporated.

10. SIA/GJ/THE/21296/2017 M/s. Sumeet Industries Ltd. R.S. No. 289, 291, 292 & 304, 304/Plot No.1 & 304/Plot No.2, Village: Karanj, Tehsil: Mandvi, Dist.: Surat, Gujarat

Screening & Scoping

Project / Activity No.: 1(d)


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Page 29 of 49

• This office has received an application vide their online proposal no.SIA/GJ/THE/21296/2017dated

01/01/2018 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.

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

• This is an existing unit engaged in Captive Power Plant, yarn manufacturing and now proposes for

expansion for Captive Power plant as tabulated below:

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

2006.


• The project proponent along with their expert / consultant M/s. M/s. Aqua Air Environmental

Engineering Pvt. Ltd., Suratattended the meeting and made presentation before the committee.


Sr. no.

Particulars Details

A Total cost of Proposed Project Existing: 395.54

SR. NO.

PRODUCT EXISTING ADDIONAL TOTAL

PROPOSED END USE

1. Captive Power plant

Natural Gas Based (Stand By)K 1.0 MW X 1 Nos = 1.0 MW 1.5 MW X 1 Nos = 1.5 MW 2.0 MW X 2 Nos = 4.0 MW 2.0 MW X 1 Nos = 2.0 MW 4.3 MW X 2 Nos = 8.6 MW Furnace Oil Based (operational)K 4.8 MW X 1 Nos = 4.8 MW Total = 21.9 MW

Coal based CPP - 20.0

MW

24.8 MW (FO Based CPP – 4.8 MW + Coal based CPP – 20.0 MW). Company will discontinuous Natural gas base CPP (17.1 MW) after getting EC and CTE of Coal base CPP.

Electricity will be captive consumed.

2. PET Melt Chips 51700 MT/Year

- 51700 MT/Year 48300

MT/Year

Yarn Mfg.

3 Filament Yarn (POY & FDY)

48300 MT/Year

- Weaving Fabric

4 Menthol Products

60.0 MT/Year

-60.0 MT/Year

00 --

5 Waste Yarn 3.0 MT/Year

- 3.0 MT/Year

--

Total

100063 MT/Year & Natural gas base CPP -17.1 MW, FO

Based CPP – 4.8 MW

Coal based CPP - 20.0

MW & -60

MT/Year

100003 MT/Year & Coal based CPP - 20.0 MW, FO

Based CPP – 4.8 MW

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Page 30 of 49

(Rs. in Crores):

Proposed: 72.62 Total: 468.16

B Total Plot area ( sq. meter)

Existing: 35705.22 Sq. m. Proposed: 3556.50 Sq. m. Total: 39261.72 Sq. m.


Existing: 6125 Sq. m. Proposed: 1175 Sq. M. Total: 7300 Sq. m.

C Employment generation Existing: 660 Proposed: 05 Total: 655

D Water

i


Bore well

Status of permission from the concern authority. Permission under process.


Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

Remarks

(A) Domestic 15.0 - 15.0 (B) Gardening - 24.0 24.0

Industrial

Process - - -

Washing 7.0 - 7.0

Boiler 8.0 230.0 238.0 Cooling 93.0 157.0 250.0

Others - - - Industrial Total 108.0 387 495

Grand Total (A+B+C) 123.0 411.0 534.0



3) Total fresh water requirement: 272.0 KLD


Category Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

Remarks

(A) Domestic 8.0 - 8.0

Industrial

Process 36.0 - 36.0

Conc. Stream Allow in MEE

Washing 7.0 - 7.0 Dilute stream allow in ETP & RO.

Boiler 6.0 174.0 180.0

Cooling 41.0 4.0 45.0

Others - - -

Total Industrial waste water

90.0 178.0 268

-

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Page 31 of 49

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

MEE capacity-100 KLD ETP -I (Low COD & TDS) = 142 KLD ETP-II (High TDS) = 36 KLD

v Mode of Disposal & Final meeting point Domestic: Sock pit /septic tank

Industrial: Zero Liquid Discharge


Not Applicable

Membership of CF Not Applicable

vii Reuse/Recycle details (KLD) 262 KLD (RO permeate-182 KLD & MEE Condensate-80 KLD) will be reuse for cooling purpose.

E Air[Existing & Proposed]


-

SR. no.

Source of emission

With Capacity


Type of Fuel


Type of emissions

i.e. Air Pollutants

Air Pollution Control Measures

(APCM)

EXISTING

1 Coal fire TFH

(7500 U) 32

Coal 33

MT/day

PM

SO2

NOx

ESP

2 Steam Boiler

(1TPH) stand by 30

MCS + Teema Cyclone Separator

3 Gas fire TFH

(4000 U) X 2 Nos. 32

Natural Gas

15,000 SM3/day

-

4

Gas Generator Sets

[1.0 MW, 1.5MW, 2.0 MW x (2 Nos.)]

Total: 6.5 MW 18

(each GG Set)

CPP

Natural Gas

17.1 MW

80,000 SM3/day

-

-

5

Gas Generator Sets

[2.0 MW, 4.3MW, 2.0 MW x (2 Nos.)]

Total: 10.6 MW

-

6 4.8 MW Power

Plant(FO BASED) 30

Furnace Oil

22 M3/day

-

PROPOSED

1

Steam Boiler (85 TPH) for Coal

Based captive Power Plant

(20 MW)

80 Coal 400

MT/Day

PM SO2 NOx

Air Pre-heater, Economizer and

Electro Static Precipitator

-Note: Gas generator sets will be discontinues after getting EC and CTE of Coal based CPP.

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

- There is no Process Gas Emission

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

- Minimum joints & Flange

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Page 32 of 49

- Close process, Auto handling for charging material - Pumps with double mechanical seal, Proper ventilation Leak detection /checking - Regular maintenance & monitoring

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 generatio

n

Category and

Schedule as

per HW Rules.

Quantity (MT/Annum)

Disposal Method Existing

Proposed

Total

1 ETP

Sludge ETP plant 34.3 25 12 37

Collection, storage, transportation and disposal at TSDF site M/s. BEIL, Ankleshwar

2

Discarded

Containers

Raw Material Storage

33.3 3000

No./Year

- 3000

No./Year

Collection, storage decontamination and disposal by selling to registered re-refiners.

3 Used Oil

Machineries

&equipments

5.1 5000

Liter/Year

1000 Liter/Ye

ar

6000 Liter/Ye

ar

Collection, storage, transportation and

disposal by reuse or selling to registered refiners approved by

GPCB.

4 MEE Salt MEE plant

34.3 - 12

MT/Year

12 MT/Yea

r

Collection, storage, transportation and

disposal at TSDF site M/s. BEIL, Ankleshwar

NON HAZARDOUS

1 Fly Ash - - 55

MT/Year

55 MT/Yea

r

Bricks manufacturing plant within factory premises & sell to National Highway

Authority of India (NHAI) for road construction.

ii Membership details of TSDF, CHWIF etc. TSDF BEIL


Fly Ash = 55 MT/Year Mode of Disposal: Bricks manufacturing plant within factory premises & sell to National Highway Authority of India (NHAI) for road construction.

G Solvent management, VOC emissions etc. i Types of solvents, Details of Solvent recovery, %

recovery. reuse of recovered Solvents NA

ii VOC emission sources and its mitigation measures - Minimum joints & Flange - Close process - Proper ventilation - Leak detection /checking - Regular maintenance & monitoring

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Page 33 of 49

• Earlier the PP was called in SEAC Meeting dated: 08/03/2018. Technical presentation was made by

the project proponent. Technical presentation was made by the project proponent. Committee

observed that this project is for expansion in Captive Power plant, however, water balance and

management is submitted considering entire project. Committee was of the view that PP shall submit

all the details pertaining to Power plant only. Issues regarding compliance of existing unit, Coal

handling, source of water etc. have been discussed during the meeting. PP informed that they will

submit revised proposal with revised water balance and relevant details. Committee found that PP

has not covered important issues regarding impact on surrounding area due to proposed project in

proposed ToR. Looking to the poor presentation by environmental consultant, Committee defer the

proposal and decided to consider the case only after satisfactory submission of Revised

proposal with Revised Form & PFR.


• At present unit is engaged in manufacturing of yarn and fabric products with captive power plant for

which they have obtained EC &CC&A. The proposal is for expansion by addition of new 20 MW coal

based CPP.


Observation:

• This proposal is for expansion of existing unit and for now proposes a new CPP. This unit is having

validEC &CC&A for existing unit. Copy of EC, CC&A, CC&A compliance report is submitted. The

compliance of EC from regional office will be submitted during EIA. PP ensured that there are no

court cases pending and no public complaints against the project.

• Total water consumption will be 534 KLD. Total wastewater generation will be 268 KLD. Diluted

stream will be treated in ETP-1 followed by RO and concentrated stream will be evaporated in MEE.

RO permeate and MEE condensate will be reused for cooling purpose. Thus, unit will maintain

complete Zero Liquid Discharge.

• 85 TPH coal based boiler will be added for proposed CPP. Air pre heater, economizer and ESP will

be provided for the proposed boiler.



• Committee deliberate that EC compliance report submitted by PP was discussed, 3 points were

partially complied and 1 point is not complied. PP has committed to comply the condition.

• Committee noted that adequate Coal handling will be provided.


After deliberation, it was unanimously decided to recommend to SEIAA to grant for Terms of

Reference:

1. Executive summary of the project – giving a prima facie idea of the objectives of theproposal, use of

resources, justification, etc. In addition, it should provide a compilation of EIA report including EMP

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Page 34 of 49

and the post-project monitoring plan in brief.

2. Present land use pattern of the study area shall be given based on satellite imagery.

3. Geological features and geo-hydrological status of the study area.

4. Demarcationof proposed activities in lay out of the existing premises. Provision of continuous

unobstructed peripheral open path within the projectareafor unobstructed easy movement of the

emergency vehicle / fire tenders without reversing back. Mark the same in the plant layout.

5. Explore the possibilities for Air cooled condensers instead of Water cooled condensers in order to

reduce the raw water requirement.

6. Technical details of the proposedpowerplant along with details of strategyforimplementation reuse /

recycle and other cleanerproductionoptionsforreduction of wastes. Generation of waste gases and

utilization of waste heat have tobeset out.

7. Assessment of source of the water supply with adequacy of the same to meet with the

requirementsfor the project. Copy of letter of permission obtained from the concerned authority

forsupply of additional raw water for the proposed activities.

8. Action plan for complete ZLD for existing as well as proposed CPP.

9. Application wise break-up of treated effluent quantity to be recycled / reused in various applications

like cooling purpose etc.

10. Detailed water balance (including reuse-recycle, if any) along with qualitative and quantitativeanalysis

of each wastestreamtobe generated from all sources including Boilers, Cooling Towers, process,

washing etc. Details of methods to be adopted for the water conservation.

11. Details of the treatment facilities proposed for the effluent to be generated from the power plant

including existing project. Details of the ETP units including its capacity (KL/day), size of each unit,

retention time and other technical parameters and details about up-gradation in the existing ETP (if

any proposed) to take care of the wastewater to be generated from the proposed activities.

12. Characteristics of untreated and treated wastewater. A detailedeffluenttreatability study vis-à-vis the

adequacy and efficacy of the treatment facilities proposed for the wastewater tobe generated along

with adequacy and efficacy report. The characteristic on which treatability is based shall also be

stated.

13. Site-specific meteorological data including temperature, relative humidity, hourly wind speed and

directionand rainfall shall be provided.

14. Anticipated environmental impacts due to the proposed project/production may be evaluated for

significance and based on corresponding likely impacts VECs (Valued Environmental Components)

may be identified. Baseline studies may be conducted within the study area of 10 km for all the

concerned/identified VECs and likely impacts will have to be assessed for their magnitude in order to

identify mitigation measures.

15. One complete season base line ambient air quality data (except monsoon) to be given along with the

dates of monitoring. The parameters to be covered shall be in accordance with the revised National

Ambient Air Quality Standards as well as project specific parameters. Locations of the monitoring

stations should be so decided so as to take into consideration the pre-dominant downwind direction,

population zone and sensitive receptors. There should be at least one monitoring station in the

upwind direction. There should be at least one monitoring station in the pre dominant downwind

direction at a location where maximum ground level concentration is likely to occur.

16. Impact of the project on the AAQ of the area. Details of the model used and the input parameters

used for modeling should be provided. The air quality contours may be plotted on a location map

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Page 35 of 49

showing the location of project site, habitation, sensitive receptors, if any. The wind roses should

also be shown on this map. Air quality modeling to be carried out considering the partial and

complete failure of the ESP.

17. Quantity of the fuel requirement, its source and transportation, storage, handling and management

along with the environmental management to beadoptedfor this. Fuel analysis to be provided

(sulphur, ash content and heavy metals including Pb, Cr, As and Hg).

18. A confirmed fuel linkage along with the supportive documents of long term supply of coal for the

project requirements should be provided.

19. Specific details of (i) Details of the utilities required (ii) Quantity and characteristics of each fuel along

with analysisreport and its source (iii) Flue gas emission ratefrom each utility (iv) Air PollutionControl

Measures proposedto each of the utility along with its adequacy.

20. Technical details of ESP proposedtobeinstalled as air pollutioncontrolsystem along with its adequacy,

details of its operational controls with DCS, system for online monitoring of the pollutants from the

stacketc. Details of provisions to be kept in ESP to ensure that in any casethe air emission does not

cross the GPCB norms including provision of standby field in the ESP, preventive maintenance,

failure / tripping control system, guaranteefrom the ESP supplier, alternative arrangements in case of

the failure / tripping of the ESP etc. ESP should be designed to achieve GPCB norms at the outlet.

21. List of all the sources of fugitive emission. Detailedplanforprevention and control of fugitive emission /

dusting at each and every stage of fuel handling including unloading / loading at port,

transportationfrom port toplant, unloading / loading / stacking / conveyance / transfer at plant etc.

Detailed specifications and schematicdiagram of water sprinkling system including number of

sprinklers to be installed, pipe diameter and nozzle diameter of the sprinklers, quantity of water to be

consumed by sprinklers etc.

22. Impact on localtransportation infrastructuredueto the project such as transportation of fuel, ash etc.

Base line status of the existing traffic, projected increase in truck traffic as a result of the project in the

present road network, impact on it due to the project activities, carrying capacity of the existing roads

and whether it is capable of handling the increased load. Arrangement for improving the infrastructure

like road etc. if any should be covered. Whether any additional infrastructure would need to be

constructed and the agency responsible for the same with time frame.

23. Details and time bound program for installation of online monitoring system in the existing as well as

proposed plants for monitoring of the pollutants from the stacks and process vents with a

softwareand an arrangement to reflect the online monitored data on the company's server, which can

be accessed by the GPCB on real time basis.

24. Provision of Continuous Ambient Air Quality Monitoring Station [CAAQMS] within premises, with an

arrangement to reflect monitored data on the company’s server, which can be accessed by the

GPCB on real time basis.

25. Details of measures proposed for the noise pollution abatement and its monitoring.

26. Details of management of the hazardous wastes tobe generated from the project stating detail of

storageareafor each type of waste, its handling, its utilization and disposal etc. How the manual

handling of the hazardous wastes will be minimized.

27. Detailed plan of ash evacuation, handling, storage and utilization should be provided. Undertaking

stating that ash pond shall not be constructed and it shall be stored in closed silos only should be

incorporated.

28. Details of seismic design aspects to be adhered to in the project.

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Page 36 of 49

29. Technical details of conveyor belts and mitigation measures toensure that there will be no dust

emission from conveyor belts.

30. Details of proposed disposal of solid wastes that may generate due to spillage of materials.

31. Specific safety measures proposed at storage yard / warehouse and conveyor belts.

32. Details of firefighting system including provision for flame detectors, temperature actuated heat

detectors with alarms, automatic sprinkler system, location of fire water tanks & capacity, separate

power system for firefighting, details of qualified and trained fire personnel& their job specifications,

nearest fire station&timerequired to reach the proposed site. Submitlinediagram of the fire hydrant

network.

33. Copy of membership certificate of Common Environmental Infrastructure like TSDF, if any taken,

should be incorporated.

34. Details of 100% fly ash utilization plan as per latest fly ash Utilization. Notification of GOI along with

firm agreements / MoU with contracting parties including other usages etc. shall be submitted. The

plan shall also include disposal method / mechanism of bottom ash.

35. A detailed EMP including the protection and mitigation measures for impact on human health and

environment as well as detailed monitoring plan and environmental management shall proposed for

implementation and monitoring of EMP. The EMP should also include the concept of waste-

minimization, recycle/reuse/recover techniques, energy conservation, and natural resource

conservation. Total capital cost and recurring cost/annum earmarkedforenvironmentpollution control

measures.

36. Occupational health impacts on the workers and mitigation measures proposed to avoid the human

health hazards along with the personal protective equipment to be provided to the workers. Provision

of industrial hygienist and monitoring of the occupational injury to workers aswell as impact on the

workers. Plan forperiodicmedical checkup of the workers exposed. Details of work zone ambient air

quality monitoring plan as per Gujarat Factories Rules.

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

scenario related to fire and explosion issues due to storage and use of fuel should be carried out.

The worst-case scenario should take into account the maximum inventory of storage at site at any

point in time. The risk contours should be plotted on the plant layout map clearly showing which of

the activities would be affected in case of an accident taking place. Based on the same, proposed

safeguard measures including On-Site / Off-Site emergency plan should be provided. Measures to

guard against fire hazards including details of automatic fire detection and controlsystem&detailed

fire control plan showing hydrant pipeline network, provision of DG Sets, fire pumps, jockey pump,

toxic gas detectors etc. should also be provided.

38. Provisions for water supply, fuel (kerosene or cooking gas), lighting, sanitation etc. to the construction

work force so as to avoid felling of trees/mangroves and pollution of water and the surroundings.

Details of personal protective equipments to be provided to construction workers at the site.

39. Submit checklist in the form of Do’s & Don’ts of preventive maintenance, strengthening of HSE,

manufacturing utility staff for safety related measures.

40. Public hearing shall be carried out as per the MoEFCC’s OM dated 04/04/2016. A tabular chart for

the issues raised and addressed during public hearing/consultation and commitment of the project

proponent on the same should be provided. An actionplanto address the issues raised during public

hearing and the necessary allocation of funds for the same should be provided.

41. Detailed five year greenbelt development program including annual budget, types &number of trees

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Page 37 of 49

to be planted, area under green belt development [with map], budgetary outlay; along with

commitment of the management to carry out the tree plantation activities outside the premises at

appropriate places in the nearby areas and elsewhere.

42. Proposal for socio-economic development activities including community welfare program most

useful in the projectareafor the overallimprovement of the environment. Submit a detailed plan for

social corporate responsibilities, with appropriate budgetary provisions for the next five years and

activities proposed to be carried out; specific to the current demographic status of the area.

43. Plan forcompliance of the EP Rules and CREP guidelinesfor the proposedpower plant.

44. Compliance status of the existing unit with respect to various conditions given in the Environmental

Clearance and CC&A orders obtained for the existing plants.

45. Records of any legal breach of Environmental laws i.e. details of show- cause notices, closure

notices etc. served by the GPCB to the existing unit in last three years and actions taken then after

for prevention of pollution.

46. Copy of Environmental Clearance obtained for the existing project and a certified report of the status

of compliance of the conditions stipulated in the environmental clearance for the existing operation of

the project by the Regional Office of the MoEF&CC.

47. Details of fatal / non-fatal accidents, loss of life or man hours, if any, occurred in the existing unit in

last three years and measures proposed to be taken for avoiding reoccurrence of such accidents in

future.

48. Any litigation pending against the project and / or any direction / order passed by any Court of Law

against the project, if so, details thereof.

49. Does the company have a well laid down Environment Policy approved by its Board of Directors? If

so, it may be detailed in the EIA report. Does the Environment Policy prescribe for standard operating

process / procedures to bring into focus any infringement / deviation / violation of the environmental

or forest norms / conditions? If so, it may be detailed in the EIA.

50. What is the hierarchical system or administrative order of the company to deal with the environmental

issues and for ensuring compliance with the EC conditions. Details of this system may be given.

51. Does the company have a system of reporting of non-compliances / violations of environmental

norms to the Board of Directors of the company and / or shareholders or stakeholders at large? This

reporting mechanism should be detailed in the EIA Report.

52. Certificate of accreditation issued by the NABET, QCI to the environmental consultant should be

incorporated in the EIA Report.

53. An undertaking by the Project Proponent on the ownership of the EIA report as per the MoEF&CC

OM dated 05/10/2011 and an undertaking by the Consultant regarding the prescribed TORs have

been complied with and the data submitted is factually correct as per the MoEF&CC OM dated

04/08/2009.

54. All documents to be properly referenced with index and continuous page numbering.

55. A tabular chart for the issues raised and addressed during public hearing/consultation and

commitment of the project proponent on the same should be provided. An action plan to address the

issues raised during public hearing and the necessary allocation of funds for the same should be

provided.

56. A tabular chart with index for point-wise compliance of above.

The above mentioned project specific TORs/additional TORs and the model TORs available in the

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MoEFCC’s sector specific EIA Manual for ‘Thermal Power Plants’ 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 draft EIA report shall be submitted to the Gujarat Pollution Control Board for conducting the

public consultation process as per the provisions of 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.

Validity of ToR:

• The ToRs prescribed for the project will be valid for a period of three years for submission of

EIA & EMP report. ToR will lapse after three years from the date of issue.

• The period of validity could be extended for a maximum period of one year provided an

application is made by the applicant to the Regulatory Authority, at least three months before

the expiry of valid period together with an updated Form-I, based on proper justification and

also recommendation of the SEAC.

•

11. SIA/GJ/IND2/18911/2017 M/s. JembyChem Limited. Plot No. C-1/335, 336,337, GIDC Estate, Phase-II, Vatva, Ahmedabad

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/18911/2017dated 10/11/2017 for obtaining


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

30/04/2017.

• Project proponent has submitted EIA Report prepared by M/s: SanEnvirotech Pvt. Ltd., Ahmedabad;

based on the TOR issued by SEIAA.

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

tabulated below:

Sr. no.


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

1 Sulpho Tobias Acid 171570-11-9 2 23 25

2 J-Acid 87-02-5 2.528 47.472 50

3 J-Acid derivatives 12.67 87.33 100

1. N-Acetyl J-Acid 6334-97-0 2. N-Methyl J-Acid 22346-43-6

3. N-Benzoyl J-Acid 132-87-6 4. N-Phenyl J-Acid 119-40-4

4 RW-Acid (Di-J Acid) 87-03-6 10 10

5 Sulpho J- Acid 6535-70-2 10 10

6 N-Methyl Gamma Acid

6259-53-9 00 05 05

Total 17.198 182.802 200


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Page 39 of 49



Sr. no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing: 2.5 Crores Proposed: 1.5 Crores Total: 4.0 Crores

(3) Capital cost for EMS (Environmental Management System): 0.4 Crores

(4) Recurring cost towards the environmental protection measures: 0.5 Crores per Annum.

B Total Plot area ( sq. meter)

Existing: 2212.0 Sq. m. Proposed: --- Sq. m. Total: 2212.0 Sq. m.

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

Existing: 200 Sq. m. Proposed: 415 Sq. m. Total: 615 Sq. m.


3. Direct Existing: 40 Proposed: 15 Total: 55

4. Indirect Existing: Proposed: Total:

D Water

I

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

GIDC water supply

Status of permission from the concern authority. Permission obtained from GIDC. ii Water consumption (KLD)

Existing KLD

Proposed (Additional)

KLD

Total after Expansion

KLD

Remarks

(A) Domestic 2.5 2.5 5.0

(B) Gardening 1.0 4.0 5.0

Industrial Process 19.0 26.0 45.0

Washing 1.5 18.5 20.0 Boiler 1.0 9.0 10.0

Cooling 9.0 6.0 15.0 Others -- 5.0 5.0

Industrial Total 30.5 64.5 95.0

Grand Total (A+B+C) 34.0 71.0 105.0

1) Total water requirement for the project: 105 KLD

2) Quantity to be recycle: ---

3) Total fresh water requirement: 105 KLD


Category Existing KLD

Proposed (Additional)

KLD

Total after Expansion

KLD

Remarks

(A) Domestic 2.0 1.0 3.0

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Page 40 of 49

Industrial

Process 16.0 52.0 68.0

Washing 15.0 5.0 20.0 Boiler 0.5 0.5 1.0

Cooling 0.5 4.5 5.0 Others (water

treatment) -- 5.0 5.0

Total Industrial waste water

32.0 67.0 99.0

Total (A+B) 34.0 68.0 102.0

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

[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. ETP1 (Dilute stream): 50 m3/day having primary & tertiary treatment units.

ETP2 (Concentrated stream): 100 m3/day having primary treatment units.


Domestic: Soak pit

Industrial: 24.0 KLD Dilute Sulphuric Acid will be sent to Novel Spent Acid Management, Vatva for reuse by actual users or for treatment; 68.0 KLD after primary treatment will be sent for common MEE/evaporator/spray dryer to avoid load on CETP; 31.0 KLD dilute effluent from washing and utilities will be treated in ETP and after achieving CETP inlet norms sent to CETP-GESCSL, Vatva for further treatment and final disposal.

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

CETP: GESCSL, Vatva Common MEE/evaporator/ spray dryer

• Sanand Eco Project Ltd.,Sanand

• GESCSL, Vatva

• Society for Clean Earth, Vatva

• Society for Clean and Green Environment., Naroda Novel Spent Acid Management, Vatva

Membership of Common facility (CF)

Attached as Annexure-V of EIA report.

vii Reuse/Recycle details (KLD)

--

E Air [Existing & Proposed]

I Flue gas emission details


Existing & Proposed

-

Sr.

no.

Source of emission

With Capacity e.g. Boiler (8

TPH)

Stack Heigh

t (mete

r)

Type of fuel

Quantity of Fuel

MT/Day

Type of emissions i.e. Air Pollutants


Measures (APCM)

Existing

1. Steam Boiler* (0.6 TPH)

15 Bio fuel 2.0 MT/da

SPM SO2

--

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Page 41 of 49

y NOx

2. Thermic Fluid Heater* (4.0 lakhs kcal/hr.)

15 Bio fuel SPM SO2 NOx

--

3. D G set (125 kVA)

11 Diesel 30 lit/hr.

Proposed scenario after expansion

1. Steam Boiler (1.0 TPH)

15 Bio fuel (Briquett

e)

4 MT/da

y

SPM SO2 NOx

Cyclone separator

2. Thermic Fluid Heater (10.0 lakhs kcal/hr.)

15 Bio fuel (Briquett

e)

6.5 MT/da

y

Multi Cyclone separator

3 D G set (125 kVA)

11 Diesel 30 lit/hr

Adequate stack height

* Existing boiler & TFH with capacity of 0.6 TPH &4.0 lakhs kcal/hr. will be dismantled after expansion and unit will install boiler of 1 TPH and TFH of 10.0 lakhs kcal/hr.

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

-

Sr. no.

Source of

emission

Type of emission



Existing

1 Reaction Vessels

SO2<40 mg/Nm3 15 Alkali Scrubber (Ventury + Packed column)

Proposed Addition

1 Reaction Vessels

SO2<40 mg/Nm3

15 Alkali Scrubber (Ventury + Packed column)

-

Iii Fugitive emission details with its mitigation measures. As below

To control fugitive emission, following steps will be implemented:

• Entire process will be carried out in closed reactors.

• Pneumatically transfer of liquid raw material in rector.

• Raw material will be stored in the covered structure.

• Regular maintenance of valves, pipes etc.

• PPEs will be provided to the workers.

• Frequent work area monitoring will be done ensure fugitive emissions level.

• Greenbelt will be developed around the plant to arrest the fugitive 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 waste

Source of

generation

Category and

Schedule as

per HW Rules

Quantity (MT/Annum)

Disposal Method

Existing Propose

d

Total

1 ETP ETP 35.3 40 250 290 Sold to cement

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Page 42 of 49

sludge MT/month

MT/month

MT/month

manufacturer or Disposal to TSDF site.

2 Discarded containers/ barrels/ liners

RM storage

and packaging area

33.1 12 nos./mo

nth Liner-8 kg/mont

h

30 nos./mo

nth Liner-50 kg/mont

h

42 nos./mo

nth Liner-58 kg/mont

h

Being used for packing of ETP sludge in case of excess it will be sold to approved recyclers.

3 Used Lubricating Oil

D.G. set,

machinery

5.1 200 Lt/yr.

200 Lt/yr.

400 Lt/yr.

It will be sold to approve recycler with CPCB.

4 Spent Sulphuric Acid (24%-65%)

Process 26.3 -- 1222 Kl/month

1222 Kl/mont

h

Collection, storage and partial reuse in-house and balance qty. sent to Novel spent management or actual users under Rule-9 of Haz. rules, 2016

5 Sodium Bi Sulfite (40-45%)

Process B(15) 45 Kl/month

345 Kl/month

390 Kl/mont

h

Collection, storage and reuse in-house


TSDF-

• Ecocare Infrastructure Pvt. Ltd., Ghaspur, Dist. Surendranagar,

• Cluster EnviroPvt. Ltd., Matar, Dist. Kheda

• MauryaEnviroProject Pvt. Ltd., Jamiyatpura, Dist. Mahisagar


Existing: 6 MT/month After expansion: 18 MT/month (sold to brick manufacturer also use for land levelling, conditioning & road construction)


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

• No use of any solvent.


• No sources of VOC emission

• During the meeting dated 25/05/2018, technical presentation made during the meeting by project

proponent.

• Technical presentation was made by the project proponent. Committee observed that water balance,

spent acid generation and its management is not addressed properly in EIA report as well as

presentation.

After deliberation, Committee decided to consider the proposal for appraisal only after satisfactory

submission of revised EIA report with proper water balance, sound spent acid management

considering as hazardous waste, cleaner production technology, area adequacy with green belt area

etc.

Observation:

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Page 43 of 49

• This is existing unit manufacturing organic chemical and now proposes for synthetic organic chemical

manufacturing plant. Unit has valid CC&A for existing unit. The CC&A Compliance was discussed in

detail. There is no court case/legal action pending against the unit.

• Committee deliberate that Total water requirement will be only 105 KLD and total wastewater

generation will be 99 KLD. 31 KLD of dilute wastewater will be treated in ETP 1 and sent to CETP. 68

KLD of concentrated stream will be treated in ETP 2 and sent to common MEE/evaporator/spray

dryer.

• 24 KLD of dilute Sulfuric acid will be sent to NOVEL.

• Biofuel will be used after expansion for steam boiler and thermic fluid heater.

• Hazardous waste management will be mentioned adequately.



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

to May 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NO2, 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. The modelling study proved that the air emissions

from the proposed plant would not affect the ambient air quality of the region in any significant

manner. The ambient air quality around the proposed project site will remain within the National

Ambient Air Quality Standards (NAAQS). The result of water samples are within the norms

prescribed in BIS.





• Committee deliberated that PP has submitted EIA report with proper water balance, sound spent acid

management considering hazardous waste, best technology available for waste reduction.

• Committee noted that Higher quantity of industrial wastewater generation will be due to use ofIce and

water retain with products. Main sources of industrial wastewatergeneration will be process, washing

and utilities. Entire quantity of theindustrial wastewater will be segregated.

• Unit has full-fledge ETP with capacity of 50 m3/day for dilute stream and100 m3/day for concentrated

stream. After expansion, unit will treat itseffluent in same ETP.

• Hydraulic or organic load onCETP will not increase resulted to proposed expansion. Concentrated

frommanufacturing activities willbe evaporated and only dilutestream will be sent to CETPafter

treatment. No additional discharge envisages.

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Page 44 of 49

• PP has acquired a new land to provide greenbelt area.

After deliberation, it was unanimously decided to recommend to SEIAA for grant of environment

clearance.

12. SIA/GJ/IND2/18298/2017 M/s.Intersperse Industries Plot No C-1-7,67/16, Phase-I, GIDC, Vatva, Ahmedabad, Gujarat 382445

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/20847/2017 dated 10/11/2017 for

obtaining Environmental Clearance.

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

29/04/2017.

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

the TOR issued by SEIAA.

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

tabulated below:

Sr. no.

Name of the Products CAS no. / CI no.

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

proposed

1 Para Amino Acetanilide 122-80-5 2.00 MT/Month

13.00 MT/Month

15.00 MT/Month

Dyes Drugs

2 2 Chloro PPD - 2.0 MT/Month

6.0 MT/Month

8.0 MT/Month Pigment

3 Carbazole 86-74-8 2.5 MT/Month

7.5 MT/Month

10.0 MT/Month

Pigment

4 N-Ethyl Carbazole 86-28-2 - 5.00 MT/Month

5.00 MT/Month

Pigment

5 2 Amino Di Methyl Terephthalate (ADMT)

5372-81-6 - 10.00 MT/Month

10.00 MT/Month

Pigment

6 2,5-Di Chloro PPD (2,5 DCPPD )

20103-09-7 - 5.00 MT/Month

5.00 MT/Month

Pigment

7 Meta Amino Acetanilide HCL ( MAA )

621-35-2 - 3.00 MT/Month

3.00 MT/Month

Dyes

TOTAL 6.5 MT/Month

42.5 MT/Month

49.0 MT/Month

-



• Salient features of the project are as under::

Sr. no.

Particulars Details

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

Existing:Rs.1.0 Crores Proposed: Rs. 0.48 Crores Total: Rs.1.418 Crores

(1) Capital cost for EMS (Environmental Management System): Rs. 0.10Crores (2) Recurring cost towards the environmental protection measures: Rs. 0.20 Crores per

Annum. B Total Plot area

( sq. meter) Existing:2000 Proposed:- Total:2000


Existing:- Proposed:600 Total:600


1. Direct Existing:10 Proposed:5 Total:15

2. Indirect Existing:15 Proposed:10 Total:25

D Water

i

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

GIDC

Status of permission from the concern authority. GIDC Letter ii Water consumption (KL/day)

Existing KL/day

Proposed (Additional) KL/day

Total after Expansion KL/day

(A) Domestic 1.1 - 1.1

(B) Gardening - 0.4 0.4

(C) Industrial

Process 2.0 14.1 16.1 Washing 2.0 1.0 3.0

Boiler 2.0 - 2.0

Cooling 2.3 - 2.3

Others - - -

Industrial Total 8.3 15.1 23.4

Grand Total (A+B+C) 9.4 15.5 24.9

iii Waste water generation (KL/day)

Category Existing KL/Day

Proposed (Additional) KL/day

Total after Expansion KL/day

(A) Domestic 1.1 0.25 1.35

(B) Industrial

Process 1.7 13.35 15.05 Washing 2.0 1.0 3.0

Boiler - - -

Cooling 0.3 - 0.3

Others - - -

Total Industrial waste water 4.0 14.35 18.35

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

ETP In house Capacity:20 KL/day


Domestic: Soak Pit

Industrial Diluted: CETP,Vatva (Existing), Common Spray Drying Facility, Vatva for proposed

Vi Reuse/Recycle details (KL/day) 5 KL/day

Vii Details of rain water harvesting ETP In house &Common Effluent Treatment Plant , Vatva, Ahmedabad

E Air[Existing & Proposed]

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

-

SR. no.

Source of emission With Capacity e.g. Boiler (8 TPH)


Name of the fuel

Quantity of Fuel MT/hr& MT/Day

Type of emissions i.e. Air Pollut ants

APCM

1. Steam Boiler (1.0 Ton)

11

Fire wood /Agro waste

6.0 MT/Day

PM SO2 NO2

Multi Cyclone

2. Hot Air Generator (2 Lac Kcal)

11 LDO

500 Lit/Month

PM SO2 NO2

Multi Cyclone

3 DG set - Diesal

5 Lit/ Hr

PM SO2 NO2

-

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

-

Sr. no.

Source of emission

Type of emission


APCM Emission Standards

There are no process gas emissions.

- Iii Fugitive emission details with its mitigation measures.

[Existing & Proposed]

• Fugitive emission will due to the leakages in pump, storage container, material transferring, and packing.

Mitigation measures:

• Proper storage of raw materials, products and fuels

• Ensuring closed feeding and sampling.

• Establishing SOPs for start-up, shut down and maintenance operational procedure Regular work place and ambient air quality monitoring will be done.

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

I

Sr. no.

Type/ Name of


Category and

Quantity(MT/Annum) Disposal Method Existing Propos After

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Page 47 of 49

Hazardous waste

Schedule as per HW Rules.

ed Proposed

1 ETP Waste

Treatment of Effluent

34.3 180 300 480 Collection, Storage, Transportation, Disposal at TSDF approved by the board

2

Process Waste

Filtration 26.1 79.2

280.8 360

Collection, Storage, Transportation, Disposal at TSDF approved by the board

3 Discarded Container

Packing 33.3

1.5

2.5

3.5

Collection, Storage, Decontamination, Transportation, Disposal by selling to authorized recycler or send back to supplier

4 Used Oil Machinery 5.1 - 0.5 0.5

Collection, Storage, Transportation, Disposal by selling to Registered re-refiners

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

CETP for discharge of treated waste water, SEPPL for TSDF, Common Spray Dryer Facilities of GESCSL, Vatva

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

AMC collection centre

G Solvent management (If any)

i Details of Solvent recovery (As per respective ToR)

Not any


VOC source:

• Liquid material storage area

• Production area VOC mitigation measures

• Store VOC-containing products in air-tight containers.

• Buy products with less packaging as the printing of packaging materials generates VOCs

• Will assign a person develop and implement the VOC reduction plan.

• Utilizing natural ventilation Maintaining the good housekeeping practice.

• During the meeting dated 28/02/2018, technical presentation made during the meeting by project

proponent.

• For the above referred proposal, Consultant of the project requested to defer the proposal as project

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Page 48 of 49

proponent could not come due to illness which was agreed upon.

• Committee insisted PP and consultant to be well aware of the proposal. After deliberation, it

was decided by the committee to defer the proposal in one of the upcoming SEAC meeting.

Observation:

• This is existingunit manufacturing organic chemical and now proposes for synthetic organic chemical

manufacturing plant. Unit has valid CC&A for existing unit. The CC&A Compliance was discussed in

detail. There is no court case/legal action pending against the unit.

• Total water consumption will be 24.9 KLD. Total wastewater generation will be 18.35 KLD it will be

treated in ETP. Existing 4 KLD discharge to the CETP will be continue and additional 14.35 KLD will

be sent to the common spray drying facility.

• Firewood or agrowaste will be used as fuel for boiler.

• There will be no process gas emission.




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

to June 2017. Ambient Air Quality monitoring was carried out for PM10, PM2.5, SO2, NO2, and VOC

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

Air Quality. The incremental Ground Level Concentration (GLC) has been computed using AIRMOD

view. The resultant concentrations are within the NAAQS. The modelling study proved that the air

emissions from the proposed plant would not affect the ambient air quality of the region in any

significant manner. The ambient air quality around the proposed project site will remain within the

National Ambient Air Quality Standards (NAAQS).


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



• The purpose of proposal was discussed. Unit has got closure in December 2017 for installation of

boiler without CTE-amendment. Then after PP has got CTE-amendment for the same.

• Committee noted that the best available technology has been used for the project.

• Committee asked PP for management of Hazardous waste as per the HW Rules 2016. Waste nickel

is generated from the mfg. process of Carbazol which is not mentioned in hazardous waste

management.


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1. Management of waste Nickel as per the HW Rules 2016. Revised HW management shall be required

to submit.

2. Detailed outlay of Environmental Management Plan with year-wise budgetary provision including

bifurcation of each activity with provision of capital cost and recurring cost. Tree plantation activity

shall be considered precisely.

3. Details of the treatability and feasibility of waste water to be disposed of by means of spray dryer and

its impact on Environment and Human Health. Submit Adequacy of Spray Dryer.

Meeting ended with thanks to the Chair and the Members.

Minutes approved by:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

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

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

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

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