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383rdmeeting of SEAC-Gujarat, Dated 15.03.2018

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Minutes of the 383rdmeeting of the State Level Expert Appraisal Committee held on 15/03/2018

at Geer Foundation,Indroda Park, Sector – 9, Gandhinagar.

The 383rdmeeting of the State Level Expert Appraisal Committee (SEAC) was held on 15thMarch,

2018at Geer Foundation, Indroda Park, Sector – 9, Gandhinagar. Following members attended the

meeting:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

4. Shri Rajesh I. Shah, Member, SEAC

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

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

7. Dr. Mayuri Pandya, Member, SEAC

The agenda of Category 8 (a)cases was taken up. Five [5] cases of Category 8 (a) were taken up.

The applicants made presentations on the activities to be carried out along with other details

furnished in the Form-1, Form-1A and conceptual plan.

1. Shree Siddhivinayak Residency (Shree Krishna Enterprise)

Chala Vapi, R.S. No. 488/1, Moje: Chala, Vapi, Valsad

Screening, Scoping & Appraisal

Details of the proposed project as presented before the committee are described below:

Sr. No.

Particulars Details

1. Proposal is for New Project [SIA/GJ/NCP/72071/2018]

2. Type of Project Residential & Commercial Project

3. Project / Activity No. [8(a) or 8(b)]

8 (a)

4. Name of the project

Shree Siddhivinayak Residency

5. Name of Developer

Shree Krishna Enterprise

6. Estimated Project Cost (Rs. In Crores)

27.70 crore

7. Whether construction work has been initiated at site?

No

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If yes, details thereof

8. Project Details • Land / Plot Area (m2): 7,236.0

• FSI area (m2):17,071.64

• Total BUA (m2):21,692.48

Permissible Proposed

FSI Area (m2) 17,366.40 17,071.64

Ground Coverage (m2) 2,683.67 2,683.67

Common Plot Area (m2) 723.60 725.0

Max. building height (m) --- 23.20

9. Building Details • No. of Buildings:7

• No. of Blocks:7

• Scope of buildings/blocks: Hollow plinth + 7 floors

• No.& size of Residential Units: 357 Flats

• No. & type of Commercial Units:3 shops

• Details of amenities if any: No

10. No. of expected residents / users

1607 occupants from flats and 6 from shops, 50 visitors

11. Water & waste water details during construction phase

• Water requirement (KL/day): 16.25

• Source of water: Water tankers

• Waste water generation quantity (KL/day): 10.53

• Mode of disposal: Septic tank &soak pit

• Details of reuse of water, if any: 4.0 KLD for curing

12. Water & waste water details during operation phase

• Fresh water requirement (KL/day):221.0

• Source of water: Water supply from VapiNagarpalika

• Waste water generation quantity (KL/day):186.0

• Mode of disposal: into drainage line of VapiNagarpalika

13. Status of water supply and drainage line

Available at site

14. Solid waste Management

Construction Phase:

Generation (m3)

Quantity to be reused (m3)

Mode of Disposal / Reuse

Top Soil 700 700 Reuse for greenbelt development.

Other excavated earth

- -

Construction debris

225 215 m3 will be reused within the premises.

Balance debris will be handed over to NagarPalika

Steel scrap 5 0 Sold to vendors

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Discarded packing materials

4 0 Sold to vendors

Operation Phase:

Type of waste

Generation Quantity (Kg/day)

Mode of waste collection


Dry waste 385 White bins Sold to vendors

Wet waste 580 Green Bins Nagarpalika bins

• Details of segregation if to be done: Green bins for bio degradable waste & white bins for non-biodegradable waste

• Capacity and no. of community bins to be placed within premises: 766 bins provided with 5 kg to 25 kg capacity

• Landfill site where waste will be ultimately disposed by local authority: At the nearby waste collection point of Vapi Nagarpalika

15. Parking Details • Total parking area requirement for the project as per GDCR:3,414.33 m2

• Parking area requirement for residential units as per GDCR:3,382.22 m2

• Parking area requirement for Commercial units as per GDCR:32.0 m2

• Total Parking area provided (m2) & No. of CPS: 2,970.0 m2&110 CPS

• Parking area provided in hollow plinth (m2) & No. of CPS:2,420.0 m2& 86 CPS

• Parking area provided as open surface (m2) & No. of CPS: 550.0 m2& 24 CPS

16. Traffic Management

• Width of adjacent public roads: 12 m and 9.0 m

• Number of Entry & Exit provided on approach road/s: 2 gates will be provided.

• Width of Entry & Exit provided on approach road/s:7.5 m and 6.0 m

• Minimum width of open path all around the buildings for easy access of fire tender (excluding the width for the plantation): 4.0 m

• Width of all internal roads: 7.5 m, 6 m, 5.0 m, 4.5 m

17. Details of Green Building measures proposed.

Maximum use of natural lighting through architectural design, energy efficient motors & pumps, water efficient taps, maximum use of RMC & aerated blocks, use of LED lighting fixtures and low voltage lighting, solar lighting in open and landscape areas, roof-top thermal insulation, rain water harvesting & ground water recharge through 2 nos. of percolating wells etc.

18. Energy Requirement, Source and Conservation

• Power supply: Maximum demand: 1700 KVA Connected load: --

• Source: DGVCL

• % of saving with calculations: ~30% by use of LEDs, solar lights and star rated energy efficient electronic consumer durables

• Compliance of the ECBC guidelines (Yes / No),if yes, compliance in tabular form: only roof area

• DG Sets: No. and capacity of the DG sets: 1x 125 KVA

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Fuel & its quantity: HSD, 25litre/hr

19. Fire and Life Safety Measures

• During Construction Phase: Provision of Personal Protective Equipment’s (PPEs) to the construction workers and its usage shall be ensured and supervised, training to all workers on construction safety aspects, first aid room with first aid kit, doctor & ambulance service.

• During operation phase: Fire extinguishers, hose reel, Down comer, manually operated fire alarm system, terrace tank - 175 KL capacity (total capacity), pump near underground static water storage tank (fire pump) with minimum pressure of 2 kg/cm2– 900 l/min at terrace level etc.

• Nearest Fire station: Vapi fire station. Distance from the project site: 3.0 km Time required by the fire tender to reach the project site: about 15 minutes.

20. Details on staircase

Type & no. of buildings

No. of floors Floor area

m2 No. of

staircase

Width of the staircase

(m)

Travel distance

(m)

A H.P. + 7 350.36 1 1.5 16

B H.P. + 7 335.49 1 1.5 16

C H.P. + 7 270.46 1 1.5 16

D, E, F H.P. + 7 379.41 1 1.5 16

G H.P. + 7 335.16 1 1.5 16

21. Rain Water Harvesting (RWH)

• Level of the Ground water table:

• No.& dimensions of RWH tank(s) : 2 Nos

• No. and depth of percolations wells : 2 nos

• Details on Pre-treatment facilities : Desilting cum filter chamber

22. Green area details

• Tree covered area (m2):100.0

• Area covered by shrubs and bushes (m2):100.0

• Lawn covered area (m2):625.0

• Total Green Area (m2):725.0

• Green Area % of plot area: 10%

• No. of trees and species to be planted: 50 no. of trees will be planted in premises.

23. Dust control measures

Spraying of water, peripheral barricading covered shed for cement loading, covering the excavated earth with tarpaulin sheet, compaction of soil during various construction activities etc.

24.

Budgetary allocation for Environmental Management Plan (Rs. in lacs)

Allocation of Rs. 17.0lacs& Rs.7.0lacs as capital cost & recurring cost respectively has been made for EMP & EMS including green belt development, rain water harvesting / ground water recharge, solid waste management etc.

25. Details of eco-friendly building materials

Fly ash bricks, aerated blocks, fly ash paving blocks, maximum use of RMC, lead free paints etc.

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26. Details of amenities to be provided to construction workers.

Sanitation facilities, maintaining hygienic condition at the project site to avoid health problems, safe drinking water, PPEs, first aid room with first aid kit & welfare facilities as per the Gujarat Building & Other Construction Workers Rules.

27. Documents related to land possession.

Village form no. 7, submitted shows NA land is in the name of M/s. Shree Krishna Enterprise.

During the meeting,it was found that the project proponent has submitted a copy of Vapi Nagarpalika letter

stating that Nagarpalika will provide water supply and drainage facilities to the project. The project

proponent was suggested to increase parking area provision for the project, to provide STP for treatment

of sewage to be generated during the operation phase, to reuse treated sewage within premises and to

provide onsite Organic Waste Convertor for converting organic waste into useful end product. After

detailed discussion, it was decided to consider the project only after submission of the following:

1. Proposal for providing STP for treatment of sewage to be generated during the operation phase.

Details of the Sewage Treatment Plant including its capacity, size of each unit, retention time, other

technical parameters etc. along with the plan &budget allocation for its installation, operation &

maintenance. Quality of treated sewage and application wise break-up of treated sewage quantitytobe

recycled / reused in flushing & green belt development, its location on the layout plan, STP sludge

management plan etc.

2. Revised water balance details considering the reuse of treated sewage for purposes like flushing,

gardening etc. within premises

3. Proposal to provide Organic Waste Converter for converting biodegradable waste into the useful end

product. Details of the proposed OWC including its type, capacity, characteristics, its location on the

layout plan, end product management plan etc. should also be submitted.

4. Revised details on increased parking area provision for the project along with the back up calculation &

parking plans.

2. Glory Heights Block No. 42, F.P. No. 131, T.P.S. No. 25 (Mota

Varachha), Surat Screening, Scoping &Appraisal.


Sr. No.

Particulars Details


2. Type of Project Residential


8(a)


Glory Heights

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Mr. Babubhai O. Maiyani


Rs. 46.93 crores

7. Whether construction work has been initiated at site? If yes, details thereof

No

8. Project Details • Land / Plot Area (m²): 6,432.0

• FSI area (m2): 17,254.12

• Total BUA (m2): 31,919.87


FSI Area (m²) - 17,254.12

Ground Coverage (m²) - 1,449.67

Common Plot Area (m²) 643.20 798.0

Max. building height (m) - 45

9. Building Details • No. of Buildings: 4

• No. of Blocks: 4

• Scope of buildings/blocks:2 level basement +Hollow plinth +14 floors

• No.& size of Residential Units: 136 units

• Details of amenities if any: Club house and jogging track


816



• Source of water: Water supply from Surat Municipal Corporation (SMC)


• Mode of disposal: Disposal through Surat Municipal Corporation drain


• Total Water requirement (KL/day): 114.70




• Mode of disposal: Disposal through Surat Municipal Corporation drain

13 Status of water supply and drainage line

Both drainage and water supply lines are existing at site.

14 Solid waste Management

Construction Phase:

Generation (m3)



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Top Soil


Construction debris

Steel scrap


Operation Phase:

Type of waste




Dry waste 293.76 Into bins to be provided within premises.

Organic waste will be treated within premises using OWC. Recyclable waste will be sold to vendors and the other garbage will be disposed as per the practice of SMC

Wet waste 195.84

• Details of segregation if to be done: Solid waste segregation at source will be adopted and wet waste will be processed within premises using OWC, recyclable waste will be sold to recycler.

• Capacity and no. of community bins to be placed within premises:2nos of bins having capacity of 75 kg each for dry waste and75 kg for wet waste will be provided to each building.

• Landfill site where waste will be ultimately disposed by local authority: Khajod Disposal Site

15 Parking Details • Total parking area requirement for the project as per GDCR: 3,796.0 m²

• Parking area requirement for residential units as per GDCR: 3,796.0 m²

• Total number of CPS requirement for the project as per NBC: 136

• Total Parking area provided (m²) & No. of CPS: 11,836.89 m² & 381 CPS

• Parking area provided in basement (m²)& No. of CPS: 9,989.22 m² and 312 CPS .

• Parking area provided asopen surface area (m²)&No. of CPS: 398.0 m²and 17 CPS

• Parking area provided in hollow plinth (m²) & No. of CPS: 1,449.67 m²and 52 CPS

16 Traffic Management

• Width of adjacent public roads: 18 m

• Number of Entry & Exit provided on approach road/s: 1 gate will be provided.

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• Width of Entry & Exit provided on approach road/s: 15 m

• Minimum width of open path all around the buildings for easy access of fire tender (excluding the width forthe plantation): 6.5 m

• Width of all internal roads:7.5 m

17 Details of Green Building measures proposed.

Provision to install aerated coke (foam type) in wash basins, kitchen, low flush water closets in toilet and pressure reducing valves in water pipeline, rain water harvesting & ground water recharge etc.

18 Energy Requirement, Source and Conservation

• Power supply: Maximum demand: 2000 KVA Connected load: 2000 KVA Source: DGVCL

• Energy saving measures: Maximum use of natural light is an integral part of the architectural design, thermal insulation on roof top, proper orientation of buildings to get maximum advantage of natural ventilation, wind direction and light, white tiles on terrace floor to reduce heat absorption, solar based LED lights in landscaped and drive way areas, LED lighting fixtures in the common areas, appropriate design to shut out excess heat and maintain indoor air quality etc.

• DG Sets: No. and capacity of the DG sets:4 x 50 KVA Fuel & its quantity: diesel (10Liter/h)

19 Fire and Life Safety Measures

Fire extinguishers & hose reel at each floor, wet riser opening at each floor, automatic sprinkler system in basement, manually operated electric fire alarm system, underground water storage tank of 75 KL capacity & terrace water storage tank of 5 KL for each building etc.

20 Details on staircase


No. of floors

Floor area

No. of staircase

Width of the staircase (m)

Travel distance (m)

A, B & D 2B+HP+14 1 2.01 < 30

C 2B+HP+14 1 2.01 < 30

21 Rain Water Harvesting (RWH)

• Level of the Ground water table:12 m

• No. & dimensions of RWH tank(s) :-

• No. and depth of percolations wells :3

• Details on Pre-treatment facilities :only roof top rainwater harvesting is proposed

22 Green area details

• Tree covered area (m²):

• Area covered by shrubs and bushes (m2): included in lawn covered area.

• Lawn covered area (m²):

• Total Green Area (m²): 798.0

• Green Area % of plot area:13.66%

• No. of trees and species to be planted: 250trees of Asopalav, Kadam, Golmohar, Jambu, Badam, Gunda, Rayan etc.

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23


Rs. 20-30 Lakhs

24 Proposed dust control measures during the construction phase

• Sprinkling of water for dust suppression.

• To avoid dust emission, excavated soil & construction debris will be sprinkled with water and kept moist.

• Construction material storage area will be covered with tarpaulin sheets.

• Trucks used for transportation of construction material will be covered to avoid dust dispersion at site.

• Project site boundary will be barricaded with sheet of 15 ft height.

25 Eco friendly building material usage details.

Fly ash bricks, aerated blocks, paving blocks, RMC, lead free paints etc.

26 Facilities to be provided to the construction workers

Drinking water, sanitation facilities, sewage disposal facility, first aid box, free medicines, doctor service etc.

27 Document related to Land possession

Registered sale deed submitted shows land is in the name of applicant Mr. Babubhai O. Maiyani& others.

During the meeting,it was presented that the project site is at a distance of 147.9 m from river Tapi. The

project proponent was suggested to provide STP for treatment of sewage to be generated during the

operation phase and to reuse treated sewage within premises. After detailed discussion, it was decided to

consider the project only after submission of the following:

1. Proposal for providing STP for treatment of sewage to be generated during the operation phase. Details

of the Sewage Treatment Plant including its capacity, size of each unit, retention time, other technical

parameters etc. along with the plan &budget allocation for its installation, operation & maintenance.

Quality of treated sewage and application wise break-up of treated sewage quantitytobe recycled /

reused in flushing & green belt development, its location on the layout plan, STP sludge management

plan etc.



3. Notarized consent of other land owners regarding issuance of Environmental Clearance for the

proposed project in the name of the applicant.

4. Copy of permission obtained from Airports Authority of India for the proposed building height.

5. Details of permissible FSI for the project along with the authentic supporting documents.

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6. Full size project plan showing building wise & floor wise built up area, FSI area, floor area tables& plot

area statement.

7. Details with respect to proposed use / disposal of excavated soil. Plan for management, use and

disposal of construction debris including excavated materials during the construction phase. Details of

top soil management plan during construction phase.

3. River Estillo (Manidhara Group)

T.P.S. No. 18 (Mota Varachha), Block No. 107 + 108, F.P. No. 56, 57, O.P. No. 53, 54, Mota Varachha, Surat

Screening, Scoping &Appraisal.

The SEIAA, Gujarat has accorded environmental clearance to Mr. Amitbhai Gorasiya for the residential

building construction project at T.P.S. No. 18 (Mota Varachha), Block No. 107 + 108, F.P. No. 56, 57, O.P.

No. 53, 54, Mota Varachha, Surat vide order no. SEIAA/GUJ/EC/8(a)/696/2016 dated 07/12/2016 for the

built up area of 25,793.98 m2 comprising of 40 flats.

The project proponent vide proposal no. SIA/GJ/NCP/72045/2018dated 01/02/2018 along with Form – I &

IA applied for the proposed changes & expansion of the project.

Details of the project after the proposed expansion as presented before the committee are described below:

Sr. No.

Particulars Details


2. Type of Project Residential


8(a)


River Estilo


Manidhara Reality LLP


Rs. 70 crores


Yes, Construction activity has been started inline with previous issued EC.

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8. Project Details • Land / Plot Area (m²): 6,395.0

• FSI area (m2): 25,485.56

• Total BUA (m2): 40,529.58


FSI Area (m²) 25,533.33 25,485.56

Ground Coverage (m²) 1,822.50 1,799.94

Common Plot Area (m²) 639.50 639.99

Max. building height (m) 100.0 77.00



• Scope of buildings/blocks: 2 level basement + Ground Floor +22 floors

and 1 Club house

• No.& size of Residential Units: 85 units

• Details of amenities if any: Club house and jogging track


425


• Water requirement (KL/day):17.80

• Source of water: Water supply from SMC


• Mode of disposal: Disposal through SMC drain


• Total Water requirement (KL/day): 64.0

• Fresh water requirement (KL/day): 40.0

• Source of water: Water supply from SMC


• Mode of disposal: Sewage to be generated will be treated in the

proposed onsite STP. Treated sewage will be reused for gardening &

flushing purpose within premises and remaining quantity of treated

sewage will be discharged into the drainage line of SMC.

• In case of STP provision, capacity of STP:- 75 KL/day

• STP Technology:- FMR technology

• Purposes for treated water utilization: - Flushing and gardening.

• Quantity of treated water to be reused: 1.Gardening (KL/day):4.0.

2. Flushing (KL/day): 20.0

• Provision of dual plumbing system (Yes/No): -Yes

• Quantity and type (treated/untreated) of water to be discharged: Sewage

to be generated will be treated in the proposed on site STP. Treated

sewage will be reused for gardening & flushing purpose within premises

and remaining quantity of treated sewage will be discharged into the

drainage line of SMC.

• Mode of disposal: as above.

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13 Status of water supply and drainage line

Both drainage and water supply lines are existing at site.

14 Solid waste Management

Construction Phase:

Generation (m3)



Top Soil 1,918.5 400

400 m3 excavated top soil will be utilized for greenbelt development.


39,404.56 2,318.5 m3 will be used for back filing & plinth filing within premises

38,604.56 m3 will be utilized at other project site after obtaining necessary permission, if any.

Construction debris

15kg/day Nil Sold off to recyclers

Steel scrap 15kg/day


6kg/day

Operation Phase:

Type of waste




Dry waste 56 kg/day Into bins to be provided within premises.

Organic waste will be treated within premises using OWC. Recyclable waste will be sold to vendors and the other garbage will be disposed as per the practice of SMC

Wet waste 72 kg/day

• Details of segregation if to be done: Solid waste segregation at source will be adopted and wet waste will be processed within premises using OWC, recyclable material will be sold to recycler.

• Capacity and no. of community bins to be placed within premises: 2 nos of bins having capacity of 50 kg each for dry waste and 50 kg for wet waste will be provided to each building.

• Landfill site where waste will be ultimately disposed by local authority: Khajod Disposal Site

15 Parking Details • Total parking area requirement for the project as per GDCR: 12,742.78 m²

• Parking area requirement for residential units as per GDCR: 12,742.78 m²

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• Total number of CPS requirement for the project as per NBC : 85

• Total Parking area provided (m²) & No. of CPS: 12,790.0 m² and 404 CPS

• Parking area provided in basement (m² ) & No. of CPS: 12,050.01 m² and 377 CPS

• Parking area provided in hollow plinth (m² )& No. of CPS: 601.83 m² and 21 CPS

• Parking area provided on surface (m² ) & No. of CPS: 138.16 m² and 6 CPS

16 Traffic Management

• Width of adjacent public roads: 45 & 24 m


• Width of Entry & Exit provided on approach road/s:9 m


• Width of all internal roads: 9.0 m

17 Details of Green Building measures proposed.

Provision to install aerated coke (foam type) in wash basins, kitchen, low flush water closets in toilet and pressure reducing valves in water pipeline, rain water harvesting & ground water recharge, maximum utilization of natural light, roof-top thermal insulation, LED lighting fixtures in the common areas, appropriate design to shut out excess heat and gain loss, use of solar energy in external lighting (landscape lighting), use of aerated blocks etc.

18 Energy Requirement, Source and Conservation

• Power supply: Maximum demand: 500 KW Connected load: 550 KW Source: DGVCL

• Energy saving measures: Maximum utilization of natural light, roof-top thermal insulation, LED lighting fixtures in the common areas, appropriate design to shut out excess heat and gain loss, use of solar energy in external lighting (Landscape lighting),use of aerated blocks etc.

• DG Sets: No. and capacity of the DG sets:4 x 60 KVA Fuel & its quantity: diesel (10Liter/h)

19 Fire and Life Safety Measures

• During the construction phase: Fire extinguishers at various locations and can be easily accessible, to keep printed board showing important telephone number of fire, ambulance, hospital etc. training to the workers on safety aspects, first aid box at identified places within premise, doctor & ambulance services, provision of PPE’s like helmet, gumboot/safety net, safety goggles etc.

• During the operation phase: Fire extinguishers on each floor & in the basement, wet riser opening at each floor, manually operated electric fire alarm system, hose reel, terrace water tanks of 15 KL capacity, underground water tank of 200 KL, smoke detectors etc.

• Nearest fire station: Varachcha fire station. Distance from project site: 4.0 Km.

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20 Details on staircase


No. of floors

Floor area

No. of staircase


Travel distance (m)

A & B 2B+G+22 1,161.40 4 1.82 m < 15 m

21 Rain Water Harvesting (RWH)

• Level of the Ground water table:12 m

• No. & dimensions of RWH tank(s) :-

• No. and depth of percolations wells :2

• Details on Pre-treatment facilities :only roof top rainwater harvesting is proposed

22 Green area details

• Tree covered area (m²) : 450

• Area covered by shrubs and bushes (m2): included in lawn covered area.

• Lawn covered area (m²): 550

• Total Green Area (m²): 1,000

• Green Area % of plot area: 15.64 %

• No. of trees and species to be planted: 105 trees of Asopalav, Kadam, Golmohar, Jambu, Badam, Gunda, Rayan etc.

23


Green belt development : 25 Lacs Drainage and rain water harvesting: 55 lacs Solar and energy saving: 45 lacs STP & dual plumbing: 40 lacs Total: 165 Lacs

24 Proposed dust control measures during the construction phase

Loading & transportation in covered trucks, covered shed provided for cement unloading activity, temporarily wind screen around project site, sprinkling of water on roads and in vicinity of storage area.

25 Eco friendly building material usage details.

Fly ash bricks & aerated block, paving blocks, RMC (Ready Mix Concrete), lead free paints etc.

26 Facilities to be provided to the construction workers

Sanitation facilities, drinking water & tap water, sewage disposal facility, first aid box, free medicines, doctor service, adequate PPEs etc.

27 Document related to Land possession

Sub- register’s office index submitted shows NA land for residential use is in the name of M/s. Manidhara Reality.

During the meeting, it was found that the project proponent submitted acopy of permission obtained from

Airports Authority of India for permissible building height of 100.0 m above ground level. Project proponent

has submitted compliance report with reference to the conditions stipulated in the Environmental

Clearance order no. SEIAA/GUJ/EC/8(a)/696/2016 dated 07/12/2016. They have also submitted a

notarized undertaking regarding the Compliance of previous Environment Clearance granted to the project

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mentioning that there isn’t any litigation pending against the project in court of law and they have not

received any notice under the Environment Protection Act – 1986. A copy of certificate from structural

engineer stating that the buildings will be designed for two level basement + ground floor + twenty second

floors has been submitted. Also project proponent has submitted a copy of LLP agreement document for

M/s. Manidhara Reality LLP. Copy of permission obtained from Urban Development & Urban Housing

Department for permissible FSI of 25,533.33 m2 has been submitted. The project proponent has submitted

an NOC from Mr. Amitbhai Gorasiya for transferring the EC in the name of M/s Manidhara Realty. After

detailed discussion committee, it was decided to recommend the project to SEIAA Gujarat for transferring

the granting Environment Clearance, in supersession of the Environmental Clearance order no.

SEIAA/GUJ/EC/8(a)/ 696/2016 dated 07/12/2016, subject to the strict compliance of the following project

specific conditions as well as the standard conditions finalized during the meeting of SEAC held on

02/08/2017 and approved during the meeting of SEIAA held on 08/09/2017 for The Building Construction

projects falling under project activity no. 8(a) as per the schedule of the EIA Notification 2006:

Project Specific Conditions with which Environment Clearance is recommended:

CONSTRUCTION PHASE :

WATER:

1. Fresh water requirement during the construction phase shall be 17.8 KL/day and it shall be met through

the water supply from Surat Municipal Corporation (SMC). No ground water shall be tapped during the

construction phase.

2. Sewage generated during the construction phase shall be disposed off through drainage system of

SMC.

OPERATION PHASE :

WATER:

3. Total water requirement during the operation phase shall be 64.0 KL/day, out of which fresh water

requirement of 40.0 KL/day shall be met through water supply system of Surat Municipal Corporation

and the remaining 24.0 KL/day of water requirement shall be met through treated sewage. No ground

water shall be tapped during the operation phase. Metering of the water shall be done and its records

shall be maintained.

4. Sewage generation during operation phase shall be 48.0 KL/day which shall be treated in the proposed

onsite Sewage Treatment Plant.

5. The unit shall install and efficiently operate STP of adequate capacity for treating the sewage to be

generated during operation phase to achieve the GPCB norms at the STP outlet. Treated sewage

conforming to GPCB norms shall be utilized within premises for gardening & flushing purpose at the

maximum extent possible. Only remaining quantity of treated sewage shall be disposed off through

drainage line of Surat Municipal Corporation.

6. A proper logbook of STP operation and also showing the quantity of treated sewage utilization within

premises & quantity of treated sewage discharged into the drainage line shall be maintained and

furnished to the GPCB from time to time.

7. Dual plumbing system with separate tanks and lines shall be provided for utilization of treated sewage

for flushing.

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8. No new bore well shall be constructed and existing bore well/s shall be either sealed or converted into

the recharge well upon completion of the construction work.

9. Rain water harvesting from rooftop and paved areas and ground water recharge through 2 nos. of

percolation wells shall be carried out as per the details submitted. Before recharging the run off, pre-

treatment must be done to remove suspended matter.

AIR:

10. D. G. sets (4 x 60 KVA) proposed as backup power shall be of enclosed type and confirm to prescribe

standards under EPA rules. Necessary acoustic enclosures shall be provided at diesel generator set to

mitigate the impact of noise.

11. The stack height of the D.G.sets shall be equal to the height needed for the combined capacity of all

proposed D.G.sets.

12. The gaseous emissions from the D.G. Sets shall conform to the standards prescribed under EPA rules

as amended from time to time. At no time, the emission levels shall go beyond the stipulated

standards.

SOLID WASTE:

13. The solid waste generated shall be properly collected and segregated at source. The biodegradable

waste shall be converted into useful end product by treating it into the proposed onsite Organic Waste

Convertor and the recyclable waste shall be sold to vendors whereas the other garbage shall be

disposed off properly as per the provisions made by the Surat Municipal Corporation (SMC).

SAFETY:

14. Fire fighting facilities like fire extinguishers on each floor & in the basement, wet riser opening at each

floor, manually operated electric fire alarm system, hose reel, terrace water tanks of 15 KL capacity,

underground water tank of 200 KL, smoke detectors etc.shall be provided as proposed.

15. All the staircases and lifts shall open out at ground level from the highest point of building [with access

from each floor] for emergency evacuation. Two staircases shall be provided in each building having

floor area more than 500 m2 on each floor.

16. In basement at least two separate ramps of adequate width and slope shall be provided, located

preferably at opposite ends.

17. Provision for adequate air changes per hour in the basement shall be made so as to avoid build up of

CO in the area.

18. Car park exhaust system equipped with CO (Carbon Monoxide) sensor shall be provided to ensure

operation of exhaust fans as CO concentration levels.

PARKING / TRAFFIC CONGESTION:

19. Minimum parking space of 12,790.0 m2 [601.83 m2 in hollow plinth + 12,050.01 m2 in basement +

138.16 m2 as open surface parking ] shall be provided as proposed.

ENERGY CONSERVATION:

20. Energy conservation measures viz. maximum utilization of natural light, roof-top thermal insulation,

LED lighting fixtures in the common areas, appropriate design to shut out excess heat and gain loss,

use of solar energy in external lighting (landscape lighting), use of aerated blocks etc.shall be

implemented as proposed.

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GREEN BELT:

21. Green belt area of 1,000.0 m2 comprising of 450.0 m2 tree covered area with 105 trees within premises

shall be developed as proposed. The other open spaces inside the plot shall be suitably landscaped

and covered with vegetation of indigenous tree species.

4. Navkar Avenue Block No. 84/B, O.P. No. 64, F.P. No. 64, T.P.S. No. 45 (Navagam Vav), Navagam, Kamrej, Surat

Screening / scoping & appraisal.


Sr. No.

Particulars Details


2. Type of Project Residential (High Rise)


8(a)

4. Name of the project “Navkar Avenue”

5. Name of Developer VipulkumarJasmatbhai


Rs. 203Crore


No


• FSI area (m2): 20,410.27

• Total BUA (m2) :27,103.89


FSI Area (m2) 20,690.46 20,410.27


Common Plot Area (m2) 770.60 1,672.0

Max. building height (m) 45 24.55



• Scope of buildings/blocks: Basement + Hollow Plinth +8 floors

• No. & size of Residential Units: 308Nos.

• No. & type of Commercial Units: --

• Details of amenities if any: --

10. No. of expected Expected residents:1540

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residents / users Expected shop users: --

Expected visitors: 700





• Mode of disposal: Soak pit

• Details of reuse of water, if any: W/W generated from washing of equipment will be reused for curing after necessary treatment.


• Total water requirement (KL/day): 222.0




• Mode of disposal: Sewage to be generated will be treated in the proposed onsite STP. Treated sewage will be used for gardening & flushing purpose within premises and remaining quantity of treated sewage will be discharged into the drainage line of SMC.

• In case of STP provision, capacity of STP:200KL/day

• STP Technology: Primary, secondary & tertiary treatment.

• Purposes for treated sewage utilization: Treated sewage will be utilized in gardening and flushing.

• Quantity of treated sewage to be reused:1.Gardening (KL/day):3.50 2. Flushing (KL/day): 85.0

• Provision of dual plumbing system (Yes/No): Yes

• Quantity and type (treated/untreated) of sewage to be discharged: Sewage to be generated will be treated in the proposed onsite STP. Treated sewage will be used for gardening & flushing purpose within premises and remaining quantity of treated sewage will be discharged into the drainage line of SMC.

• Mode of disposal: as above.


SMC Water supply line is passing 1 km away from the plot boundary

14. Solid waste Management Construction Phase:

Generation (m3)



Top Soil 385.30 385.30 Reuse for developing garden area


2,091.0

842.25 Will be disposed to other project site

Construction debris

285 136 Reused as a filler up to plinth level &

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remaining will be reused for outer road development and balance quantity if any will be disposed as per C & D waste rules 2016.

Steel scrap 11 -- Sold to local scrap vendors


07 -- Sold to local vendors

Operation Phase:

Type of waste


Mode of waste

collection


Dry waste 369.60 Blue colour bucket

Through door to door waste collection system of SMC.

Wet waste 554.40 Green colour bucket

Collection in separate bins and converted intomanure by installing organic waste converter with in premises. Manure will be either sold or reuse within the premises.

Used oil 80 L/year Drum Sell to registered recyclers approved by GPCB/CPCB.

E-Waste 60 kg/d -- Collection, Storage and disposal through agency authorized by GPCB/ CPCB.

STP Sludge 20 kg/d On SDB Reused in gardening as manure within

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project premises

• Details of segregation if to be done: Separate bins will be provided to collect dry and wet waste.

• Capacity and no. of community bins to be placed within premises: 0.5 m3 in each building

• Landfill site where waste will be ultimately disposed by local authority: KhajodLandfill site of SMC.

15. Parking Details • Total parking area requirement for the project as per GDCR: 4,082.05 m2

• Parking area requirement for residential units as per GDCR: 4,082.05 m2

• Total Parking area provided (m2) & No. of CPS: 5,216.19m2 &187

• Parking area provided in Basement (m2) & No. of CPS: 1,543.19m2&48 ECS

• Parking area provided in hollow plinth (m2) & No. of CPS: 2,585.28m2& 92 CPS

• Parking area provided as open surface (m2) & No. of CPS:1,087.72 m2& 47 CPS

16. Traffic Management • Width of adjacent public roads:18.0 m


• Width of Entry & Exit provided on approach road/s: 7.50m


• Width of all internal roads:4.0 m, 7.50 m


Use of fly ash based material, provision of flush tank instead of direct flushing in toilet, provision of foam type aerated cock for water usage, use of LED light in common building areas, solar lights for landscape areas, maximum use of natural lighting, reflective / white tiles on terrace floor etc.


• Power supply

Maximum demand: 3000 KVA

Connected load:

• Source: D.G.V.C.L

• Energy saving measures: Use of LED light in common areas, solar lights for landscape areas, maximum use of natural lighting, reflective / white tiles on terrace floor etc.

• D.G. sets:

No. and capacity of the DG sets: 3 x 125 KVA

Fuel & its quantity: Low Sulphur High speed Diesel (HSD) & quantity 55 L/h in each.

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Fire extinguisher, hose reel, wet riser, automatic sprinkler system in basement, manually operated electric fire alarm system, underground water tank of 75 KL capacity, terrace tank of 10 KL capacity, one electric & one diesel pump of capacity 1800 L/min. & one electric pump of capacity 200 L/min. having pressure 4.0 kg/cm2 at terrace level etc.


Bldg. No.

No. of Floors Floor Area

(m2) No. of

Staircase

Width of Staircase

(m)

Maximum Travel

Distance up to the

Staircase (m)

A B+HP+8 245.71 01 1.52 11.21

B, C, D, E, F, K B+HP+8 241.06 01 1.52 8.88

G + H B+HP+8 501.65 02 1.52 8.77

I + J B+HP+8 480.72 02 1.52 9.13

21. Rain Water Harvesting

(RWH)

• Level of the Ground water table: 20.0 m

• No. & dimensions of RWH tank(s): 04no. of RWH tanks;

Size: 4 m x 3 m x 3 m

Size of Bore: 350 mm dia.

Size of pipe: 150 mm dia.

• No. and depth of percolations wells: 04nos. of percolating wells.

• Details on Pre-treatment facilities: A de-silting chamber will be provided to de-silt and remove floating material through bar screen

22. Green area details • Tree covered area (m2):40.60

• Area covered by shrubs and bushes (m2): --

• Lawn covered area (m2): 730.0

• Total Green Area (m2):770.60

• Green Area % of plot area: 10.00 %

• No. of trees and species to be planted: 64 trees of Asopalav,Coconut Palm, Neem, Gulmoharetc.

23.

Budgetary allocation for Environmental Management Plan

(Rs. in lacs)

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Sr

.

N

o.

Particulars

Approximate

recurring cost

per annum (Rs.

In Lacs)

Approxim

ate

Capital

cost

(Rs. In

Lacs)

1. Air pollution 0.75 1.80

2. Water pollution including STP

4.50 25.0

3. Solid and hazardous waste management including STP sludge

0.60 1.0

4. Green belt development 1.0 3.0

5. Rain water harvesting 1.0 7.50

Total 7.85 38.30

24. Proposed dust control measures during the construction phase

Covering of building materials by tarpaulin, sprinkling of water, covering structure with Hessian clothes will be made to curb fugitive emission.

25. Eco friendly building material usage details

Fly ash bricks, aerated blocks, paving blocks PP Cement in concrete will be used.

26. Basic amenities to be provided to construction workers

Drinking water & tap water, sanitation facilities, first aid box, free medicines, medical services, PPE will be provided.


NA order submitted shows that NA land for residential use is in the name of the applicant & others. Notarized consent of other land owners, in favour of the applicant has been submitted.

During the meeting, it was found that the project proponent has submitted a copy of certificate obtained

from structural engineer stating that the buildings will be designed for ground floor + eight floors.Acopy of

application made for obtaining NOC from Airport Authority of India has been submitted. The project

proponent was suggested to increase the parking area provision for the project by providing full basement,

to which the project proponent was agreed. After detailed discussion, it was decided to consider the project

only after submission of the following:

1. Details of permissible FSI for the project along with the authentic supporting documents.

2. Revised details on increased parking area provision for the project along with back up calculations &

parking plans. If the basement area will be increased for increasing the parking area provision, the

revised project plan & revised Form-I should also be submitted in view of increased built up area of the

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project.

5. Dream City R.S. No. 322/P1, Dungra, Vapi, Valsad Screening / scoping & appraisal.


Sr. No.

Particulars Details


2. Type of Project Residential Project


8 (a)


Dream City


Regal Infra


25.30Crores


No


• FSI area (m2):17,036.99

• Total BUA (m2):23,370.21


FSI Area (m2) 32,202.0 17,036.99


Common Plot Area (m2) 1,789.0 1,790.0

Max. building height (m) -- 15.0

9. Building Details • No. of Buildings:10

• No. of Blocks:10

• Scope of buildings/blocks: H.P. + 4 floors

• No.& size of Residential Units:236 Flats, 26 Bunglows

• No. & type of Commercial Units: Nil

• Details of amenities if any: No


1180 occupants from Residential units

11. Water & waste water details



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during construction phase


• Mode of disposal: Septic tank &Soak pit

• Details of reuse of water, if any: 4.0 KL/day for curing


• Total water requirement (KL/day): 169.0


• Source of water: Water supply from Vapi Nagarpalika


• Mode of disposal: into drainage line of Vapi Nagarpalika


Available at site

14. Solid waste Management

Construction Phase:

Generation (m3)



Top Soil 1,800.0 1,800.0 Reuse for greenbelt development.


- -

Construction debris

260.0 240.0 m3 will be reused within premises.

Balance debris will be handed over to Nagar Palika

Steel scrap 8 0 Sold to vendors


5 0 Sold to vendors

Operation Phase:

Type of waste




Dry waste 300 White bins Sold to vendors

Wet waste 450 Green Bins Nagarpalika bins

• Details of segregation if to be done: Green bins for bio degradable waste & white bins for non-biodegradable waste

• Capacity and no. of community bins to be placed within premises: 645 bins provided with 5 kg to 25 kg capacity

• Landfill site where waste will be ultimately disposed by local authority: At the nearby waste collection point of Vapi Nagarpalika

15. Parking Details • Total parking area requirement for the project as per GDCR:3,407.40 m2

• Parking area requirement for residential units as per GDCR:3,407.40 m2

• Total Parking area provided (m2) & No. of CPS: 6,546.64 m2&257 CPS

• Parking area provided in hollow plinth (m2) & No. of CPS:3,656.64 m2&131 CPS

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• Parking area provided as open surface (m2) & No. of CPS: 2,890m2&126 CPS

• Parking area provided (at any other place-specify) (m2) & No. of CPS: - Individual parking for bungalows

16. Traffic Management

• Width of adjacent public roads: 24 m

• Number of Entry & Exit provided on approach road/s: 01 gate will be provided.

• Width of Entry & Exit provided on approach road/s: 12.0 m


• Width of all internal roads: 7.0 m, 12.0 m


Maximum use of natural lighting through architectural design, energy efficient motors & pumps, water efficient taps, maximum use of RMC & aerated blocks, use of LED lighting fixtures and low voltage lighting, solar lighting in open and landscape areas, roof-top thermal insulation, rain water harvesting & ground water recharge through 5 nos. of percolating wells etc.


• Power supply: Maximum demand: 1200 KVA Connected load: --

• Source: DGVCL

• % of saving with calculations: ~30% by use of LEDs, solar lights and star rated energy efficient electronic consumer durables

• DG Sets: No. and capacity of the DG sets: 1x 125 KVA

Fuel & its quantity: HSD, 25litre/hr


• During Construction Phase: Provision of Personal Protective Equipment’s (PPEs) to the construction workers and its usage shall be ensured and supervised, training to all workers on construction safety aspects, first aid room with first aid kit, doctor & ambulance service.

• During operation phase: Fire extinguishers, hose reel, Down comer, manually operated fire alarm system, terrace tank - 150 KL capacity (total capacity), pump near underground static water storage tank (fire pump) with minimum pressure of 2 kg/cm2– 900 l/min at terrace level etc.

• Nearest Fire station: Vapi GIDC fire station. Distance from the project site: 3.3 km Time required by the fire tender to reach the project site: about 15 minutes.



No. of floors Floor area

m2 No. of

staircase


(m)

Travel distance

(m)

A1 + A2 HP+4 526.55 2 1.50 17

B HP+4 335.86 1 1.50 17

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C1 + C2 HP+4 651.87 2 1.50 17

D1 + D2 HP+4 739.40 2 1.50 17

E HP+4 346.26 1 1.50 17

G1 + G2 HP+4 553.35 2 1.50 17

21. Rain Water Harvesting (RWH)

• Level of the Ground water table:

• No.& dimensions of RWH tank(s) : 5 No

• No. and depth of percolations wells : 5 no and 10 m

• Details on Pre-treatment facilities : Desilting cum filter chamber

22. Green area details

• Tree covered area (m2) :400

• Area covered by shrubs and bushes (m2): -

• Lawn covered area (m2):1,390.0

• Total Green Area (m2):1,790.0

• Green Area % of plot area: 10%

• No. of trees and species to be planted: 200trees will be planted within premises.

23. Dust control measures

Spraying of water, peripheral barricading, covered shed for cement loading, covering the excavated earth with tarpaulin sheet, compaction of soil during various construction activities etc.

24.


Allocation of Rs. 20.0lacs& Rs.8.0lacs as capital cost & recurring cost respectively has been made for EMP & EMS including green belt development, rain water harvesting / ground water recharge, solid waste management etc.

25. Details of eco-friendly building materials

Fly ash bricks, aerated blocks, fly ash paving blocks, maximum use of RMC, lead free paints etc.

26. Details of amenities to be provided to construction workers.

Sanitation facilities, maintaining hygienic condition at the project site to avoid health problems, safe drinking water, PPEs, first aid room with first aid kit & welfare facilities as per the Gujarat Building & Other Construction Workers Rules.


Copy of NA order submitted shows that the land for residential/ commercial use is in the name of Mr.Salim A. Kherani as a power of Attorny holder of Mr.Ikbal Hamid Khan. Village form no. 7/12 submitted shows that the land is in the name of Mr.Ikbal Hamid Khan. Partnership deed submitted shows that Mr.Salim A. Kheraniis a partner of M/s Regal Infra.

During the meeting,the project proponent submitted a letter obtained from Vapi Nagarpalika stating that

the basic amenities like water supply & drainage facilities will be provided to the project. The project

proponent was suggested to provide STP for treatment of sewage to be generated during the operation

phase, to reuse treated sewage within premises and to provide onsite Organic Waste Convertor for

converting organic waste into useful end product. After detailed discussion, it was decided to consider the

project only after submission of the following:

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1. Proposal for providing STP for treatment of sewage to be generated during the operation phase. Details

of the Sewage Treatment Plant including its capacity, size of each unit, retention time, other technical

parameters etc. along with the plan &budget allocation for its installation, operation & maintenance.

Quality of treated sewage and application wise break-up of treated sewage quantitytobe recycled /

reused in flushing & green belt development, its location on the layout plan, STP sludge management

plan etc.



3. Proposal to provide Organic Waste Converter for converting biodegradable waste into the useful end

product. Details of the proposed OWC including its type, capacity, characteristics, its location on the

layout plan, end product management plan etc. should also be submitted.

4. Details on parking space available within premises of bungalows considering the plot area of each type

of bungalow, ground coverage etc.

5. Authentic documents justifying the ownership of land by the project proponent.

Meeting was concluded with thanks to the Chair.

--------------------------------

Minutes approved by:

Sr.

No.

Name & designation Sign




4. Shri Rajesh I. Shah, Member, SEAC

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



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Minutes of the 383thmeeting of the StateLevelExpertAppraisalCommittee held on

15/03/2018 at Committee Room, GEER Foundation, Gandhinagar.

The 383rdmeeting of the StateLevelExpertAppraisalCommittee (SEAC) was held on 15thMarch2018

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




4. Shri Rajesh I. Shah, Member, SEAC.


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


The agenda of TOR/Scopingcases and Appraisal were taken . cup. 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/IND2/21248/2017 M/s. DevnandanAuxichem LLP

Plot No: 2501, Opp- Torrent Pharma Rajpur, TA- Kadi, Dist: Mehsana

Screening & Scoping

Category of the Project: 5(f)

Project Status: New

• This office has received an application vide their online proposal no. SIA/GJ/IND2/21248/2017 dated 02/12/2017regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP report.

• This is a new unit proposes manufacturing of synthetic organic chemicals as tabulated below:

Sr. No.

Name of the Products CAS no. /CI no.

Quantity MT/Month

End-use of products

1 Textile Emulsion Auxiliary & Adhesive

-- 1260 Textile Industries and other adhesive Industries

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

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notification 2006.

• PP was called for presentation in SEAC meeting dated 10/01/2018.

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

Sr. no.

Particulars Details

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

B Total Plot area ( sq. meter) 7284 Sq. m.

Green belt area,/Tree Plantation area ( sq. meter) 300 Sq. m.

C Employment generation 10 Nos.

D Water i

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

Bore Well

Status of permission from the concern authority. Not applicable

ii Water consumption (KLD)

Category

KLD Remarks

(A) Domestic 1.2

(B) Gardening

(C) Industrial

Process 14.26

Process(DM Water) 3.06* DM Water

Washing 0.8

Boiler 2.5

Industrial Total 17.56

Total (A + B + C)

21.52 3.06* DM Water

Note: 3.06* DM Water Purchase from Out Source

1) Total water requirement for the project: 21.52 KLD

2) Quantity to be recycle: 0.00 KLD

3) Total fresh water requirement: 18.46 KLD

iii Waste water generation (KLD)

Category

Waste water KLD

Remarks

(A) Domestic 1.0 Discharge through

Soak Pit

(B) Industrial

Process NIL

In house Evaporate

Process (DM Water) NIL

Washing 0.8

Boiler 0.2

Cooling

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Total Industrial waste water

1.0

* Note: Total proposed domestic waste water generation 1.0 KLD which will discharge through soak pit. There will be 1.0 KLD wastewater generation from manufacturing activity and other ancillary operation, waste water will be reuse in Emulsion based on quality of waste water or sent to in house Evaporate for the Evaporation, unit is going to ZERO LIQUID DESCHARGE.

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

ZERO LIQUIED DISCHARGE

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

Industrial: There will be 1.0 KLD wastewater generation from manufacturing activity and other ancillary operation, waste water will be reuse in Emulsion based on quality of waste water or sent to in house Evaporate for the Evaporation, unit is going to Zero liquid Discharge

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

Not Applicable

Membership of Common facility (CF) Not Applicable

vii Reuse/Recycle details (KLD) We will reuse for Emulsion Process

E Air

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

-

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control Measures

(APCM)

1 IBR Boiler 11.00

Agro

Waste/

Bio Fuel

2

MT/Day

PM SO2 NO2

Cyclone Separator

Followed By Dust

Collector

-

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

-We have no Process gas Emission

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

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

i

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Sr. no.

Type/Name of Hazardous

waste

Source of generation

Category and

Schedule as per HW

Rules.

Quantity (MT/Ann

um) Disposal Method

1 Used Oil Process

Equipment 5.1 0.5

Collection, storage, Reuse within premises.

2 Discarded Container/

Barrels

Ware House

33.1 6000 Nos.

Collection, storage, Transportation and Dispose

to Registered Recycler

3 Evaporation Evaporation

system 37.3 0.200

Collection, storage, Transportation and Dispose

to Registered Recycler

4 ETP Sludge ETP Area 20.4 0.500 Collection, storage,

Transportation and Dispose to Registered Recycler

Quantity of discarded containers must be in MT/Annum.

ii Membership details of TSDF, CHWIF etc. N.A

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

----

G Solvent management, VOC emissions etc.

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

N.A

ii VOC emission sources and its mitigation measures N.A

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

under 5(f). Committee noted that this is a new proposal.During presentation, water consumption, waste

water generation and final management of treated waste water were discussed at length. PP

mentioned that water supply source will be through bore-well and CGWA permission will be obtained

by the PP. PP stated that as they are outside the GIDC and having water consumption less than 25

KLPD, fuel consumption less than 25 MTPA and no MAH confirming category chemicals are stored in

the premises, they may be considered under the B category which was agreed by the committee.

Committee asked to submit undertaking regarding aforementioned three conditions for qualifying under

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category B as well as details of raw material proposed to be stored in the premises which are in

compliance to non-applicability of major accident hazard chemicals threshold limit as prescribed.

Considering the above project details, it was decided to recommend standard TOR for the Synthetic

Organic Chemical projects approved by SEIAA in its 12th meeting dated 16/09/2017 for the EIA study

to be done covering 10 Km radial distance from the project boundary including following project

specific TOR.

1. To submit NOC from the CGWA for drawing bore well water.

2. Undertaking for the proposed industrial unit under category B qualifying small scale unit

requirement as mentioned in MOEF&CC Notification 25/06/2014.

Further, the TOR prescribed as above and as per the standard TOR approved by SEIAA and the model

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

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

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

2006.

Project proponent shallprepare the draft EIA report covering the all above TOR and it shall be submitted

to the GPCB for conducting the public hearing / 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

7. SIA/GJ/IND2/21264/2017 M/s. Amal Ltd.

Plot No. 136/137, GIDC Ankleshwar, Taluka

Ankleshwar, District Bharuch, Gujarat.

Screening & Scoping

Project / Activity No.: 5(f)

Project status: Expansion

• This office has received an application vide their online proposal no. SIA/GJ/IND2/21264/2017

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

report.

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

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as tabulated below:

Sr.

no. Name of the Products CAS no.

Quantity (MT/Month) End-use

of product Existing Proposed Total

1 98% Sulfuric Acid, 25%-65% Oleum, Liquid SO3& Liquid SO2

7664-93-9, 8014-95-7

3900 6000 9900 As raw material for other chemicals

2 Di Methyl Sulphate (DMS) 77-78-1 0 2000 2000

3 70% sulfuric Acid (Co-product) 7664-93-9 0 100 100

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

2006.

• PP was called for presentation in the SEAC meeting dated 15/03/2018.

• During the meeting dated 15/03/2018, technical presentation made during the meeting by

project proponent.

• Salient features of the project are as under:

Sr. no.

Particulars Details

A Total cost of proposed project (Rs. In Crores):

Existing: INR 6 Crores Proposed: INR 71 Crores Total: INR 77 Crores

(1) Capital cost for EMS (Environmental Management System) : 2.5 Crores (2) Recurring cost towards the environmental protection measures: 0.50 Crores

per Annum.

B Total Plot area (Sq. meter)

Existing: 15552.973 m2 Proposed:36587.65 m2 Total: 52140.623 m2

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

Existing:0 Proposed:5214.06 m2 Total: 5214.06 m2

C Employment generation

1. Direct Existing: 55 Proposed: 36 Total: 91

2. Indirect Existing:-30 Proposed:50

D Water

i

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

Water is sourced from GIDC water supply.

Status of permission from the concern authority.Membership Certificate of NCTL for water supply is already taken.

ii Water consumption (KL/day)

of 137


Page 34 of 137

-

Existing KL/day

Proposed (Additional) KL/day

Total after Expansion KL/day

Remarks

(D) Domestic 15 15 30

(E) Gardening 0 25 25

(F) Industrial

Process 24 172 196

Washing 0 2 2

Waste Heat Recovery Boiler

54 83 137

Cooling 162 340 502

Others 5 5 10 For Fire Fighting

Total (A+B+C) 902

-

iii Waste water generation (KL/day)

-

Category Existing KL/Day



Remarks

(C) Domestic 15 15 30 To Septic Tank

(D) Industrial To ETP

Process 2 11 13

Washing 0 2 2

Waste Heat Recovery Boiler

3 5 8

Cooling 35 73 108

Others - - -


55 106 161 131.0 KLD will be discharged in CETP and Domestic 30 KLD is disposed through Septic tank/soak pit system

-

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

The industrial effluent is treated in ETP of capacity 55 KLD & treated water is going to CETP for further treatment.

v Mode of Disposal & Final meeting point

Domestic:To Septic Tank

Industrial: The industrial effluent is treated in ETP of capacity 55 KLD & treated water is going to CETP for further treatment.

vi Reuse/Recycle details (KL/day) -

vii Details of rain water harvesting System in place. There are two empty ponds at ETP which are used as catchment area of rain water. Office terrace area water also flows to the ponds. Rain water thus collected used in place of raw water.

E Air(Existing and Proposed)

of 137


Page 35 of 137


-

Sr.

no

.

Source

of

emissio

n With

Capacity

e.g.

Boiler

Stack

Heig

ht

(mete

r)

Name

of the

fuel

Quantity

of Fuel

MT/hr&

MT/Day

Type

of

emiss

ions

i.e.

Air

Pollut

ants

AP

CM

Emiss

ion

Stand

ards

Remark

Existing

1

Waste

heat

boiler

2 Nos.

(6

Ton/hr)

-

Waste

heat

Boiler

- -

- -

This is waste heat

boiler. Sulfuric

Acid production is

exothermic

reaction and hence

heat is being

generated. The

same is used for

steam generation.

Hence there is no

fuel or stack

involved in it.

Proposed

1

Waste

heat

boiler

2 Nos.

(12

Ton/hr)

-

Waste

heat

Boiler

- -

- -

This is waste heat

boiler. Sulfuric

Acid production is

exothermic

reaction and hence

heat is being

generated. The

same is used for

steam generation.

Hence there is no

fuel or stack

involved in it.

of 137


Page 36 of 137

2

D.G Set

(600

kVA)

- Diesel 6-8

kl/year

Particulate

Matter, SO2, NOx

Ade

qua

te

Sta

ck

Hei

ght

PM-

150

mg/N

m3,

SO210

0

ppm,

NOx50

ppm

-

-

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

-

Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height

(meter)

APCM

Emission Standards

Existing

1 Sulphuric

Acid Plant

SO2, Acid

Mist 50 Alkali Scrubber

SO2- 2kg/T

Acid Mist- 50 mg/Nm3

Proposed

1 Sulphuric

Acid Plant

SO2, Acid

Mist 50 Alkali Scrubber

SO2- 2kg/T

Acid Mist- 50 mg/Nm3-

-

iii Fugitive emission details with its mitigation measures. Existing:

Sampling

Location

Identified

contaminant

Sampling

instrument

used

TWA concentration

(as given in 2nd

Schedule)

Reference

method

1 Near the storage

acid tank area

SO2 HVS 5.0 mg/Nm3 IS 5182

Part-II 1969

Proposed:

Sampling Identified

contaminant

Sampling

instrument

TWA concentration

(as given in 2nd

Reference

method

of 137


Page 37 of 137

Location used Schedule)

1 Near the storage

acid tank area

SO2 HVS 5.0 mg/Nm3 IS 5182

Part-II 1969

2 Near Methanol

storage tank

Methanol HVS 260.00 mg/Nm3 ASTM

Method

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

i

Sr. no.


waste


Category and

Schedule as per HW

Rules.

Quantity (MT/Annum)

Disposal Method

Exis

tin

g

Pro

pose

d

Tota

l

1 Catalyst Process 17.2 0.06 0.09 0.15 Common TSDF

2 Used oil DG set,

Gear boxes 5.1 0.05 0.08 0.13

re-refiners having valid

authorization of SPCB

3 ETP Sludge Wastewater Treatment

35.3 3.0 4.6 7.6 Common TSDF

4 Sulfur

sediment Process 17.1 20.0 30.8 50.8 Common TSDF

5 Catalyst Process 17.2 0.0 1.4 1.4 Common TSDF

6 Used

Drums/Liners/Carboys|

Packaging 33.1 0.0 3.0 3.0

Sell to authorized

party/ Common TSDF having

authorization of SPCB


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

CETP:Membership Certificate of M/s. Narmada Clean Tech Ltd. For Effluent Treatment TSDF: Membership Certificate of M/s. Bharuch Enviro Infrastructure Ltd. For Hazardous Waste


Not Applicable

G Solvent management (If any)

i Details of Solvent Recovery (As per respective ToR) Not Applicable

ii VOC emission sources and its mitigation measures Not Applicable

of 137


Page 38 of 137


under 5(f). Committee noted that this is a new proposal.During presentation, water consumption, waste

water generation and final management of treated waste water were discussed at length. PP

mentioned that water supply source will be through bore-well and CGWA permission will be obtained

by the PP. PP stated that as they are outside the GIDC and having water consumption less than 25

KLPD, fuel consumption less than 25 MTPA and no MAH confirming category chemicals are stored in

the premises, they may be considered under the B category which was agreed by the committee.

Committee asked to submit undertaking regarding aforementioned three conditions for qualifying under

category B as well as details of raw material proposed to be stored in the premises which are in

compliance to non-applicability of major accident hazard chemicals threshold limit as prescribed.




specific TOR.

1. To submit NOC from the CGWA for drawing bore well water.

2. Undertaking for the proposed industrial unit under category B qualifying small scale unit

requirement as mentioned in MOEF&CC Notification 25/06/2014.





2006.

Project proponent shall prepare the draft EIA report covering the all above TOR and it shall be

submitted to the GPCB for conducting the public hearing / consultation process as per the

provisions of the EIA Notification, 2006.


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

8. SIA/GJ/IND2/21291/2017 M/s. Hans Met Industries Screening & Scoping

of 137


Page 39 of 137

Plot No 2, GIDC Dhrol Industrial Estate,Dhrol

361210,Dist.: Jamnagar, Gujarat.


Project status: New


dated 14/12/2017 regarding grant of Terms of Reference [ToR] for preparation of EIA/EMP

report.

• This is anew unit proposes manufacturing for Synthetic organic chemicals as tabulated below:

Sr. No.

Name of the Products CAS no. /CI no.

Quantity MT/Month

End-use of products

1 Haxachloroethane 67 – 72 – 1 280 MT/ Month

As degassing agent in foundry

2 Foundry flux (EC Not Applicable)

- 100 MT/ Month

Foundry Industries

3 Sodium Hypo Chloride (EC Not Applicable)

7681-52-9 75 MT/ Month By Product As disinfectant


2006.



project proponent.


Sr. no.

Particulars Details

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

B Total Plot area ( sq. meter) 554 Sq. m.

Green belt area,/Tree Plantation area ( sq. meter) 100 Sq. m.

C Employment generation 6 D Water i


GIDC

Status of permission from the concern authority.


Category KLD

(A) Domestic 0.1

(B) Gardening 0.1

(C) Industrial 0.0

Process 0.0

Washing 0.0

of 137


Page 40 of 137

Boiler 0.0

Cooling 0.0

Others 0.0

Industrial Total 0.0

Total (A + B + C) 0.2

1) Total water requirement for the project:0.2 KLD

2) Quantity to be recycle: W0.0 KLD



Category Waste water (KLD)

(A) Domestic 0.06

(B) Industrial 0.0

Process 0.0

Washing 0.0

Boiler 0.0

Cooling 0.0

Others 0.0

Total Industrial waste water 0.0

-

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

NA

v Mode of Disposal & Final meeting point Domestic: by Septic tank and Soak peat

Industrial: No Water Consumption

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

Not Applicable

Membership of Common facility (CF) NA

vii Reuse/Recycle details (KLD) NA

E Air


-

Sr.

no.

Source of

emission

With Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

Air Pollution

Control Measures

(APCM)

1 NA NA NA NA NA

NA

-

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

of 137


Page 41 of 137

-

Sr.

no. Source of emission

Type of

emission

Stack/Vent

Height (meter)

Air Pollution

Control Measures

(APCM)

1

In chlorination process

un reacted chlorine gas

in side reactor

Cl2

No process

Stack – Closed

loop process

Caustic Scrubber

-

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

• Identification of sources valve, pipes, joints, Pump seal and flanges.

• Fugitive emissions over reactors, formulation areas, centrifuges, chemical loading transfer area etc.

• For chlorine lead acetate paper checking the joint of pipes.

• Are yet to be collected through hoods and ducts by induced draft and controlled by scrubber / dust collector.

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

i

Sr. no.

Type/Name of Hazardous waste


Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Disposal Method

NA NA NA NA NA

ii Membership details of TSDF, CHWIF etc. NA

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

Empty barrels & Empty Gunny Bags. Supply to Users authorized by GPCB under Hazardous and Other Wastes (Management and Tran’s boundary Movement) Rules, 2016.



NA

ii VOC emission sources and its mitigation measures NA


under 5(f). It is mentioned that proposal is new.Considering the product profile, PP is asked to justify no

water consumption for industrial use. It is also noted that chlorination vessel is associated with alkali

scrubber however process vent is not proposed. PP is asked to explain methodology of scrubbing of

un-reacted chlorine and its subsequent handling with Sodium hypochlorite solution management.

Committee noted that none of the queries could be addressed by the PP satisfactorily.

of 137


Page 42 of 137

Considering above, committee unanimously decided to defer the proposal in one of the upcoming

SEAC meeting and asked PP to come prepared for the aforementionedproposal.

9. SIA/GJ/IND2/21188/2017 M/s. Riddhi Pharma

Plot No. 6120/2, GIDC Estate Ankleshwar– 393

002, Dist. Bharuch, State: Gujarat, India

Screening & Scoping





report.


as tabulated below:

Sr. no.

Name of the Products CAS no. / CI

no.

Quantity MT/Month

End-use of the products

Existing Proposed Total

(A) SPRAY DRYING PRODUCTS

1. Basic Chromium Sulphate (Powder)

39380-78-4 2 X 500

Kg/h --

1000 Kg/h

Dyes & Leather Tanning

2. Para Aluminum Chloride 7446-70-0 -- 200 MTM 200

MTM Water Treatment

(B) API & API INTERMEDIATES

1. 4-Amino 1,2,4 Triazole 584-13-4 -- 40.0 40.0 Fluconazole

2. Basic Chromium Sulphate (Powder)*

39380-78-4 -- 250.0 250.0 Dyes & Leather

Tanning

3. Beflubutamid (FMB) 113614-08-7 -- 15.0 15.0 Fine Chemical

4. 2-Amino-3,5-Dibromo Benzaldehyde (ADBA)

50910-55-9 -- 25.0 25.0 Ambroxol HCL

5. Trans-4-Aminocyclohexanol 27489-62-9 -- 5.0 5.0 Ambroxol HCL

6. Ambroxol Base 18683-91-5 -- 5.0 5.0 Ambroxol HCL

7. Menadione Sodium Bi Sulfite/ Vitamin K3

130-37-0 -- 15.0 15.0 Poultry Feeding

8. 1,3-Dichloro Acetone 534-07-6 -- 75 75 Famotidin /

of 137


Page 43 of 137

Nizatidin

9. Mono Bromo Acetic Acid 79-08-3 -- 5.0 5.0 Fine Chemical

10. 1-H-1,2,4 Triazole 288-88-0 --

200.0 200.0 Fluconazole 11.

1-H-1,2,4 Triazole salt (Na salt)

41253-21-8 --

12.1-H-1,2,4 Triazole salt (K salt)

41253-23-0 --

13. Acetophenone 98-86-2 -- 10.0 10.0 Fluconazole

14.Methyl Magnesium Chloride In THF/ Diethyl Ether 3.0 M Solution

676-58-4 -- 10.0 10.0 Montelucast

15.2-Phenoxy Methane Sulphonamide

51765-51-6 -- 5.0 5.0 Nimesulide

16.1-(2,4-Difluorophenyl)-2-(1H-1,2,4-Triazol-1-yl) Ethanone ( DFTA)

86404-63-9 -- 10.0 10.0 Fluconazole

17.

1[-2-(2,4-Difluorophenyl)-2,3-Epoxy Propyl]-1h-1,2,4-Triazole Methane Sulfonate (DFTA EPOXY MESYLATE)

86386-77-8 -- 7.0 7.0 Fluconazole

18.1-(3-Carboxy Pyridyl)-2-Phenyl-4-Methyl Piperazine (Acid)

61338-13-4 -- 3.0 3.0 Metrazepine

19.1-(3-Hydroxy Methylpyridyl-2) -2-Phenyl-4-Methylpiperazine (Alcohol)

61337-89-1 -- 3.0 3.0 Metrazepine

20.1-[4-(chloromethyl)-1,3-thiazol-2-yl]-N,N-dimethyl lmethanamine.2HCl (NI-4)

140176-73-4

-- 5.0 5.0 Nizatidin

21.

4-(2-Aminoethyl) Thiomethyl-2 DimethylaminomethylThiazole (NI-5)

78441-62-0 -- 5.0 5.0 Nizatidin

22.2-[4-(4-chlorobutanoyl) phenyl]-N,N,2-trimethyl propanamide (FEXO-3)

-- -- 15.0 15.0 Fexotidine

23.

1-[4 (Cyclopropylcarbonyl) Phenyl]1-Methylpropionic Acid Cyclohexylamine Salt (FEXO-6)

1690344-90-1 -- 10.0 10.0 Fexotidine

24.1-[4-(Chloromethyl)-1,3-Thiazol-2yl]Guanidine (FIT)

69014-12-6 -- 4.0 4.0 Famotidin

25.

IsoThiourea- [(S)-((2-Guanidino-4-Thiazolyl) MethylisothioureaDihydrochloride] (ITU)

88046-01-9 -- 4.0 4.0 Famotidin

of 137


Page 44 of 137

26.N-Sulphamyl-3-Chloropionamidine Hydrochloride (IFM)

106649-95-0 -- 3.0 3.0 Famotidin

27.2,2-Bis-(1-H-1,2,4-Triazole-1-yl-Methyl)-1,3-Dioxolane [DCDO-2]

Intermediate so no CAS no.

-- 1.6 1.6 Fine Chemical

28.1,3-Bis (1H-1,2,4-triazole-1-yl)propan-2-one [DCDO-3]

-- -- 1.0 1.0 Fine Chemical

29. 3-Amino-1,2,4-Triazole 61-82-5 -- 15.0 15.0 Anti Fungal

30. 3, 3-Diphenyl Propionitrile 2286-54-6 -- 3.0 3.0 Fine Chemical

31.Trans, trans 2,4-Hexadienyl Acetate

1516-17-2 -- 10.0 10.0 Fine Chemical

32. AP-200 Acetate 53880-51-6 -- 8.0 8.0 Fine Chemical

33. Meloxicam 71125-38-7 -- 2.0 2.0 API

34. Piroxicam 36322-90-4 -- 2.0 2.0 API

35. Mefenamic Acid 61-68-7 -- 10.0 10.0 API

36. Fluconazole 86386-73-4 -- 3 3 API

37. Ambroxol Hydrochloride 23828-92-4 -- 5.0 5.0 API

38. R & D Product -- -- 10.0 10.0 Fine Chemical

Total (Excluding Basic Chromium Sulphate)

0 549.6 549.6


2006.



Sr. no.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing: 1 crore Proposed: 8.99 Crores Total: 9.99 Crores

B Total Plot area ( sq. meter)

Existing: 6674.70 Sq. m. Proposed: This is an existing plot. Total: 6674.70 Sq. m.

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

Existing: 100 Sq. m. Proposed: 2103 Sq. m. Total: 2203 Sq. m.

C Employment generation Existing: Contract Labour: 7 nos. Proposed: Permanent: 50 Nos. + Contract Labour: 43 Nos. Total: Permanent: 50 Nos. + Contract Labour: 50 Nos.

D Water

of 137


Page 45 of 137

i


GIDC


As per CTO, Industrial = NIL Domestic = 6 KL/day


Requirement (In KL / day)

Existing

as per

CTO

Additiona

l for

expansio

n

Total after

Proposed

Expansion

Available

from

Recycle

Total fresh water

requirement after

Proposed

Expansion

(i)

Domestic :

6.0 4 10

-- 10

(ii)

Industrial :

(a) Process

: NIL 25 25 -- 25

(b) Boiler : NIL 12 12 -- 12

(c) Cooling : NIL 40 40 -- 40

(d) Washing

: NIL

*(Note 1) *(Note 1) -- *(Note 1)

(e) Gardening

: NIL 6 + 7.2 =

13.2 13.2 7.2 6

DOMESTI

C : 6.0 4 10

-- 10

INDUSTRI

AL : NIL 90.2 90.2

7.2 83

TOTAL : 6.0 94.2 100.2 -- 93

*Note 1: Utility blow down water (Boiler: 2 KLD + Cooling tower: 3 KLD = 5 KLD) shall be directly reused for washing purpose.

of 137


Page 46 of 137



3) Total fresh water requirement: 93 KLD


Category Existing

KLD

Proposed (Additional)

KLD

Total after Expansion

KLD Remarks

(A) Domestic

4.2 3 7.2

Sewage shall be disposed to STP (10 KLD) & treated water shall be used for Green belt development & maintenance

Industrial

Process NIL 22 22 Industrial effluent shall be treated in own ETP consisting of Primary & Tertiary treatment and treated water shall be sent to CMEE of M/s. BEIL, Ankleshwar.

Washing NIL 5 5

Boiler NIL *(Note 2) NIL

Cooling NIL *(Note 2) NIL

Others -- -- -- --


4.2 30 34.2

-*Note 2: Utility blow down water (Boiler: 2 KLD + Cooling tower: 3 KLD = 5 KLD) shall be directly reused for washing purpose and then shall be sent to ETP for further treatment.

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

ETP Capacity = 40 KLD (Consisting of Primary and Polishing Treatment.) STP Capacity = 10 KLD (Based on MBBR Technology)

v Mode of Disposal & Final meeting point Domestic: Sewage shall be disposed to STP (10 KLD) & treated water shall be used for Green belt development & maintenance

Industrial: Industrial effluent shall be treated in own ETP consisting of Primary & Tertiary treatment and treated water shall be sent to CMEE of M/s. BEIL, Ankleshwar.


Name of CF: CMEE of M/s. BEIL, Ankleshwar

Membership of CF The unit is under process of obtaining membership.

vii Reuse/Recycle details (KLD)

Refer point no. D (ii) & (iii)

E Air[Existing & Proposed]


of 137


Page 47 of 137

SR. no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1

(Existing)

Hot Air

Generator

(1no.)

1 unit

12 Natural

gas 80 Nm3/ h

PM

SO2

NOX

Dust Collector

2

(New)

OR

Boiler (1

no.)- 3 TPH

12 Natural

gas

260

Nm3/hr

Since Natural gas is used as fuel, no APCM is required.

Boiler (1

no.)(stand

by)- 1 TPH

90 Nm3/hr

3

(New)

Multi Fuel

Boiler (1

No.)- 2 TPH

15

Coal

OR

300 Kg/h

OR Multi Cyclone +

Bag filter+ Water Scrubber

Briquett

e 600 Kg/h

4

(New)

Thermic

Fluid Heater

(1 No.)- 3

Lakh Kcal/h

12 Natural

gas 50 Nm3/hr

Since Natural gas

is used as fuel, no

APCM is required.

5

(New)

DG Sets (1

No.)

(Standby)-

200 KVA

9 Diesel 40 L/h --

6

(New)

DG Sets (1

No.)

(Standby)-

750 KVA

9 Diesel 150 L/h

--

-

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

-

of 137


Page 48 of 137

Sr. no. Source of emission Type of

emission

Stack/Vent

Height

(meter)

Air Pollution

Control Measures

(APCM)

1. (Existin

g)

Spray Dryer (2 nos.)

(Capacity – 500 Kg/h) SPM 12 Ventury Scrubber

2. (New)

Process Emission Vessel (Mono

Bromo Acetic Acid)

HCl 11 2- Stage Water

Scrubber (1 no.)

Process Emission Vessel

(Acetophenone)

Process Emission Vessel (1-(2,4-

Difluorophenyl)-2-(1H-1,2,4-

Triazol-1-yl) Ethanone ( DFTA))

Process Emission Vessel

(Mefenamic Acid)

3. (New)

Process Emission Vessel (1-[4-

(chloromethyl)-1,3-thiazol-2-yl]-

N,N-dimethyl lmethanamine.2HCl

(NI-4)) HCl

SO2

Cl2

11 Water + Caustic

Scrubber (1 no.) Process Emission Vessel (2-[4-

(4-chlorobutanoyl) phenyl]-N,N,2-

trimethyl propanamide (FEXO-3))

Process Emission Vessel (AP-

200 Acetate)

-

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

Fugitive emission shall remain within permissible limit as handling of chemicals will be in closed system.

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

i

Sr. no.



Category and Schedule as

per HW

Quantity (MT/Annu

m) Disposal Method

of 137


Page 49 of 137

Rules.

1.

Empty barrels/ Containers/ Liners contaminated with

hazardous chemicals/ wastes

From Raw material

containers/ bags/ Drums

Schedule: I Category:

33.1

62 MT (Bags & Liners) & 366 MT (Drums)

Empty barrels/ Containers/ Liners/ Drums/ Bags - Sent to GPCB authorized dealer.

2. Used or Spent oil From

Machinery Schedule: I

Category: 5.1 0.096 MT

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

3. Process Residue

and wastes From

Process


28.1 50 MT

Process residue- Sent to CHWIF of M/s. BEIL, Ankleshwar.

4. Chemical sludge from waste water

treatment From ETP


35.3 80 MT

ETP Sludge - Sent for land filling at TSDF site of M/s. BEIL, Ankleshwar.

5. Off specification

products

From manufacturing process


28.4 36 MT

Off Specification Products/ raw material OR Failed batch - Sent for co-processing OR to CHWIF of M/s. BEIL, Ankleshwar

6. Potassium Bromide From

Process -- 115 MT

Potassium Bromide- 10-12% - Disposal by sell out to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste.

7. Manganese Oxide From

Process -- 80 MT

Manganese Oxide - Disposal by sell out to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste.

8.

Halogen-Containing compounds which

produce acidic vapours on contact

From Process

Schedule: II Category:

B10 1705 MT

25%- Spent Aluminium chloride solution - Disposal by sell out to

of 137


Page 50 of 137

with humid air or water e.g. slicon

tetrachloride, aluminium chloride,

titanium tetrachloride

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

9. Potassium Iodide

Solution From

Process -- 330 MT

Potassium Iodide Solution-8-9% - Disposal by sell out to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste.

10. 28-32% Sodium

Bisulphite (Sodium salt) Solution

From Process

-- 300 MT

28-32% Sodium Bisulphite (Sodium salt) Solution - Disposal by sell out to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste.

11. Ammonium Sulphate From

Process -- 75 MT

Ammonium Sulphate-10% - Disposal by sell out to authorized users who are having authorization with valid CCA and rule 9 permission to receive this waste.


ii Membership details of TSDF, CHWIF etc. The unit is under process of obtaining membership.

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

Ash = 790 MT, Generation from - Coal / Briquette combustion Disposal - Collection, Storage and sale to brick manufacturers.



Following are the solvents which shall be used for production: Methanol, Acetone, Isopropanol, Tetrahydrofuran, Ethylene dichloride, Toluene, Dimethyl aniline, Acetonitrile, Methylene

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Page 51 of 137

dichloride, Dimethyl formamide, Ethyl acetate, Mono ethylene glycol, Chloroform, N- Methyl Pyrrolidone, O-Xylene, Ethylene chloride Approximately 95-98 % of solvent recovery shall be carried out and will be reused.

Ii VOC emission sources and its mitigation measures

Handling of chemicals will be in closed system. Primary and secondary condensers are proposed.


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

existing conditions of CCA, details of public complaints/public litigation if any and action initiated by the

GPCB against the industrial unit which was replied by the PP. Committee satisfied with the reply of PP.

During presentation, water consumption, waste water generation and final management of treated

waste water were discussed at length.Industrial effluent will be treated in own ETP consisting of

Primary, Tertiary treatment and treated water shall be sent to CMEE of M/s. BEIL, Ankleshwar. PP

asked to verify compliance of 18(1) b direction of CPCB and asked details of condensate being handled

by BEIL from MEE. Further, it is noted that PP has sought 10 MTPM of R& D products and unit

processes are not addressed for R&D products. It is also asked to reduce quantum of R&D

products.Industrial unit is located in GIDC, Ankleshwar which is existing prior to EIA Notification 2006

and hence it is decided to exempt public hearing for the aforementioned proposal.




specific TOR.

1. To verify handling of condensate generating from common MEE of BEIL and its detail

management.

2. To define unit processes involved in R & D Products keeping proposed product group in

view.

3. To reduce quantity of R & D products keeping proposed product groups in view.





of 137


Page 52 of 137

2006.


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

10. SIA/GJ/IND2/21326/2017 M/s. VIHITA DRUGS & INTERMEDIATES

(Plot No. C1B/4754, Nr. FikomChowkadi, GIDC

Industrial Estate, Ankleshwar – 393002, Dist –

Bharuch, State: Gujarat)

Screening & Scoping


Project status: New



report.


as tabulated below:

Sr. no.

Name of the Products CAS no. /

CI no.

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

1 Mebendazole 31431-39-7 1.00 -- 1.00 Bulk Dugs

Intermediates

2 2-(2-Methoxy Phenoxy) Ethyl Phthalimide

26646-63-9

-- 10.00 10.00 Bulk Dugs

Intermediates

3 2,4-Dimethoxy Benzoic Acid 91-52-1

4 2,5-Dimethoxy Benzoic Acid 2785-98-0

5 2-[(2-Methoxy Phenoxy) Methyl] Oxirane

2210-74-4

6 2 - Bromo-2 – 5 - DimethoxyAcetophenone

93-07-2

7 2-Bromo 4, 5 - Dimethoxy Benzoic Acid

6286-46-0

8 2-Bromo 4, 5 - Dimethoxy Benzyl Bromide

53207-00-4

9 2-Bromo-3 – 4 - DimethoxyAcetophenone

1835-02-5

10 2-Methyl 2-Oxazoline 1120-64-5

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Page 53 of 137

11 3,4-Diethoxy Benzoic Acid 5409-31-4

12 3,4-Dimethoxy Acetophenone 93-07-2

13 4-Bromo Veratrole 2859-78-9

14 4-Methyl Catechol 452-86-8

15 4-Methyl Catechol Dimethyl Acetate

52589-39-6

16 5-Bromo-2-Chloro Benzoic Acid 21739-92-4

17 5 – Bromo – 2 – Chloro – 4 - EthoxyBenzophenone

461432-22-4

18 6-Nitro Veratric Acid 4998-07-6

19 Diacetone Fructose Pyranose 20880-92-6

20 Sesamol 533-31-3

21 Veratric Acid 105-13-5


2006.



project proponent.


Sr. No

Particulars Details

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

Existing: 1.50 Crore

Proposed: 2.7395 Crore

Total: 4.2395

B Total Plot area

( sq. meter)

Existing: 700.00 Sq. m.

Proposed: -- Sq. m.

Total: 700.00 Sq. m.

Green belt area,/Tree Plantation area

( sq. meter)

Existing: 135.00 Sq. m.

Proposed: 96.00 Sq. m.

Total: 231.00 Sq. m.

Employment generation

Existing: 10

Proposed: 12

Total: 22

D Water

i

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

GIDC, Ankleshwar


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Page 54 of 137


Existing

KLD


KLD


KLD

Remarks

(G) Domestic 1.00 Nil* 1.00 --

(H) Gardening 0.55 3.15 3.70 --

Industrial

Process 1.40 13.50** 14.90 --

Washing 0.25 0.50 0.75 --

Boiler 1.55 -- 1.55 --

Cooling 0.25 2.75 3.00 --

Others -- 1.45# 1.45 Water Consumption

in Scrubber

Industrial Total 3.45 18.20 21.65

Grand Total (A+B+C)

5.00 21.35 26.35

1. Total water requirement for the project: 26.35 KLD 2. Quantity to be recycle: -- KLD 3. Total fresh water requirement: 26.35 KLD

Note: * Granted quantity is sufficient after addition of proposed products. ** Maximum water consumption takes in product no. 15 (i.e. 5-Bromo-2-Chloro Benzoic Acid). # Maximum scrubber water consumption takes place in product no. 9 (i.e. 2-Methyl 2-Oxazoline).


Category Existing

KLD


KLD


KLD

Remarks

(E) Domestic 1.00 Nil* 1.00 --

Industrial

Process 1.79 13.46** 15.25 --

Washing 0.25 0.50 0.75 --

Boiler 0.95 -- 0.95 --

Cooling 0.01 0.14 0.15 --

Others -- 1.35*** 1.35 Waste Water

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Page 55 of 137

Generation in Scrubber


3.00 15.45 18.45

-Note:

* Granted quantity is sufficient after addition of proposed products.

** Maximum waste water generation take in product no. 15 (i.e. 5-Bromo-2-Chloro Benzoic Acid).

*** Maximum scrubber waste water generation take place in product no. 16 (i.e. 5-Bromo-2-Chloro-4-Ethoxy Benzophenone).

iv

Treatment facility within premises with capacity

[ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc].

Existing:

ETP: 17.50 m3/day (Primary Treatment). Industrial wastewater generated from manufacturing process and other ancillary operation shall be allowed into in-house ETP for primary treatment. Treated water will be sent to M/s. NCTL for its further treatment and final disposal. Proposed: ETP: 18.50 m3/day (Primary Treatment). Industrial effluent after primary treatment into ETP, it is esteemed that 3.00 m3/day of waste water is disposed to CETP of M/s. ETL after getting prior permission from GPCB, as we have already permission for only 3.00 m3/day for disposal in CETP. For proposed quantity (15.45 m3/day), it will be allowed in to in-house ETP for primary treatment. Then primary treated water will be sent to common MEE facility M/s. Ankleshwar Cleaner Process Technology Centre Ltd. (ACPTCL) for final disposal.


Domestic: Septic Tank / Soak Pit.

Industrial: In-house ETP for primary treatment and after CETP & Common MEE of M/s. ACPTCL, Ankleshwar.

vi

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

At present existing quantity of primary treated water is sent to CETP of M/s. NCTL. After expansion existing quantity of primary treated water will sent to CETP of M/s. ETL after getting prior permission of GPCB. Proposed quantity is sent to common MEE facility M/s. Ankleshwar Cleaner Process Technology Centre Ltd. (ACPTCL) for final disposal

Membership of CF We will get membership of CF after getting EC but before starting of production.

vii Reuse/Recycle details (KLD) --

E Air [Existing & Proposed]

i

Flue gas emission details

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

-

SR.

No.

Source of

emission

Stack

Height

Type of

Fuel

Quantity

of Fuel

Type of

emissions i.e.

Air Pollutants

Air Pollution

Control

Measures

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Page 56 of 137

With Capacity (meter) MT/Day (APCM)

Existing

1

Industrial Boiler

(Capacity: 800

Kg/Hr)

11 m Natural

Gas

400

m3/day

PM

SO2

NOx

Not Required

Proposed

2

Thermic Fluid

Heater (Capacity:

5.0 Lac Kcal/Hr)

15 m Natural

Gas

900

m3/day PM

SO2

NOX

Not Required

3

D. G. Set – 01 Nos.

(Stand by)

(Capacity: 250 KVA)

7 m HSD 68 Lit/hr

-

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

[Existing & Proposed]

-

Sr.

No.

Source of

emission

Type of

emission

Stack/Vent

Height (meter)

Air Pollution Control

Measures (APCM)

Existing

1 Reaction

Vessels-1

SO2

HCl

Chlorine

Ammonia

H2S

11 m Scrubber

Proposed

2 Reaction

Vessels-2 NH3

10 m

Alkali Scrubber

3 Reaction

Vessels-3

SO2

HCl Water Scrubber

Note: NH3 gas generated from reaction column will be scrubbed into acid scrubber by using H2SO4 and generated Ammonium Sulphate solutions recovers as a by- product. HCl generated from reaction column will be scrubbed into water scrubber. Generated Dil. HCl solution recovers as a by-product.

iii Fugitive emission details with its mitigation measures.

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Page 57 of 137

[Existing & Proposed]WAs below:

Suction hood with ID fan will be provided at production & raw material storage area for suction of any fugitive emission and diverted it to alkali / caustic scrubber.

F

Hazardous waste

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

I

Sr. No.



Category and Schedule as

per HW Rules.

Quantity

(MT/Annum)

Disposal Method

1

Empty Barrels / Containers / Liners Contaminated with Hazardous Chemicals / Wastes

Effluent Treatment

Plant 33.1 2.50

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

2 Chemical Sludge from Waste Water Treatment

MEE 35.3 5.00

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

3 Used or Spent Oil Process 5.1 0.15

Collection, Storage, Transportation & Disposal by reuse in plant & machinery as lubricant or sell it to authorized re-refiners / recyclers.

4 Distillation Residue

Process 36.1 47.00

Collection, Storage, Transportation and Disposal at TSDF site – for incineration.

5 Aluminum Chloride

Process (By-

Products) --

828.00

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

6 Dil. HCl Solution 264.00

7 Zinc Chloride 192.00

8 Ammonium Sulphate

648.00

9 Sodium Bromide Solution

1716.00

10 Sodium Sulphate 66.00


ii Membership details of TSDF, For existing, 4 KLD of effluent permission from CETP of M/s.

of 137


Page 58 of 137

CHWIF etc. NCTL, 0.36 MT/year of incineration waste permission from CHWIF of M/s. BEIL, 02 MT/year of solid waste disposal permission from TSDF of M/s. BEIL. Unit is also member of M/s. ACPTCL, Ankleshwar, for common MEE. For proposed project activity, unit will get TSDF membership after getting EC & before start of proposed production.


Sr.

No. Type of Waste

Source of

Generation

Category of

Waste Disposal

1. Construction

Waste

Proposed

construction

activity

-

Construction waste generated will

be stored at one identified place

and sold off to recyclers.

2.

Domestic Waste

(Food waste,

Plastic, Paper etc.)

Employees

working in the

premises

MSW Collected in separate bin and

disposed to bin of GIDC.

3. E-waste Entire Plant --

Collection, Storage and disposal

to M/s. Earth E-Waste

Management Pvt. Ltd., Surat


i

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

In house solvent recovery plant will be installed and recovered solvent will be again reuse in process and waste residue will be send to TSDF site for incineration.

More than 96 % of solvent will be recovered from recovery plant.

ii VOC emission sources and its mitigation measures

VOC generated from solvent storage area and control of VOC by Carbone tower.






waste water were discussed at length.After expansion,18.50 m3/day waste water will be

generated.Industrial effluent after primary treatment into ETP,3.00 m3/day of waste water will be

disposed to CETP of M/s. ETL as per CCA andproposed quantity of 15.45 m3/day will be treated within

premises and will be sent to common MEE facility M/s. Ankleshwar Cleaner Process Technology

Centre Ltd. (ACPTCL).Industrial unit is located in GIDC, Ankleshwar which is existing prior to EIA

of 137


Page 59 of 137

Notification 2006 and hence it is decided to exempt public hearing for the aforementioned proposal.




specific TOR.

1. Detailed Leak Detection and Repairing Programme (LDAR)for volatile organic solvents proposed in house with detailed chemical properties including vapor pressure. LDAR shall endeavor prevention of losses of solvents to the best minimum extent.





2006. The project proponent shall have to apply for Environmental clearance through online portal


11. SIA/GJ/IND2/21430/2017 M/s. Harsiddhi Organics Pvt. Ltd.

124/25-26, GIDC, Nandesari, Vadodara –

391340

Screening & Scoping



• PP has submitted online application vide no. SIA/GJ/IND2/21430/2017 dated 01/01/2018 for

obtaining Environmental Clearance.


as tabulated below:

Sr. no

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

1 REACTIVE BLUE H5G 12236-87-2 09 -- 09

2 Solvent Dyes -- 40 40 Dyes

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Page 60 of 137

2 Aliphatic Bromide (n-Propyl Bromide, Di Bromo Ethane, Bromo Acetic Acid)

106-94-5, 106-93-4, 79-08-3 etc

--

300

300

Pharmaceuticals / Pesticide

3 Aromatic Bromide (Bromo Aniline, BromoBenzaldehyde, Bromo Benzoic Acid etc.)

591-19-5, 1122-91-4, 586-76-5 etc

--


2006.



Sr. no.

Particulars Details


(Rs. in Crores):

Existing: 1.27 Cr Proposed: 2.0 Cr Total: 3.27 Cr

(1) Capital cost for EMS (Environmental Management System):...0.45.Crores

(2) Recurring cost towards the environmental protection measures:...0.65.Crores per

Annum.


Existing: 1520 Proposed: -- Total: 1520


Existing: 200 Proposed: 300 Total: 500


1. Direct Existing:25 Proposed: 35 Total: 60

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

D Water i


GIDC Water Supply



Existing KL/day



(A) Domestic 5.0 5.0 10.0

(B) Gardening 5.0 - 5.0

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Page 61 of 137

(C) Industrial

Process 4.7 49.7 54.0

Washing 1.0 1.5 2.5

Boiler 10.0 6.5 16.5

Cooling 4.3 7.7 12.0

Others

Total (A+B+C) 30 110.0





(A) Domestic 4.0 4.0 8.0

(B) Industrial

Process 59.7 26.3 86.0

Washing 1.0 1.5 2.5

Boiler 2.6 0.4 3.0

Cooling 1.2 0.3 1.5

Others


68.5 101.0


100 KL/day capacity ETP will be constructed


Domestic: Soak Pit

Industrial: CETP, Nandesari

vi Reuse/Recycle details (KL/day) Not Applicable

vii Details of rain water harvesting Not allowed in GIDC

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


-

SR

.

no

.

Source of

emission

With Capacity

e.g. Boiler (8

TPH)

Stack

Height

(meter

)

Name

of the

fuel

Quantity of

Fuel

MT/hr&

MT/Day

Type of

emissions

i.e. Air

Pollutants

APCM

1 Existing Boiler

(0.6 TPH) 10 mts

Wood

/LDO 1.5 MT/day SO2, NOx,

PM -

2 Steam Boiler

(Existing) 30 mts

Agro

Waste 2 MT/day SO2, NOx,

PM Cyclone

3 Steam Boiler 30 mts Agrowa 5 MT/day / SO2, NOx,

PM Cyclone

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Page 62 of 137

(Proposed) 4TPH ste /

Coal

1.75

MT/day

+ Bag

filter

4 DG Set (250 KVA)

- Proposed 3 mts HSD 20 Lts/hr SO2, NOx,

PM --

-

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

-

Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height

(meter)

APCM

1 Scrubber

(Exisiting)

Bromine,

Cl2, HCl 6 mts

Water scrubber

followed by Caustic

Scrubber

2 Scrubber

(Proposed) Bromine 6 mts

Water scrubber

followed by Caustic

Scrubber

-

iii Fugitive emission details with its mitigation measures. [Existing & Proposed] - All reactions are taken under closed condition


i

Sr. no.




Quantity (MT/Annum)

Disposal Method

1 ETP Sludge ETP 35.3 1500 MT/Yr TSDF, NECL

2 Used Oil Gear Box 5.1 2.5 MT/Yr To registered recyclers or TSDF, NECL

3 Liner Bags Raw material

33.1 5 MT/Yr Used to fill ETP Sludge or sold to srap dealers



Membership of CETP and TSDF Taken

iii Details of Non-Hazardous waste & its disposal NA

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Page 63 of 137

(MSW and others)


i Details of Solvent recovery (As per respective ToR) MCB/O-xylene will be recovered by distillation

ii VOC emission sources and its mitigation measures Vent Condensors are proposed






waste water were discussed at length.After expansion, Industrial effluent after treatment will be sent to

CETP.Industrial unit is located in GIDC, Nandesari which is existing prior to EIA Notification 2006 and

hence it is decided to exempt public hearing for the aforementioned proposal.




specific TOR.

1. To address applicability and compliance Ozone Depleting Substances(Regulation and Control) Rules, 2000 keeping proposed product in view.

2. Detailed Leak Detection and Repairing Programme (LDAR) for volatile organic solvents proposed in house with detailed chemical properties including vapor pressure. LDAR shall endeavor prevention of losses of solvents to the best minimum extent.

3. Detailed hazardous waste management including bleed liquor management( Saturated

scrubbing media) as per Hazardous and other waste (Management and Transboundary) Rules

2016.





2006.



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Page 64 of 137

12. SIA/GJ/IND2/21420/2017 M/s. Ascent Fine Chem (P) Ltd.

Plot No. 273A & B, 272/5/P/1-2 & 493, Phase –

II, GIDC Vatva, Ahmedabad-382445

Screening & Scoping






as tabulated below:

Sr. no.

Name of the Products CAS no. / CI no.

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

Existing Proposed Total

1. 4-Methoxy benzaldehyde [Anisaldehyde]

123-11-5 2.0 68.0 70.0

To be used as a Flavor & Fragrance ingredient and as a key starting material in the Performance chemicals industry. It may be also used in Synthesis of Organic Chemicals in the Pharmaceuticals and API applications

2. 4-Methoxy benzalalcohol [Anisyl alcohol]

105-13-5 30.0 --- 30.0

3. 4-Methoxy benzal acetate/formate [Anisyle Acetate/Formate]

104-21-2 0.5 2.1 2.6

4. 4-Methoxy benzalammine [4-MBA]

2393-23-9 0.5 --- 0.5

5. 4-Methoxy methyl benzene [PVME]

1515-81-7 1.0 --- 1.0

6. 3-Benzyloxypropionitrile [BNPT]

6328-48-9 0.5 0.5 1.0

7. 4-Phenyl-2-Butanone [Benzyl Acetone]

2550-26-7 1.0 --- 1.0

8. 4-Acetoxy methyl benzene [Cresyl Acetate]

104-39-6 0.1 0.1 0.2

9. Aminopropyl imidazole [API] 5036-48-6 1.0 9.0 10.0

10. 1-Para Hydroxyphenyl-3-butanone [Raspberry ketone]

5471-51-2 0.5 9.5 10.0

11. 1-[Cyano (P- Methoxyphenyl) Methyl] Cyclohexanol (VNF-1)

93413-76-4 0.1 0.9 1.0

12. 1-(Para-Methoxyphenyl)-2-propanone [4-MPA]

122-84-9 0.5 14.5 15.0

13. 4-Methoxy phenyl acetonitrile [MPAN]

104-47-2 5.0 15.0 20.0

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Page 65 of 137

14. Anisole/Veratrole 91-16-7 1.0 1.0 2.0

15. 4-Methoxy phenylethylamine [Methyl Tyramine]

55-81-2 0.5 --- 0.5

16. 4-(Para-Methoxyphenyl)-2-butanone [Anisyl/Acetone]

104-20-1 0.5 --- 0.5

17. 1-Methoxy Phenyl acetic acid [PMPA]

7021-09-2 1.0 --- 1.0

18. 4-Methoxy Phenyl acetic acid 104-01-8 --- 15.0 15.0


19. 4-Hydroxy phenyl acetonitrile 14191-95-8 --- 1.0 1.0

20. 4-Benzyloxy phenyl acetonitrile 836-96-0 --- 0.5 0.5

21. 1-[2-Amino-1-(p-methoxyphenyl) ethyl]cyclohexanol Acetate [VNF-2 acetate]

839705-03-2 --- 1.0 1.0

22. 1-[2-Amino-1-(p-methoxyphenyl) ethyl]cyclohexanol HCl [VNF-2 HCl]

130198-05-9 --- 5.0 5.0

23. 1-[2-Dimethylamino-1-(4-methoxyphenyl)-ethyl]cyclohexanol HCl [VNF HCl]

9930078-4 --- 5.0 5.0

24. Venlafaxine Base 93413-69-5 --- 1.0 1.0

25. Para hydroxy phenyl Acetic acid

156-38-7 --- 0.5 0.5

26. Para Benzyloxy phenyl Acetic acid

6547-53-1 --- 0.1 0.1

27. Methyl 4-Hydroxy phenyl acetic acid (HPME)

14199-15-6 --- 0.1 0.1

28. Ethyl 4-Hydroxy phenyl acetic acid (HPEE)

14062-18-1 --- 0.1 0.1

29. 4-Hydroxy phenyl amine/base/salts [o-Methyl tyramine / Tyramine]

55-81-2/ 51-67-2

--- 4.0 4.0

30. N-(4-chloronenzoyl)Tyramine 41859-57-8 --- 0.5 0.5

31. Mebavarine amine 14367-46-5 --- 2.0 2.0

32. Para Anisyl acetone 104-20-1 --- 3.0 3.0

33. Para Anisoyl chloride 100-07-2 --- 2.0 2.0

34. Trimethoxydobutamine HCl(DBN-3)

51062-14-7 --- 0.5 0.5

35. 3,4-Dimethoxy phenyl acetonitrile [Homo veratronitrile]HVN

93-17-4 --- 2.0 2.0

36. Homo Veratryl Amine [HVA] 120-20-7 --- 2.0 2.0

37. 3,4 Dimethoxy phenyl aceticacid(DMPAA)

93-40-3 --- 0.5 0.5

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Page 66 of 137

38. 3,4-Dihydropapavarine HCl (DPH)

5884-22-0 --- 0.5 0.5

39. Octopamine hydrochloride 770-05-8 --- 3.0 3.0


40. KetoOctopamine Hydrochloride

77369-38-1 --- 0.5 0.5

41. Benzilidine acetone 122-57-6 --- 2.0 2.0

42. Benzyl Acetone 2550-26-7 --- 8.0 8.0

43. 2-Amino-4-phenyl butane 22374-89-6 --- 0.5 0.5

44. Indoline 496-15-1 --- 10.0 10.0

45. para Hydoxybenzyl alcohol 623-05-2 --- 2.0 2.0

46. Diethyl (thien-2-ylmethylene) malonate (ES-1)

---- --- 1.0 1.0

47. Diethyl (thien-2-ylmethyl)malonate (ES-2)

26420-00-8 --- 1.0 1.0

48. Ractopamine HCl 90274-24-1 --- 1.0 1.0

49. AminopropylCyclohexyl Amine 3312-60-5 --- 1.0 1.0

50. 4-Methoxy benzoic acid [Anisic acid]

100-09-4 --- 1.0 1.0

51. Para cresyl phenyl acetate 101-94-0 --- 1.0 1.0

52. Para cresyl methyl ether (PCME)

104-93-8 --- 10.0 10.0

53. Anisyl butyrate 6963-56-0 --- 0.2 0.2

54. Anisyl propionate 7449-33-9 --- 0.2 0.2

55. Canthoxal 5262-06-6 --- 1.0 1.0

56. Aldehyde C-14 104-67-6 --- 2.0 2.0

57. Aldehyde C-18 104-61-0 --- 2.0 2.0

58. Mugentanol 63737-86-2 --- 0.5 0.5

59. Majanntol 103694-68-4 --- 0.5 0.5

60. Normajantol 1009-62-7 --- 0.5 0.5

61. Florazone 67634-15-5 --- 0.5 0.5

62. Calone 28940-11-6 --- 0.5 0.5

63. Development products ---- --- 30.0 30.0

64. TOTAL 45.7 246.8 292.5

65. Glauber’s Salt – Liquid/Powder form equivalent (100% Basis)

100 MT/Month

---- 100

MT/Month

66. MnSO4 (Mangeneze sulphate) – Liquid/Powder form, equivalent (100% Basis)

500 MT/Month

100 MT/Mon

th

600 MT/Mont

h


2006.



of 137


Page 67 of 137

project proponent.


Srno

Particulars Details


(Rs. in Crores):

Existing: 23.9929 Proposed: 13.0000 Total: 36.9929


Existing: 9195 Proposed:1838 Total: 11033


Existing: 630 Proposed:200 Total: 830

C Employment generation Existing: Proposed: Total:

D Water

i

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

GIDC

Status of permission from the concern authority. ----


Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 2.0 2.0 4.0

(B) Gardening 2.0 --- 2.0

Process 3.5 28.5 32.0

Washing 18.5 -5.5 13.0

Boiler 3.0 5.0 8.0

Others (Cooling) 2.0 13.0 15.0

Industrial Total 27 41 68

Grand Total

(A+B+C) 31 43 74

1) Total water requirement for the project: 74 KLD

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Page 68 of 137




Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

(A) Domestic 1.5 1.5 3.0

Process 3 23 26

Washing 18.5 6.5 12

Boiler 0.6 0.4 1

Others (Cooling) 0.9 0.1 1

Total Industrial

waste water 23 17 40

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

Primary, Secondary & Tertiary Treatment , ETP Capacity: 40 KL


Domestic: Soak Pit

After proposed expansion, Industrial Effluent: 23.KL/Day

(quantity after proposed expansion) effluent generated

will be treated in existing Effluent Treatment Plant having

primary, secondary and tertiary treatment units and will

be sent to CETP. 17 KL/Day effluent will be sent to

common spray dryer facilities.


1)Green Environment Co. Operative Society Ltd. (CETP – Vatva) 2)GECSL-Vatva, Society for Clean Earth (Common Spray Drying Facility)

Membership of CF 1)Green Environment Co. Operative Society Ltd. (CETP)

vii Reuse/Recycle details (KLD) There is not reuse waste water in process.



-

of 137


Page 69 of 137

SR.

no.

Source of

emission

With Capacity

Stack

Height

(meter)

Type of

Fuel

Quantity of

Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

1 IBR Boiler (6 TPH) (Existing)

30 Agro waste or Castor DOC

10 MT/Month

SPM<150 mg/NM3

SO2<100

ppm

NOX<50 ppm

Multi Cyclone

Bag Filter

2 Thermic Fluid Heater(Existing)

30 Furnace oil

Exi: 1200 Prop:1200 Total: 0

Multi Cyclone

Bag Filter

3 Small Industrial Boiler(0.8 TPH)* Existing)

30 Natural Gas ---- ---

-*After expansion it will be dismantled


-

Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height (meter)

Air Pollution

Control Measures

(APCM)

1

Reaction vessel –

1

[EXISTING]

NH3<=175

mg/NM3 20 m Two stage Venturi

PP-FRP scrubber

2 Reaction vessel – 2 [PROPOSED]

HCl <= 20 mg/NM3

20 m Four stage Scrubber system

-


Sources of fugitive emissions include storage of chemicals, and solvents storage, loading and unloading section, raw material handling, hazardous waste storage area. Mitigation Measures Water shall be sprinkled during the construction - Mechanical seals for pumps etc. should be used and maintained. - Closed unloading, conveying and packing system - All the reactors shall be closed. - Safety devices shall be provided to workers - Raw material storage in closed storage area - Regular monitoring of solvents’ concentration in work zone.

F Hazardous waste

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Page 70 of 137

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

i Sr. no.




Quantity(MT/Annum) Disposal Method

Existing Proposed

Total after expansion

1. ETP Waste Effluent treatment plant

35.3 0.75

MT/Month

1.25 MT/Mont

h

2.0 MT/Mont

h

Collection, Storage, Transportation, Disposal, at TSDF site

2. Used Oil

Lubrication of plant machineries

5.1 0.2

MT/Month

0.3 MT/Mont

h

0.5 MT/Mont

h

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

3. Discarded Containers/ Liners

Raw material section

33.1 300

Nos./Month

700 Nos./Mo

nth

1000 Nos./Mo

nth

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

4. Distillation residue

During distillation process of Solvents

20.3 1.5

MT/Month

12.0 MT/Mont

h

13.5 MT/Mont

h

Collection, Storage, Transportation, Disposal by incineration at CHWIF site

5. Spent catalyst

During manufacturing process

35.2 180

Kg/Year 320

Kg/Year 500

Kg/Year

Collection, Storage and reuse within premises after regeneration.

6.

Contaminated cotton rags or other cleaning materials

From Process

33.2 ----- 100

Kg/Month

100 Kg/Mont

h

Collection, Storage, Transportation, Disposal by incineration at CHWIF site

7. Ammonia solution 10%:

From Process

--- --- 85

MT/Month

85 MT/Mont

h

Collection, Storage, Transportation, Disposal by selling to authorized user.

8. Hydrochloric acid 20%

From Scrubber

D2-Sch.II

--- 35

MT/Month

35 MT/Mont

h


9.

Glauber’s Salt Liquid/Powder form


--- 100

MT/Month

---- 100

MT/Month


of 137


Page 71 of 137

equivalent (100% Basis)

10.

MnSO4 (Mangeneze sulphate) – Liquid/Powder form, equivalent (100% Basis)


--- 500

MT/Month

100 MT/Mont

h

600 MT/Mont

h



ii Membership details of TSDF, CHWIF etc.

We are member of common TSDF site GEMSPL-Vatva


No any kind of Non-hazardous waste.



We have the facility for distillation & recovered solvent will be reuse in the Process. We will recover 95-98% solvent & it will be reuse back in the same process.


VOC emission may be through the vent of storage tanks & transferring of the solvents. The vents are connected with the seal pot. Most of the solvent are transferred through closed system through pipelines & pumps. So there are minimum source of VOC.






waste water were discussed at length.After proposed expansion, existing Industrial effluent of 23.KLPD

will be treated in existing Effluent Treatment Plant having primary, secondary and tertiary treatment

units and will be sent to CETP. Additional effluent load of 17 KL/Day due to proposed expansion will be

sent to common spray dryer facilities. As unit process include hydrogenation, details of safety aspect

for handling and utilization of hydrogen were deliberated. PP informed the methodology for

hydrogenation process stating removal of oxygen presence in the vessel.Industrial unit is located in

GIDC, Vatwa which is existing prior to EIA Notification 2006 and hence it is decided to exempt public

hearing for the aforementioned proposal.


of 137


Page 72 of 137



specific TOR.

1. Detailed Leak Detection and Repairing Programme (LDAR) for volatile organic solvents proposed in house with detailed chemical properties including vapor pressure. LDAR shall endeavor prevention of losses of solvents to the best minimum extent

2. To verify compatibility of water consumption keeping proposed expansion in a view.





2006.



13. SIA/GJ/IND2/21052/2017 M/s. Laakoona Reactions

Plot No. 56/B-2, Phase-I,GIDC-Vatva,Ahmedabad-382445.

Screening & Scoping



• PP has submitted online application vide no. SIA/GJ/IND2/21052/2017 dated 12/01/2018for



as tabulated below:

Sr. no.

Name of the Products CAS no. / CI

no.


1 D.A.S.A. (4-4 diaminosulphanilide)

1203494-49-8

10 0 10

Acid Dyes

2 FC Acid (4'4 Diamino, Diphenylamine, 2-Sulfonic Acid)

59-30-3 Direct Dyes

3 OAPSAMIDE (3 Amino - 98-32-8 0 40 40 Pigment

of 137


Page 73 of 137

4 hydroxybenzeneSulphonamide)

Intermediate

4

'N-[4-[[(4-aminophenyl)sulfonyl] amino] phenyl] acetamide

3366-61-8 Acid Dyes

5 Metanilic Acid (3 Amino benzene Sulphonic Acid)

121-47-1 Reactive dyes/OBA

6 sodium 5-amino-2-(4-aminoanilino) benzene sulphonate

85135-98-4

0 40 40

Direct Dyes

7 4 ADAPSA (4-Aminodiphenyamine-2-sulfonic acid)

91-30-5 Acid & Reactive Dyes

8 4 NADAPSA (4-Nitro, 4' Amino, Diphenylamine, 2-Sulfonic Acid)

91-29-2 Acid Dyes

9 6 CHLORO 4 NAP (6 - Chloro 4 - Nitro 2 - Amino Phenol) 37674-72-9

0 10 10

Acid Dyes

10

HEGN STAGE 2 (Diarylamino-3,6-dichloro-1,4-benzoquionone)

124448-55-1 Reactive dyes

11 4 NAPSA (4-Nitro-2-Amino Phenol-6-SulfonicAcid)

96-67-3 Acid Dyes

12 Reactive Blue 220 128416-19-3

0

50

50

Textile Dyes

13 Reactive Black B 60202-35-9 Textile Dyes

14 Direct Black 22 6473-13-8 Paper Dyes

15 Reactive Red 195 93050-79-4 Textile Dyes

16 Reactive Yellow 145 93050-80-7 Textile Dyes

17 Direct Red 239 60202-35-9 Paper Dyes

18 Acid Black 210 99576-15-5 Leather Dyes

19 Direct Black 19 6428-31-5 Paper Dyes

20 Reactive BLUE 19 -- Dying & Printing of cellulosic fiber

21 Reactive Yellow ED -- Dying & Printing of cellulosic fiber

22 Reactive Red ED -- Dying & Printing

23 PCOSA (Polycystic ovary syndrome)

120-71-8 0 40 40 Dyes and food color

of 137


Page 74 of 137

24 4 Acetyl Sulphonamide -- Dyes and food color

TOTAL 10 180 190

25 Spray drying of dyes 24

KL/Day 0

24 KL/Day


2006



project proponent.


Sr. no.

Particulars Details


Existing: 6.02 Crores Proposed: 1.10 Crores Total: 7.12 Crores


Existing: 2636 Sq. m. Proposed: 0 Total: 2636 Sq. m.


Existing: 245 Sq. m. Proposed: 100 Sq. m. Total: 345 Sq. m.

C Employment generation Existing: 25 Proposed: 25 Total: 50

D Water i


GIDC Bore well

Status of permission from the concern authority. No


Existing KLD


KLD


KLD

(A) Domestic 0.8 1.6 2.4

(B) Gardening 0 2 2

Process 2.68 69.82 72.5

Washing 3.4 2 5.4

Boiler 2.5 3.5 6

Scrubber 0.2 1 1.2


of 137


Page 75 of 137

Grand Total (A+B+C)

9.58 79.92 89.5





Category Existing KLD


KLD


KLD

(A) Domestic 0.6 1.5 2.1

Process 3.65 83.45 87.1

Washing 3.4 2 5.4

Boiler 0.25 0.35 0.6

Scrubber 0.2 1 1.2


7.5 86.8 94.3

-

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

ETP (Primary, Secondary)


Domestic: 2.1 KLPD Discharge to Soak Pit via Septic Tank.

Industrial: Industrial effluent generation will be 94.3 KLPD. It will be segregated as follows:

• Effluent reuse in process: 27.2 KLPD.

• 7.5 KLPD Effluent to ETP treat with Primary, Secondary & Tartary Treatment after achieving prescribed Norms send to CETP-Vatva

• 59.6 KLPD effluent send to ETP treat with Primary Treatment and then send to Common Spray Dryer for Spray Drying.


CETP – The Green Environment Service Co-op. Society Ltd. Common Spray Dryer –

1. The Green Environment Service Co-op. Society Ltd.

2. Society For Clean Earth-Vatva 3. Society For Clean & Green Earth - Naroda

Membership of CF

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

of 137


Page 76 of 137

vii Reuse/Recycle details (KLD)

27.2 KLD Waste Water Reuse in Manufacturing Process.

Sr. No.

Product Name Quantity

MT/Month

Waste Water Generation

KL/Day

Water Reuse KL/Day

Goes to ETP

1 FC Acid 10 10.03 2.67 7.36

2 OAPSAMIDE 40

19.06 5.33 13.73

3 Metanilic Acid 10.2 2.67 7.53

4

Sodium 5-amino-2-(4-aminoanilino) benzene sulphonate

40 24 14.67 9.33

5 6-Chlor 4-Nap

10

3.73 2 1.73

6 HEGN Stage 2 19.8 4.5 15.3

7 4-NAPSA 3.18 2 1.18

Total Water Reuse: 27.2 KL/Day



-

SR.

no.

Source

of

emission

With

Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

1

Boiler

(2 MT)

(Existing)

15

Bio

Coal/

Coal

0.38

Particulate

Matter

SOx

NOx

--

2

Hot Air

Generator

(600 kg

kcal)

(Existing)

11 PNG

0.24

SCM/Da

y

Particulate

Matter

SOx

NOx

--

3

Hot Air

Generator

(600 kg

11 LDO 8 Particulate

Matter --

of 137


Page 77 of 137

kcal)

(Existing)

SOx

NOx

-


-

Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution Control

Measures

(APCM)

1

Chlorosulp

honic

vessel

(Existing)

SOx

HCl

15

Venturi water

scrubber + Packed

column water

scrubber + Packed

column alkali

scrubber

2

Spray

Dryer

(1000

litter/day)

(Existing)

Particulat

e Matter 15

Cyclone separator +

Wet scrubber

-


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

i

Sr. no.


waste


Category and

Schedule as per HW

Rules.

Quantity (MT/Annu

m) Disposal Method

1 ETP Waste Effluent

treatment plant

35.3 180 Collection, storage, transportation, disposal at TSDF by Eco Care.

2 Used oil

Lubrication in plant

5.1 20 Collection, storage, reuse, disposal by selling to

of 137


Page 78 of 137

machineries registered recycler

3 Discarded containers & bags

Raw Material Section

33.1 35

Collection, storage, decontamination, reuse, transportation, disposal by selling to authorized recycler

4 Process waste (Iron Sludge)

From manufacturing Process

26.1 6378

Collection, storage, transportation, disposal at TSDF site and/or by selling to M/s. Ultratech cement ltd, Jafrabad, Dist: Amreli

5 Gypsum Sludge

From Manufacturing Process

-- 1500

Collection, storage, transportation, disposal at TSDF site and/or by selling to M/s. Ultratech cement ltd, Jafrabad, Dist: Amreli or any cement Co-Processing Unit.

6 Spent sulphonic acid

From manufacturing Process

26.3 15312 Collection, storage, transportation, disposal by selling to actual Rule-9 user (M/s. Shree Cement Beawer, Rajasthan., M/s. Gopinath Chem Tech, M/s. GautamInd. Corporation), reuse in manufacturing process & for further treatment send to NOVEL.

7 Spent hydrochloric acid

-- 60


Spent Sulphuric Acid Generation Product Wise

Sr. No.

Product Name Quantit

y

Spent Sulphuric

Acid Consumption

Spent Sulphuric

Acid Generation

Spent Sulphuric

Acid Reuse

MT/B

MT/M MT/B MT/M MT/B

MT/M

1 DASA 10

5 50 16 160 5 50

2 FC Acid 6 60 -- 6 60

3 OAPSAMIDE

40

4 160 10 400 4 160

5

'N-[4-[[(4-aminophenyl)sulfonyl] amino] phenyl] acetamide

0.6 24 15.6 624 0.6 24

of 137


Page 79 of 137

7 4 ADAPSA 40

3 120 -- -- 3 120

8 4 NADAPSA 2 80 -- -- 2 80

9 6-Chlor 4-Nap 10

2.5 25 -- -- 2.5 25

11 4-NAPSA 1.5 15 -- -- 1.5 15

21 Reactive Red ED 50 1 50 -- -- 1 50

23 PCOSA

40 -- --

12.23

489.21

-- --

24 4 Acetyl Sulphonamide

-- -- 12.3 492 -- --

Spent Hydrochloric Acid Generation Product Wise

Sr. No.


Spent Hydrochloric Acid Generation

MT/B MT/M

1 DASA 10

0.5 5

2 FC Acid --

Iron Sludge Generation Product Wise

Sr. No.

Product Name Quanti

ty

Iron Sludge Generation

MT/B MT/M

1 DASA 10

2 20

2 FC Acid 2 20

3 OAPSAMIDE

40

6 240

4 Metanilic Acid 2.55 102

5 'N-[4-[[(4-aminophenyl)sulfonyl] amino] phenyl] acetamide

2.5 100

6 Sodium 5-amino-2-(4-aminoanilino) benzene sulphonate

40

6 240

7 4 ADAPSA 1.5 60

8 4 NADAPSA 1.5 60

9 6-Chlor 4-Nap

10

10 HEGN Stage 2 3.15 31.5

11 4-NAPSA

TOTAL GENERATION 531.5 MT/Month

Gypsum Sludge Generation Product Wise

Sr. No.


Gypsum Sludge Generation

MT/B MT/M

1 Reactive Blue 19 50 2.5 125

ii Membership details of TSDF, CHWIF etc. TSDF – Eco Care-Sanand

iii Details of Non-Hazardous waste & its disposal NO

of 137


Page 80 of 137

(MSW and others)



No use of any type of solvent.


We will measure VOC level in our manufacturing unit as well as Raw Material Storage area we will also do work place monitoring & according implementation.






waste water were discussed at length.Industrial effluent generation will be 94.3 KLPD. Effluentquanity

to be reused reuse in process will be 27.2 KLPD Existing waste water quantity of 7.5 KLPD will be

treated in ETP having Primary, Secondary & Tertiary Treatment facility and will be discharged to CETP-

Vatva. Waste water from the additional products of 59.6 KLPD will betreated in ETP and finally sent to

Common Spray Dryer for Spray Drying. Industrial unit is located in GIDC, Vatwa which is existing prior

to EIA Notification 2006 and hence it is decided to exempt public hearing for the aforementioned

proposal.Considering the above project details, it was decided to recommend standard TOR for the

Synthetic Organic Chemical projects approved by SEIAA in its 12th meeting dated 16/09/2017 for the

EIA study to be done covering 10 Km radial distance from the project boundary including following

project specific TOR.

1. Feasibility report for spent sulfuric acid utilization within the premises in the processes with reference to the spent sulfuric acid quantity produced due to proposed expansion and management of its balanced quantity.





2006.



of 137


Page 81 of 137

14. SIA/GJ/IND2/21189/2017 M/s. ADITYAM INDUSTRIES

Plot No: C/1/126 Phase II, GIDC Vatva,

Ahmedabad

Screening & Scoping





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

as tabulated below:

Sr. no.



Non EC Product

1 Blending of so dyes -- 50 NIL 50 Actual User

EC Product

2 Reactive Yellow: M4G, H4G, ME2RL, FG, ME4GL

NIL 150 150 Textile and

Other actual User

3 Reactive Golden Yellow: MR, HR, MERL

4 Reactive Red: BS, ME4BL, HE3B,

5 Reactive Orange : 2R, 3R

6 Reactive Navy Blue : ME2RL

7 Reactive Magenta : MB, HB

8 Reactive Black: B, WNN,

9 Reactive Orange : M2R, H2R, ME2RL

10 Reactive Red: M5B, M8B, H8B, ME6BL, P2B

11 Reactive Blue: P3R

• The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification

2006



project proponent.


Sr. Particulars Details

of 137


Page 82 of 137

no.


(Rs. in Crores):

Existing: 0.25 Cr. Proposed: 1 Cr. Total: 1.25 Cr.


Existing: 703 Sq. m. Proposed: NIL Total: 703 Sq. m.


Existing: 15 Sq. m. Proposed: NIL Total: 15 Sq. m.

C Employment generation Existing:10 person Proposed:5 person Total:15 person

D Water i


GIDC Vatva



Category Existing

KLD


KLD


KLD Remarks

(A) Domestic 0.8 1.0 1.8

Water Consumption From GIDC Vatva (B) Gardening

Industrial

Process NIL 8.09 8.09

Washing NIL 1.0 1.0

Boiler NIL 4.0 4.0

Industrial Total NIL 13.09 13.09

Grand Total (A+B+C) 0.8 14.09 14.89


2) Quantity to be recycle; Nil

3) Total fresh water requirement 14.89 KLD


Category Existing

KLD


KLD


KLD Remarks

(A) Domestic 0.8 1.0 1.8

Discharge through soak pit

Industrial

Process NIL 2.8 2.8

Washing NIL 1.0 1.0

Boiler NIL 0.4 0.4

Total Industrial NIL 4.2 4.2 Send to Captive

of 137


Page 83 of 137

waste water Spray Drier

- There will be 4.2 KLD wastewater generation from manufacturing activity and other ancillary operation, waste water will be evaporated through captive spray drier, unit has going to ZERO LIQUID DISCHARGE

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

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

Industrial: There will be 4.2 KLD wastewater generation from manufacturing activity and other ancillary operation, waste water will be evaporated through captive spray drier, unit has going to Zero Liquid Discharge


No

Membership of CF No

vii Reuse/Recycle details (KLD) No



-

SR.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1 Boiler (1 T) 11.00

PNG 3000

SCM/Day

Not Applicable

Not applicable 2 HAG 11.00

3 Spray

Dryer 9.0 PM, So2,

No2

Cyclone & Water

Scrubber


- There will no process gas Emission from proposed or Existing project.

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

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

i

of 137


Page 84 of 137

Sr. no.

Type/Name of

Hazardous waste


Category and

Schedule as per HW

Rules.

Quantity (MT/Annu

m) Disposal Method

1 ETP

Sludge ETP

Operation 35.3 12

Collection, storage, Transportation and Dispose to Active TSDF/Co-processing

2 Used Oil Process

Equipment 5.1 0.02

Collection, storage, Reuse within premises.

3 Discarded Container/

Bags

Ware House

33.1 1800 Nos. Collection, storage,

Transportation and Dispose to Registered Recycler




Not Applicable



Not Applicable

Ii VOC emission sources and its mitigation measures






waste water were discussed at length.After proposed expansion, treated waste water of 4.2 KLPD is

proposed to be spray dried in captive spray drier.Industrial unit is located in GIDC, Vatwa which is

existing prior to EIA Notification 2006 and hence it is decided to exempt public hearing for the

aforementioned proposal.



to be done covering 10 Km radial distance from the project boundaryincluding following project

specific TOR.

1. To verify compatibility of water consumption and waste water generation keeping proposed expansion in a view.


of 137


Page 85 of 137




2006.



15. SIA/GJ/IND2/21282/2017 M/s. Rohan Dyes & Intermediates Ltd.

Factory Address: plot no123, GIDC, Phase-I,

Vatva.

Screening & Scoping





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

expansion as tabulated below:

Sr. No.

Product CAS NO. Existing MT

/Month

Proposed Increase

in MT /Month

Total After Proposed

MT / Month

END USE OF

PRODUCT

1. Reactive Black 5OR 17095-24-8 300 350 650 Reactive dyeing used for coloration of cellulosic fibres. It can also be applied on wool and nylon.

2. Reactive Black JNN OR

-

3. Reactive Black WNN OR

-

4. Reactive Red RR OR -

5. Reactive Orange W3R OR

-

6. Reactive Yellow 145 OR

93050-80-7

7. Reactive red 111 OR 88232-20-6

8. Reactive Red 195 OR 93050-79-4

1. Acid Black 10BX OR 1064-48-8 300 350 650 Acid dyes are used for dyeing wool,

2. Acid Black 210 OR 99576-15-5

3. Acid Black 234 OR 157577-99-6

of 137


Page 86 of 137

4. Acid Black 194 OR 61931-02-0 nylon, leather and as wood stains.

5. Acid Brown 14 OR 5850-16-8

6. Acid Brown 188 OR 12219-57-7

7. Acid Brown 354 OR 71799-43-4

8. Acid Brown 425 OR 119509-49-8

9. Acid Brown 432 OR 119509-50-1

10. Acid Brown 434 OR 126851-40-9

11. Acid Brown 58 OR 12269-87-3

12. Acid Brown 83 OR 13011-68-2

13. Acid Brown ICN OR -

14. Acid Brown SS OR -

15. Acid Orange 6 OR 547-57-9

16. Acid Orange 61 OR 6408-33-9

17. Acid Orange 7 OR 633-96-5

18. Acid Yellow 194 OR 61814-52-6

19. Acid Blue 193 OR 12392-64-2

20. Acid Brown 106 OR 61724-11-6

21. Acid Brown 161 OR 61724-13-8

22. Acid Brown 282 OR 12219-65-7

23. Acid Brown 348 OR 72827-72-6

24. Acid Brown 349 OR 72827-73-7

25. Acid Brown 355 OR 60181-77-3

26. Acid Brown 75 OR 8011-86-7

27. Acid Brown 97 OR 108347-99-5

28. Acid Green 20 OR 5850-39-5

29. Acid Red 357OR 61951-36-8

30. Reactive Blue 222 OR 93051-44-6

31. Reactive Blue RGB (250) OR

93951-21-4

32. Direct Black 22 OR 6473-13-8 Directdyes widely used for colorationof cellulosic fibres.

33. Direct Blue 71 OR 4399-55-7

34. Direct red 81 OR 2610-11-9


2006



project proponent.

of 137


Page 87 of 137


Sr.

no.

Particulars Details

A TotalcostofProposedProject

(Rs.inCrores):

Existing: Rs. 20.0 Crores

Proposed: Rs. 5.0 Crores

(1)CapitalcostforEMS(EnvironmentalManagementSystem):Rs.1.0 Crores

(2)Recurringcosttowardstheenvironmental protectionmeasures: Rs. 0.75 Crores B TotalPlotarea

( sq.meter)

Existing: 10,000 m2

Proposed: -

Greenbeltarea,/TreePlantationarea

( sq.meter)

Existing:300 m2

Proposed:- 200m2

C Employmentgeneration

1. Direct Existing: 80

Proposed: 80

2. Indirect Existing: 90

Proposed: 90

D Water

i SourceofWaterSupply

(GIDC,Borewell,Surfacewateretc...)

Private Borewell

Statusofpermission from theconcernauthority.

ii Waterconsumption(KL/day)

Existing

KL/day

Proposed

(Additional)

Totalafter

Expansion

Remarks

KL/day KL/day

(A)Domestic

10.0 0.0 10.0 - (B)Gardening

(C)Industrial

Pro

70.0 135.0 205.0 - Washing 55.0 -40.0 15.0 -

Boiler 30 30 - Cooling 0 0 0 -

Others 0 0 0 - Total(A+B+C) 135.0 125.0 260.0 -

iii Wastewatergeneration(KL/day)

of 137


Page 88 of 137

Category Existing

KL/Day

Proposed

(Additional)

KL/day

Totalafter

Expansion

KL/day

Remarks

(A)Domestic

4.0 0.0 4.0 - (B)Industrial

Process 45.0 65.0 110.0 - Washing 55.0 -40.0 15.0 -

Boiler - - 3.0* Reused in process Cooling - - - -

Others - - - - TotalIndustrial 104.0 25.0 129.0 -

Note: 125 KLD process waste water will be treated in ETP and 55 KLD of treated effluent will be discharged to the CETP as per the CC&A quantity. 70 KLD treated effluent will be passed through the R. O. system. Permeate of R.O. (50 KLD) shall be reused back in process and rejects of R.O. (20 KLD) shall be spray dried completely.

* 3 KLD will be reused in process.

**55 KLDwashing wastewater shall be treated and disposed off to CETP.

*** 4 m3

/day of domestic waste water is disposed off through soak pit.

iv Treatmentfacilitywithcapacity

(ETP,CETP,MEE,STPetc).

ETP facility of 150 KLD

CETP, GESCSL, Vatva.

v ModeofDisposal&Finalmeetingpoint Domestic: soak pit

Industrial: CETP, Vatva vi Reuse/Recycledetails(KL/day) 53 KLD

vii Detailsofrainwaterharvesting Roof Top area will be consider for rain water

harvesting. 10 KLD od storage tank will provide for

collection of the rain water. E Air[Existing&Proposed]

I Fluegasemissiondetails

No.OfBoilers/TFH/Furnaces/DGsetsetc.with capacitiesviz.TPH,Kcal/hr,MT/hr,KVAetc.

of 137


Page 89 of 137

Sr.

no.

Sources of

Emission

with

capacity

Stack

height

(m)

Name

of the

fuel

Quantity of Fuel MT/day Type of

Emissio

ns i.e.

Air

pollutant

APCM

Existin

g

Proposed Total

1 Steam boiler

(4 Ton)

30 m Import

ed

coal

15 20 35 <PM

150

mg/Nm3

<SOX10

0 ppm

Bag Filter

&

Dust Collector

2 Hot air

generator -1

30 m

3 Hot air

generator-2

30 m

4 Hot air

generator-3

30 m

ii Processgasi.e.Typeofpollutantgases(SO2, HCl,NH3, Cl2,NOxetc.) [Existing&Proposed]

Sr. no.

Source of emission

Type of

emission

Stack /vent

height in meter

APCM Emission Standards

1 Spray dryer – 1 PM 30 m Cyclone + two stage Water scrubber

< 150 Mg/Nm3

2 Spray dryer – 2

3 Spray dryer -3 (evaporation of concentrated effluent generated from RO reject)

Cyclone + two stage Water scrubber

iii Fugitive Emissions details with its mitigation measures (Existing & Proposed)

Fugitive emission source:

• Liquid material storage area

• Production area Fugitive emission 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.

of 137


Page 90 of 137

Sr. No.

Sources of emission Mitigation measures (Air pollution Control System)

1 Steam boiler(4 Ton) Bag filter & Dust collector

2 Hot air generator -1 -

3 Hot air generator-2 -

4 Hot air generator-3 -

F Hazardous Waste (As per Hazardous & Other Wastes (Management & Transboundary Movement ) Rules 2016 (Existing & Proposed)

Sr. no.

Type/ Name of Hazardous waste

Sources of Generation

Category & Schedule as per HW Rules

Quantity (MT/annum) Disposal Method

Existing Proposed

Total After Proposed

1 ETP Sludge

Filter press (ETP Plant)

34.3 248.4 3351.6

3600 Collection, storage, transportation, disposal at the approvedTSDF site.

2 Used oil Plant Machinery

5.1 4.8 1.2 6.0 Collection, storage, transportation, disposal by selling to registered Re-processors.

3 Discarded container

Raw Material & Finished Goods area

33.3 1.4 1.6 3.0 Collection, storage, decontamination, Transportation, disposalby selling toauthorized recycler. i Membership details of CETP, TSDF, CHWIF, MEE

etc.

TSDF : GESCSL (Vatva), SEPPL

(Bhachau) & ECOCARE

(Surendranagar)

Ii Details of Non-Hazardous waste & its disposal

(MSW and others)

VIA & AMC


I Details of solvent recovery (as per respective TOR) NA

Ii VOC emission sources and its mitigation measures NA

of 137


Page 91 of 137






waste water were discussed at length.After proposed expansion, 125 KLPD waste water will generated

which be treated in ETP.As per existing CCA, 55 KLDof treated effluent will be discharged to the CETP

and additional 70 KLD treated effluent will be passed through the R. O. system. Permeate of R.O.

about 50 KLPD will be reused back in process and rejects of R.O. of 20 KLD will be spray dried

completely.Industrial unit is located in GIDC, Vatwa which is existing prior to EIA Notification 2006 and

hence it is decided to exempt public hearing for the aforementioned proposal.



to be done covering 10 Km radial distance from the project boundary including following project5

specific TOR.

1. To verify compatibility of water consumption and waste water generation keeping proposed expansion in a view.

2. NOC from the CGWA for the additional water requirement to be sourced from the existing bore-well for proposed expansion of the products.

Further, the TOR prescribed as above and as per the standard TOR approved by SEIAA and the

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

Chemical Industry’ shall be considered as generic TORs for preparation of the EIA report in

addition to all the relevant information as per the generic structure of EIA given in Appendix III in the

EIA Notification, 2006.



16 SIA/GJ/IND2/21230/2017 M/s. Amoli Organics Pvt. Ltd.

Plot No.: 322/4, 40 Shed Area, GIDC Vapi Dist:

Valsad, Gujarat- 396195

Appraisal

of 137


Page 92 of 137





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

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

Surat based on the TOR issued by SEIAA.



Sr. no



1

Diclofenac Sodium & its Salts

15307-79-6

20.0 245 265

Pharmaceutical Drugs

Diclofenac potassium 15307-81-0

Diclofenac diethyl amine

78213-16-8

Diclofenc free acid 15307-86-5

DiclofenacResinate 56187-47-4

DiclofenacDeonal NA

DiclofenacAppolomine 119623-66-

4

2 Aceclofenac 89796-99-6 0.5 49.5 50

3 Clotrimazole 23593-75-1 1.0 9 10

4 Di Hydralazene Sulphate

7327-87-9 1.0 1.5 2.5

5 Bifonazole 60628-96-8 0.5 4.5 5

6 Norethisterone Acetate 0.25 -0.25 0

7 Oxcarbazepine 5.0 -5.0 0

8 Carbamazepine 1.0 -1.0 0

9 Sildenafil Citrate 0.5 -0.5 0

10 Pioglitazole 0.5 -0.5 0

11 Momiflumate 1.0 -1.0 0

12 Celecoxib 0.5 -0.5 0

13 CetrizeneDihydrocloride

0.1 -0.1 0

14 Sertaline Hydrochloride

0.5 -0.5 0

15 NoscapineResineComplex

0.05 -0.05 0

16 Nitroxaline 0.05 -0.05 0

17 Formasulphathiazole 1.0 -1.0 0

18 MentronidazoleBebzoa 1.0 -1.0 0

of 137


Page 93 of 137

te

19 Ascorbic Acid 10.0 -10.0 0

20 Rofecoxib 0.20 -0.2 0

21 2 Chloro Ethyl Phenyl Ether

0.1 -0.1 0

22 Venlafaxine Hydrochloride

0.5 -0.5 0

23 Fexofenadine Hydrochloride

0.5 -0.5 0

24 CatalpidogrelHydrogensulphate

0.5 -0.5 0

25 Citalopram Hydrobromide

0.5 -0.5 0

26 Pyridoxine Acetonide Hydro Chloride

58-56-0 0 2.5 2.5

Total 46.75 288.25 335.0


2006



project proponent.


Sr. no.

Particulars Details


(Rs. in Crores):

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

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

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


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


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


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

2. Indirect Existing: 10 Proposed:80-100

of 137


Page 94 of 137

Total:90-100

D Water i


GIDC

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

ii Water consumption (KLD):

Existing KLD

Proposed (Additional) KLD

Total after Expansion KLD

Remarks

(A) Domestic 15 5 20

(B) Gardening 10 5 15

Industrial

Process& Washing

55 88 143 Processing and product washing

Washing 34 6 40

Floor/container/ equipment

Boiler 20 40 60

Cooling 20 55 75

Others 5 2 7 Scrubber

Industrial Total 134 201 325

Grand Total (A+B+C)

159 8.14 360

1) Total water requirement for the project: 360KLD

2) Quantity to be recycle: 0 KLD

3) Total fresh water requirement: 360KLD





Remarks

(A) Domestic 12 5 17

Industrial

Process& Washing

60 109 169 Process and product washing

Washing 34 6.0 40.0 Equipment & Floor washing

Boiler 18.0 7.0 25.0

Cooling 10.0 0.0 5.0

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

Total Industrial 125 118 244 After Expansion (Normal

of 137


Page 95 of 137

waste water effluent 151 KLD+ Concentrated 18 KLD+ Utilities 75 KLD) )

-

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

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


Industrial: ETP &MVR


CETP: Vapi Green Enviro Ltd.

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

vii Reuse/Recycle details (KLD) --



-

Sr.

no

.

Source of

emission

With Capacity

e.g. Boiler (8

TPH)

Stack

Height

(meter

)

Name of

the fuel

Quantit

y of

Fuel

MT/hr&

MT/Day

Type of

emissions

i.e. Air

Pollutants

APCM

Existing

1 Boiler (3

TPH) 31

Imported

coal

583

kgs/hr PM, SO2

NOx

MDC &

bag filter

Proposed

1 Boiler (8

TPH) 30

Imported

coal

972

kgs/hr PM, SO2

NOx ESP

2 D.G Set -1250

KVA 11 HSD

220

kgs/hr PM, SO2

NOx Chimney

-


Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height

APCM

of 137


Page 96 of 137

(meter)

Existing

1 Reactor HCl, Cl&

SO2 11

Two stage graphite

followed by alkali scrubber

Proposed

1 Reactor HCl, Cl&

SO2 11

Two stage graphite

followed by alkali scrubber

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

[Existing & Proposed]

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

conditions through timely predictive and preventive maintenance;

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

plant.

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

developed along with construction activity.

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

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

accordingly.

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

prevent fugitive emission.

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

implementing latest automation technology.

All venting system will have vapor recovery system


i

Sr. no.




Existing Quantity (MT/Annum)

Proposed Quantity (MT/Annum)

Disposal Method

1. Used oil D.G Sets & equipment maintenance

5.1 0.24 0.3 Is being/will be sent

to registered re-processors

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Page 97 of 137

2. Discarded containers

Unloading of raw materials 33.1 30.0 50.0

Collection, Storage, Decontamination

3. Process

Residue & waste

Manufacturing process 28.1 12.0 1200.9

Is being/will be sent to incinerator

4. ETP waste ETP

35.3 180 4900 Is being/will be sent

to TSDF

5. Spent Carbon

Manufacturing process 28.2 48 192.0

Is being/will be sent for co-processing to RSPL, Panoli

6 Spent solvent

Manufacturing process 28.6 20.0 622.764

Is being/ will be reuse within industrial unit

7. Aluminum Chloride

Soln.

Manufacturing process SCH:

II, B10 1500 6264

Is being/ will be sale to authorized

unit through manifest system

8 Chemical Sludge

from high COD

stream

Manufacturing process

35.3 6.6 0 Is being sent for

incineration

9 Used Glass wool

Manufacturing process Z-22 0.06 0.12

Is being/will be sent to TSDF

10 Salt from MVR

MEE/ MVR 35.3 0 842

Will be dispose off into TSDF

11 Inorganic Acid (30%

HCl)

Manufacturing process Sch: II

B 15 0 2922

Will be sold to authorized users

12 KCl Powder from

process

Manufacturing process 28.1 0 744


13 NaCl from process

Manufacturing process 28.1 0 272




• TSDF SEPPL, Kutch Membership No. 1200001191

• CSWP, Vapi Membership No. 105

• RSPL membership for co-processing: CPAW1A0012

iii Details of Non-Hazardous waste & its disposal

Fly Ash from Boiler Existing : 145 TPA

of 137


Page 98 of 137

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


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

Solvent Stripper is/will be installed for solvent recovery.

Solvent Name

Kg/Month Overall

% Recovery Input Recovered Consumed Loss

Toluene 376690 361625 0 15065 96.00

Methanol 50065 47815 0 2250 95.51

N-N Di Methyl Aniline

61 552 0 61 94

Formic Acid 180 1699.19 0 180 95.7

Acetone/ Ethyl Acetate

162133 156465 469 5198 96.79

IPA 989.3 637.11 876.9 112.4 60


Source:

• Process Reactor

• Raw material Handling & Storage Mitigation Measures:

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

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

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

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

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

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

of 137


Page 99 of 137

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

month of March2017 to May 2017to determine the prevailing status of ambient air, land use, noise level

topography, meteorology, ecology & socioeconomic outline and additional one month in October 2017

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

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

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

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

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

36.0µg/m3 to maximum 52.9µg/m3. Concentration of SO2 recorded ranged from minimum 9.7µg/m3 to

maximum 22.0µg/m3. Concentration of NO2 recorded ranged from minimum 15.1 µg/m3 to maximum

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

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

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

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

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

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

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

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

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

wastewater generation will be 244 KLD. The concentrated effluent of 18 KLD will be treated in MVR and

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

generation will be 17 KLD. The domestic wastewater will be disposed of through Soak pit/septic tank.

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

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

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

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

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

waste water generation will be 224 KLPD. Break up of waste water generation is normal effluent 151

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

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

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

scheme by passing waste water through MVR followed by RO. For prevention of release of VOC in the

ambient air, PP is asked to address leak detection and repairing programme. Committee deliberated on

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

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

addressed satisfactorily

of 137


Page 100 of 137

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

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

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

existing consented waste water discharge quantity to CETP.

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

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

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

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

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

17 SIA/GJ/IND2/17973/2016 M/s. Jalaram Chemicals.

Plot No. 3114, GIDC, Sarigam, Tal. Umargam,

Dist.-Valsad, Gujarat-396155

Appraisal


Project status: New

• PP has submitted online application vide no. SIA/GJ/IND2/17973/2016dated 01/01/2018 for


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

24/04/2017.

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

research labs pvt ltdbased on the TOR issued by SEIAA.



Sr. No.

Name of the Products CAS No.

Quantity MT/Month End-use of the

products Existing Proposed Total

1. Ferrous Sulphate# -- 40.00 0.00 0.00 --

2. Chemsonite PC 27 (Construction chemicals) #

-- 30.00 0.00 0.00 --

of 137


Page 101 of 137

3. Chemsonite SP 270 (Construction Chemicals) #

-- 30.00 0.00 0.00 --

4. Chemsonite SP 450 (Construction Chemicals) #

-- 30.00 0.00 0.00 --

5. Sulphated Caster Oil (TRO) 8002-33-3 10.00 10.00 20.00

Textile auxiliary , Rubber industries, Ink, Distillery and Dye industries

6. 2,6, Di Chloro Para Nitro Aniline *

99-30-9 00.00 70.00 70.00 Dye and pigment intermediates

7. Para Benzo Quinone * 106-51-4 00.00 75.00 75.00 Pharma & Dyes Industries

8. Para Tertiary Butyl Catechol

98-29-3 00.00 35.00 35.00 Polymerization inhibitor (Antioxidant)

9. Sodium Phenate 139-02-6 00.00 5. 00 5. 00 Therapeutic uses and dyesindustries

Note:

*= Only one of the two products will be produced at a time.

#=Production of these four products will be discontinued after proposed expansion.


2006



project proponent.


Sr. No.

Particulars Details

A Total cost of Proposed Project (Rs. In crores):

Existing:0.0994 Proposed: 1.0955 Total: 1.1949

(1) Capital cost for EMS (Environmental Management System): 0.3475 Crores (2) Recurring cost towards the environmental protection measures: 0.1855 Crores per Annum.


Existing: 1125.00 Proposed:0.00 Total: 1125.00


Existing: 249.00 Proposed:0.00 Total: 249.00


1. Direct Existing: 10 Proposed:10.00 Total: 20.00

of 137


Page 102 of 137

2. Indirect Existing: 20.00 Proposed:10.00 Total: 30.00

D Water

i


GIDC water supply

Status of permission from the concern authority.Permission obtained


Existing KL/day



Remarks

(A) Domestic 5.00 - 4.00 1.00 --

(B) Gardening 1.00 - 0.50 0.50 --

(C) Industrial

Process 1.64 8.86 10.50 --

Washing 1.00 0.00 1.00 --

Boiler & Cooling 0.00 1.50 1.50 --

Scrubbing 0.00 0.50 0.50 --

Others -- -- -- --

Total (A+B+C) 8.64 10.86 15.00




KL/day


KL/day

Remarks

(A) Domestic 4.00 - 3.3 0.70 Disposal through septic tank/soak pit

(B) Industrial

Process 0.05 8.45 8.50 Disposal through CETP, Sarigam after treatment in in-house ETP.

Washing 0.50 0.00 0.50

Boiler & Cooling 0.00 0.50 0.50

Scrubbing 0.00 0.50 0.50

Others -- -- --


0.55 9.45 10.00


In-house ETP (Capacity: 15 KL/Day Max.)


Domestic: Septic tank/soak pit

Industrial: In-house ETP then treated effluent to CETP, Sarigam for final disposal.

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

vii Details of rain water harvesting Total Rainwater harvesting is 1358.15 m3/annum


of 137


Page 103 of 137


Sr.

No.

Source of

emission

With Capacity

e.g. Boiler (8

TPH)

Stack

Height

(meter

)

Name

of the

fuel

Quantity of

Fuel

MT/hr&

MT/Day

Type of

emissions

i.e. Air

Pollutants

APCM Emission

Standards

1

Proposed Steam

Boilers

(1000 kgs/hr)

-1 No.

11.00 LSD 60 L/hr PM SOX NOX

--

PM<150 mg/Nm3

SOX< 100 ppm

NOX< 50 ppm

2

Proposed

Thermopack

(2 lakh Kcal/hr

each)- 2 Nos.

11.00 Natural

Gas 30 SCM/hr

PM SOX NOX

--

PM<150 mg/Nm3

SOX< 100 ppm

NOX< 50 ppm

3

Proposed D.G.

Set

(25 HP) -1 No.

11.00 HSD 8 Lit/Hr PM SOX NOX

Acoustic

enclosure.

PM<150 mg/Nm3

SOX< 100 ppm

NOX< 50 ppm


Sr.

no.

Source

of

emission

Type of

emission

Stack/Vent

Height

(meter)

APCM Emission

Standards

1 Reaction

Vessel

HCl

Cl2

SOx

VOC

11 m

Two Stage Scrubbing system

(Water scrubber+ Alkali

scrubber)

HCl<20 mg/NM3

Cl2 <09 mg/NM3

SOX< 100 ppm

of 137


Page 104 of 137

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

There is no particular fugitive emission from the existing and proposed project. Proper maintenance and planning will be done for Fugitive emission from the transportation and accidental leakage.


i

Sr. no.

Type/Name of

Hazardous waste


Category and

Schedule as per HW

Rules.

Quantity (MT/Annum)

Disposal Method

ETP Waste

ETP Operation 35.3 30 MT/Year

Collection, Storage, Transportation, Disposal at TSDF

Used Oil

Machinery 5.1 50 Lit/Year

Collection, Storage, Transportation, disposal by selling to registered recyclers.

Discarded drum/Bags /Liners

Raw Materials 33.1 7.2 MT/Year (800

Nos./Year)

Collection, Storage, Decontamination, Disposal on sale to actual users.

Distillation Residue

Mfg. Process 20.3 37.80 MT/Year Disposal through CHWIF or Co-processing at Cement Plant



Membership obtained from CETP Sarigam and Sarigam waste and effluent Management. Co. Ltd.

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

No other waste generation from the proposed project.


i Details of Solvent recovery (As per respective ToR)

Two solvents are there and solvent recovery will be done by distillation process


VOC would be emitted from reaction vessel and it will be controlled by Two Stage Scrubbing system (Water scrubber+ Alkali scrubber) Stack ht.: 11 mt.&Dia.: 100 mm





month of October 2016 to December 2016 to determine the prevailing status of ambient air, land use,

of 137


Page 105 of 137

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

was measured at eight locations. Monitoring was carried out for PM10, PM2.5, SO2,NOx, CO, O3,

NH3, Pb, As, Ni, Benzene, BaP and VOCwithin 5 km radius from the project site. The maximum

concentrations of PM10, PM2.5, SO2,NOx CO, O3, NH3, Pb, As, Ni, Benzene, BaP and VOC at each

ambient air monitoring locations were compared with NAAQS for industrial, residential, rural and other

areas. Concentration of PM10 ranged from 45 µg/m3 to 95 µg/m3. Concentration of PM2.5 recorded

from minimum 11µg/m3 to maximum 39 µg/m3. Concentration of SO2 recorded ranged from minimum

9.30µg/m3 to maximum 29.10µg/m3. Concentration of NO2 recorded ranged from minimum

11.40µg/m3 to maximum 28.40µg/m3.Concentration of CO recorded ranged from minimum 1.20µg/m3

to maximum 1.50 µg/m3. Concentration of O3 recorded ranged from minimum 5.00µg/m3 to maximum

13.70µg/m3.Concentration of NH3 recorded ranged from minimum 20.0µg/m3 to maximum 45.0 µg/m3.

Concentration of Pb, As, Ni, Benzene, BaP and VOCfounded BDL.The incremental Ground Level




with NAAQ standards.Committee observed that PP has proposed natural gas as fuel for thermo pack

and LSD as fuel for Boiler. Unit has proposed two stage scrubbing system for reaction vessel. The total

industrial water consumption will be 15 KLD which will be sourced from GIDC. The industrial

wastewater generation will be 10 KLD which will be treated in ETP and treated wastewater will be

discharged to the CETP, sarigam. The domestic wastewater generation will be 0.7 KLD. The domestic

wastewater will be treated in soak pit.

Committee noted that proposal is falling under 5(f). PP is asked PP for compliance of existing

conditions of CCA, details of public complaints/public litigation if any and action initiated by the GPCB

against the industrial unit which was satisfactorily replied by the PP. It is further noted that PP has

proposed to surrenderconsented products namely Ferrous Sulphate, Chemsonite PC 27,Chemsonite

SP 270and Chemsonite SP 450 and has proposed Sulphated Caster Oil (TRO)2,6, Di Chloro Para

Nitro Aniline, Para BenzoQuinone, Para Tertiary Butyl Catechol, Sodium Phenate. After surrendering

the existing products, water consumption for existing products is considered. Committee asked PP to

correct water consumption. Committee deliberated on air pollution control measures for flue gas and

process emission, hazardous waste generation and management and risk assessment based on worst

case scenario. PP is asked to readdress bleed liquor of scrubber under the Hazardous and other Waste

(Management and Transboundary) Rules 2016. For rest of the aspects, committee found TORs

addressed satisfactorily.



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Page 106 of 137

1. Revised project details mentioning corrected water consumption, waste water generation considering deletion of existing consented products.

2. Readdress hazardous waste details considering bleed liquor from scrubber under the Hazardous and other Waste (Management and Transboundary) Rules 2016

18 SIA/GJ/IND2/18864/2017 M/s. Lanxess India Private Limited

at Plot No. 748/2/A, 748/3, 748/4/A & 748/4/B,

Jhagadia Notified GIDC Industrial Estate,

Taluka – Jhagadia, Dist. Bharuch, State -

Gujarat, India

Appraisal





• The 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: Siddhi Green Excellence Pvt.

Ltd., Ankleshwarbased on the TOR issued by SEIAA.



Sr.

No. Products Quantity in MT/month

Remarks

Additional for

EC

expansion(MT

A)

Total after EC

expansion(MT

A)

1

Ion exchange resin

chemicals- (I) Strong

acid cation/ (II) Weak

acid cation/ (III) Strong

base anion/ (IV) Weak

base anion/ (V) Mixed

beds

2916.670

m3/month

Ion Exchange

resin chemicals-

35,000

CUM/Annum

-- 35000

2 Leather chemicals-(I)

Syntans/ (II) 833.340

Rubber &

Leather

chemicals-

-- 10000

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Page 107 of 137

Finishing chemicals/ (III)

Preservative/ (IV)

Rubber compounding

10,000

MT/Annum

3 Rubber chemicals-

Accelerators 500.000

Rubber

chemicals- 6000

MT/Annum

-- 6000

4 Rubber chemicals-

Antioxidants* 1250.000

Rubber

chemicals-

15,000

MT/Annum

20000 35000

5

Semi crystalline

product- (I)

Durethan A/ (II)

Durethan B/ (III) Pokan

1666.670

Semi crystalline

product- 20,000

MT/Annum

-- 20000

6 Zinc di- thiophosphates 333.340

Total production

shall not exceed

4000 MT/Annum

-- 4000

7 Lubricant oil additive

packages 166.670

Total production

shall not exceed

2000 MT/Annum

-- 2000


2006



project proponent.


Sr. no

Particulars Details

A Total cost of Proposed Project (Rs. in Crores): 95.47 rore (for expansion only)

(1) Capital cost for EMS (Environmental Management System):Rs. 15 Crores

(2) Recurring cost towards the environmental protection measures: 1.3 Crores per Annum.

B Total Plot area ( sq. meter) Existing: 182400 Sq.m Proposed: 00 Sq. m. Total: 182400 Sq. m.

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Existing: 38365 Sq.m Proposed: Additional at surrounding villages 27424 Sq.m Total: 65790 Sq.m


1. Direct Existing: 675 (company employee +

on contract basis)

Proposed: 25 (company employee +

on contract basis)

Total: 700 (company employee + on contract basis)

2. Indirect

D Water

i


GIDC

Status of permission from the concern authority. Process is ongoing


Water

Consumption

quantity In kL / day

Existing

quantity

as per

CTO

Additional

quantity for

proposed

expansion

Total water

consumption

after proposed

expansion

(i) Domestic :

99 -- 99

(ii) Industrial : (a) Processing : 2778.96 11.04 2790

(b) Boiler : 117 34.00 151

(c) Cooling : 835 -- 835

(d) Washing : 43 -- 43

(g) Gardening : 35 -- 35

DOMESTIC : 99 -- 99

INDUSTRIAL : 3808.96 45.04 3854

TOTAL : 3907.96 45.04 3953

1) Total water requirement for the project: 3953 KLD

2) Quantity to be recycle: Boiler blow down (19.64 KLD) shall be used for washing and

then sent to ETP.

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Page 109 of 137

3) Total fresh water requirement: 3953 KLD


Wastewater

Quantity In kL / day

Existing

quantity as

per CTO

Additional

quantity from

proposed

expansion

Total waste water

generation after

proposed

expansion

(i) Domestic 89.10 -- 89.10

(ii) Industrial

(a) Processing : 2229.66 41.00 2270.66

(b) Boiler : 26.00 Note 1 26.00

(c) Cooling : 175.70 -- 175.70

(d) Washing : 68.00 19.64 87.64

DOMESTIC : 89.10 -- 89.10

INDUSTRIAL : 2499.36 60.64 2560.00

TOTAL 2588.46 60.64 2649.10

Note 1: Boiler blow down shall be used for washing and then sent to ETP. Units has already implemented waste segregation and recycle practices and limited the effluent discharge within 2500 KLD as per CTO. About 1344 KL/day of low COD effluent generated from Ion Exchange Resin Chemicals Plant is recycled after specific treatment plant comprising of Neutralization tank, DMF and membrane separation units and reused for process water consumption. This accounts to 37.8% of total effluent generated from Ion exchange resin chemicals production. For additional effluent generation of 60.64 KLD due to proposed expansion, existing ETP shall be upgraded to increase design capacity from 2500 KLD to 2700 KLD. The treatment scheme shall remain the same.

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

ETP capacity: Existing 2500 KLD to be upgraded upto 2700 KLD STP: 100 KLD (Existing)

v Mode of Disposal & Final meeting point Domestic: Total domestic effluent shall be treated in existing STP

Industrial: Total effluent after proposed expansion shall be discharged into Jhagadia Deep Sea pipeline governed by M/s. Narmada Clean Tech (NCT),Ankleshwar and final discharge into deep sea.

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Page 110 of 137


--

Membership of Common facility (CF) --

vii Reuse/Recycle details (KLD) Refer point no. D (ii) & (iii)



Stack No.

PCB ID of stack

Stack Attached

to

Stack Height

(M)

Fuel used & rate of

consumption Parameters

Control Measures provided

As per Existing CTO

1 48709

Incinerator

(Off gas) 30 NG-341Sm3/h

Particulate

Matter

SO2

NOx

Water Scrubber

2 71081

DG set – 1

SIS (500

KVA)

(Stand by)

12 Diesel-

102 L/h

Particulate

Matter

SO2

NOx

Diesel engine meets stringent exhaust

emission tests as per MoEFCC norms

3 69414

Multi Fuel

Boiler (14

TPH)

40

Coal-3300 kg/h

or

Biomass (Mix)-

4666 kg/h or

both

Particulate

Matter

SO2

NOx

ESP + Water Scrubber

4 75740

DG Set – 2

ION (500

KVA)

(Stand by)

18 Diesel-

102 L/h

Particulate

Matter

SO2

NOx



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Page 111 of 137

5 78898

Diesel

Generator

(1010 KVA)

(Stand by)

30 Diesel-

204 L/h

Particulate

Matter

SO2

NOx



6 78899

Thermo

cleaning

machine

15 NG-5 Sm3/h

Particulate

Matter

SO2

NOx

Since Natural gas is used as fuel, no air pollution control equipment is

required

7 78901

Fire

Hydrant

pump-

1(156 HP)

5 Diesel- 27.4

L/h

Particulate

Matter

SO2

NOx



8 78896

Boiler – 10

TPH 21 NG- 600 Sm3/h

Particulate

Matter

SO2

NOx

Boiler meets stringent exhaust emission tests as

per MoEFCC norms

9 78900

Hot water

generation

unit

15 NG-4 Sm3/h

Particulate

Matter

SO2

NOx

Since Natural gas is used as fuel, no air pollution control equipment is

required

10 78902

Fire

Hydrant

pumps - 2

(156 HP)

5 Diesel-27.4 L/h

Particulate

Matter

SO2

NOx



EC applied for Additional expansion

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Page 112 of 137

11 --

Multi Fuel

Boiler- 8

TPH *

40

Coal-1886 kg/h

or

Biomass (Mix)-

2666 kg/h or

both

Particulate

Matter

SO2

NOx

ESP + Water Scrubber

Adequate stack with sampling platform and access ladder shall be provided *If steam will be supplied by nearby company like Shriram Alkali & chemicals, unit will not install proposed new Multi fuel boiler (MFB).


Existing & Proposed process stacks

Stack

No.

PCB ID

of stack Stack Attached to

Stack Height

in Meter Parameter

Air pollution

control measure

1. 50804

Storage tank Vents

(Acetone) 9 Hydrocarbon

Vent chiller for

acetone

2. 78903

HS Packing Silo

area 9 SPM Bag Filter

3. 85583

Accelerator packing

silo 9 SPM Bag Filter

There shall be no additional process emission after proposed expansion of Rubber Chemical Plant- Antioxidants.

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

Sr. Probable sources Proposed Control measures

1. Pump, agitators

and compressor

Emissions

Use of mechanical seals in pumps, agitators and compressors

where VOC are handled

Unit has provided many provisions like pressurized seal, Teflon

coated, magnetic coupling, and mechanical seals to avoid

leakage from the coupling.

2. During charging Liquid raw materials are charged by pumping & closed loops

and dosing will be done by metering system to avoid fugitive

emissions. Dedicated measuring tanks are provided for each

reactor.

Suitable stoichiometric calculation is done and followed to

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Page 113 of 137

regulate the quantity of reactants to be charged to reaction

vessels in order to avoid use of excess chemicals, which in turn

will minimize organic load in the effluent.

3. During reactions &

Solvent recovery

systems

All reactors & solvent recovery systems are closed and provided

with primary and secondary condensers for vapor recovery

Solvent recovery of minimum 95% is achieved

Temperature and pressure conditions are stringently controlled

through DCS as per the process requirement and optimized

with low temperature and vacuum conditions wherever feasible.

Off-gas incinerator for controlling hazardous vapors from

process vents. Even scrubber outlets are connected with

incinerator.

4. Pressure Relief

Valve Emissions

from pipelines

For highly pressurized lines, pressure equalization is followed

with return lines so that the pipelines as well as connected

equipment do not get pressurized unduly.

5. Release from

Sampling Lines

Using a closed loop sampling system.

6. Emissions from

Bulk Storage

Tanks during

storage, loading

and unloading

Breather valves, PSVs, Rupture discs provided

Closed transfer system.

Vapour recovery system installed for process/storage tank vents

Tank Pressure equalization applied wherever required

Use of ISO tankers wherever required

7. Valves, Flanges,

plugs and

instrument

connections

Welded pipes used wherever feasible

Suitable gasket material used

Suitable gland packing used in valves

Periodic inspection and maintenance of pipes and pipe fittings

8. Chemical vapor

from wet cake in

Covered transfer systems adopted, workers are provided PPE,

fume extraction systems provided, wherever required

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Page 114 of 137

filtration and drying

area

9. Warehouse storing

drums and bags

Spillages are strictly prevented by providing drip pans, proper

handling equipment, minimum manual operations, local

exhausts and roof top ventilators

Spill control procedures and equipment are provided


i

Sr.

No.

Type of

Waste

Sched

ule

I/II/III/I

V

Catego

ry

(As Per

2016)

Generation (MT

/Annum)

Source

of

generatio

n

Facility

Mode of

disposal &

remarks

As per

Existi

ng

CTO

EC

applied

for

Additio

nal

quantity

Total

after

EC

expansi

on

1.

Discarded

asbestos I 15.2 1.0 NIL 1.0

Old

gaskets

&

insulatio

n rope

Collection,

Generation

, Disposal,

Storage,

Transporta

tion

Disposal

by send it

to TSDF-

M/s. BEIL,

Ankleshw

ar

2.

Contamin

ated

aromatic,

aliphatic

or

naphtheni

c solvents

may or

may not

be fit for

reuse

I 20.1 40 NIL 40

From

Manufact

uring

Process

Collection,

Generation

, Disposal,

Storage,

Transporta

tion

Disposal

by send it

to TSDF-

M/s. BEIL,

Ankleshw

ar

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Page 115 of 137

3.

Spent

Solvents

I 20.2 25 NIL 25

From

laborator

y

Collection,

Generation

,

Incineratio

n,

Disposal,

Storage,

Transporta

tion

Disposal

by

incineratio

n in

common

incinerator

of M/s.

BEIL,

Ankleshw

ar

4.

Distillation

Residue

I 20.3 620 360 980

From

Manufact

uring

Process

Co-

Processing

,

Collection,

Generation

,

Utilization,

Incineratio

n,

Disposal,

Storage,

Transporta

tion

Disposal

by

incineratio

n in

common

incinerator

of M/s.

BEIL,

Ankleshw

ar OR by

co-

processin

g at

Ambuja

Cement

Ltd,

Kodinar

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Page 116 of 137

5.

Process

Sludge

I 20.4 100

0 400 1400

From

Manufact

uring

Process

Co-

Processing

,

Collection,

Generation

, Disposal,

Storage,

Transporta

tion

Disposal

send it to

TSDF,

M/s. BEIL,

Ankleshw

ar OR by

co-

processin

g at

Ambuja

Cement

Ltd,

Kodinar

6.

Process

wastes,

residues

and

sludge

I 21.1 20 20 40

From

Manufact

uring

Process

Collection,

Generation

,

Incineratio

n,

Disposal,

Storage,

Transporta

tion

Disposal

by

incineratio

n in

common

incineratio

n of M/s.

BEIL,

Ankleshw

ar

7.

Sludge

and filters

contamina

ted with oil

I 3.3 0.2 NIL 0.2 During

filtration

Collection,

Generation

,

Incineratio

n,

Disposal,

Storage,

Transporta

tion

Disposal

by

incineratio

n in

common

incineratio

n of M/s.

BEIL,

Ankleshw

ar

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Page 117 of 137

8.

Empty

barrels/co

ntainers /

liners

contamina

ted with

hazardous

chemicals

/ wastes

I 33.1 416 80 496

From

raw

material

and

product

handling

Collection,

Recycling,

Decontami

nation,

Generation

, Disposal,

Reuse,

Storage,

Transporta

tion

Disposal

by send it

to

authorized

decontami

nation

facility /

recycler or

reuse or

send back

to supplier

9.

Exhaust

Air or Gas

cleaning

residue

I 35.1 2.0 NIL 2.0 From

stack

Collection,

Generation

,

Incineratio

n,

Disposal,

Storage,

Transporta

tion

Disposal

by

incineratio

n in

common

incinerator

of

M/s.BEIL,

Ankleshw

ar

10.

Spent ion

exchange

resin

containing

toxic

metals

I 35.2 0.1 NIL 0.1

From ion

exchang

e plant

Collection,

Generation

,

Incineratio

n,

Disposal,

Storage,

Transporta

tion

Disposal

by

incineratio

n in

common

incinerator

of M/s.

BEIL,

Ankleshw

ar

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Page 118 of 137

11.

Chemical

sludge

from

waste

water

treatment

*

I 35.3 120

0 600 1800

From

ETP

Co-

processing

,

Collection,

Generation

, Disposal,

Storage,

Transporta

tion

Disposal

by send it

to TSDF-

M/s. BEIL,

Ankleshw

ar OR by

co-

processin

g at

Ambuja

Cement

Ltd,

Kodinar

12.

Spent

carbon or

filter

media

I 36.2 2.0 NIL 2.0

From

carbon

filter

Collection,

Generation

,

Incineratio

n,

Disposal,

Storage,

Transporta

tion

Disposal

by

incineratio

n in

common

incinerator

of M/s.

BEIL,

Ankleshw

ar

13.

Used or

Spent Oil I 5.1 43 10 53

Gear box

&

transfor

mer

Collection,

Recycling,

Generation

, Disposal,

Reuse,

Recovery,

Storage,

Transporta

tion

Disposal

by Reuse

in plant &

machinery

as

lubricant

or sell it to

authorized

re-refiners

/ recycler.

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Page 119 of 137

14.

Inorganic

Acids II B15

600

0 NIL 6000

From

manufact

uring

process

Collection,

Recycling,

Generation

, Disposal,

Recovery,

Storage,

Transporta

tion

Sulfuric

acid (65-

85%), sell

to

authorized

user

having

authorizati

on with

valid CTO

and Rule

9

permissio

n

15. Corrosive II C2

200

0 NIL 2000

From

manufact

uring

process

Collection,

Recycling,

Generation

, Disposal,

Storage,

Transporta

tion

NaSH

solution :

Sell to

authorized

user

having

authorizati

on with

valid CTO

and Rule

9

permissio

n

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Page 120 of 137

16. Corrosive II C2

600

0 NIL 6000

From

manufact

uring

process

Collection,

Recycling,

Generation

, Disposal,

Storage,

Transporta

tion

Ammonia

Solution :

Sell to

authorized

user

having

authorizati

on with

valid CTO

and Rule

9

permissio

n

*Presently unit has given additional Fenton treatment and during cleaning of ETP plant sludge quantity may be increased from 1200 to 1800 MT/Annum without increase in hydraulic load.


The unit has valid membership certificate for existing & additional waste of M/s. BEIL, Ankleshwar (TSDF &CHWIF) for disposal of hazardous waste & NCT for treated effluent quantity for discharge into Jhagadia Deep Sea pipeline governed by M/s. Narmada Clean Tech (NCT),Ankleshwar and final discharge into deep sea.


Fly ash: 6613 MT/Annum shall be sold to brick manufacturer


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

Solvents are used in Vulkanox series of antioxidants both as media as well as raw materials. Reactors for this production are provided with: 1). Chiller at the outlet of common vent system to condensed solvent vapors. Condensed liquid is delivered to storage tank. 2). Distillation column for enriching solvent purity.


Refer point no. E (iii)



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Page 121 of 137



month of February 2017 to April 2017 to determine the prevailing status of ambient air, land use, noise

level topography, meteorology, ecology & socioeconomic outline. Baseline ambient air quality was

measured at ten locations. Monitoring was carried out for PM10, PM2.5, SO2, NOx,Benzene,NH3, CO,

Benzo(a)pyrene and VOC within10 km radius from the project site. The maximum concentrations of

PM10, PM2.5, SO2, NOx,Benzene,NH3, CO, Benzo(a)pyrene and VOC at each ambient air monitoring

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

PM10 ranged from 78 µg/m3 to 102 µg/m3. Concentration of PM2.5 recorded from minimum 26µg/m3

to maximum 57µg/m3. Concentration of SO2 recorded ranged from minimum 22µg/m3 to maximum

34µg/m3. Concentration of NO2 recorded ranged from minimum 26µg/m3 to maximum

37µg/m3.Concentration of Benzene recorded ranged from BDL to maximum 3.4µg/m3.Concentration of

NH3 recorded ranged from BDL to maximum 12µg/m3. Concentration of CO recorded ranged from BDL

to maximum 1.2 µg/m3.Concentration of Benzo(a)pyrenefounded from BDL.Concentration of VOC

ranged from 1.9µg/m3 to 4.8µg/m3.The incremental Ground Level Concentration (GLC) has been

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

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

model (ISCST3) for PM10, SO2, NOx and resultant values also meets with NAAQ

standards.Committee observed that PP has proposed ESP and water scrubber for additional multi fuel

boiler. Unit has no proposed additional process gas emission. The total industrial water consumption

after expansion will be 3953 KLD; which will be sourced from GIDC. The industrial wastewater

generation will be 2560 KLD.Unit will be upgrade ETPfor proposed increased load of wastewater and

treated wastewater will be discharged to the M/s. NCT through underground pipeline to the deep sea.

The domestic wastewater generation will be 89.1 KLD. The domestic wastewater will be treated in STP.


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

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

the GPCB against the industrial unit which was addressed by PP.Committee noted that compliance

report of ZO,MOEF&CC, Bhopal is for the year 2015 and hence certified compliance report is required.

For ECconditions.PP mentioned that total effluent of 2649.10 KLPD after proposed expansion will be

discharged into Jhagadia deep Sea through pipeline governed by M/s. Narmada Clean Tech

(NCT),Ankleshwar. Committee deliberated on air pollution control measures for flue gas and process

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

scenario and found all the TORs are addressed satisfactorily.



of 137


Page 122 of 137

1. Certified compliance report of Environmental Clearance conditions from GPCB as per the circular dated 07/09/2017 vide letter of J-11013/6/2010-IA-II(Part).

2. Detailed break up of year-wise utilization of funds ( 48 lacs) spared for CSR activities with details of financial outlay of each activity.

19 IA/GJ/IND2/62899/2017 M/s. Clairchem India pvt. Ltd.

Plot No. 905/12/A, G.I.D.C Panoli, Taluka:

Ankleshwar, Dist: Bharuch, Gujarat.

Appraisal



• PP has submitted online application vide no. IA/GJ/IND2/62899/2017 dated 21/11/2017 for


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

07/07/2017.

• Project proponent has submitted EIA Report prepared by M/s: Ultratechbased on the TOR

issued by SEIAA.



Sr.

No. Product

CAS

No.

Existing

quantity

(TPM)

Proposed

quantity

(TPM)

Total

Capacity

(TPM)

End Use of

product

Inorganic products

1 Copper Sulphate 7758-99-8

850 0 850

fungicide

2 Potassium Sulphate 7778-80-5 fertilizers

3 Sodium Nitrate 7632-00-0

food additive and

preservative

4 Mono Ammonium Phosphate 7722-76-1 agricultural fertilizers

Organic Products

1 1H -1,2,4-Triazole 288-88-0 0 30 30

Drug

Intermediate

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Page 123 of 137

2 4-Amino-1,2,4 -Triazole 584-13-4 Drug

Intermediate

3 Methyl -3-Amino Crotonate 14205-39-1 Drug

Intermediate

4 2,4-Difluoro-alpha-(1H-1,2,4-Triazole) acetophenone

86404-63-9 0 5 5

Drug

Intermediate

5 Trifluoro Acetic Anhydride 407-25-0 0 5 5

Drug

Intermediate

6 Trifluoro methane sulphonic Anhydride

358-23-6

0 3 3

Drug

Intermediate

7 5-Methyl [1,2,4] triazolo [3,4-b][1,3]benzothiazole

41814-78-2 0 10 10

Agro

intermediate

8 Bromo Benzene 108-86-1 0 10 10

Drug

Intermediate

9 Benfotiamine 22457-89-2

0 2 2

anti-diabetic

10 Betahistine 5638-76-6 anti-vertigo

11 Indometacin 53-86-1 anti-

inflammatory

12 Ivermectin 70288-86-7 antiparasitic

13 D-biotin 58-85-5

0 0.5 0.5

Vitamin H

Supplement

14 Tadalafil 171596-29-5

erectile

dysfunction

15 Tobramycin sulfate 49842-07-1 aminoglycosid

e antibiotics

16 Mupirocin 12650-69-0 antibiotic

17 Acarbose 56180-94-0 anti-diabetic

18 Voglibose 83480-29-9 0 0.05 0.05

alpha-

glucosidase

of 137


Page 124 of 137

19 Ethyl Valerate 539-82-2 0 2 2 flavors

20 Methyl Valerate 624-24-8 0 2 2 fragrances

21 Cyclohexyl Acetate 622-45-5 0 5 5 flavors

By Products

1

Liquor Ammonia (12-15%)

1336-21-6 0

43.35 43.35

acid

neutralizer

2 Aluminum Hydroxide

21645-51-2 0 32.68 32.68 antacid

3

Phosphoric Acid (H3PO4) {40 To 50 %}

7664-38-2 0

195.30 195.30

leavening

agents

4

Formic Acid (35%)

64-18-6 0

8.69 8.69

antibacterial

agent

5

Hydrobromic acid (25%-30%)

10035-10-6 0

8.97 8.97

reducing

agent


2006



project proponent.


i Total cost of Proposed Project

(Rs. in Crores):

Existing: 1 Cr. Proposed: 2 Cr. Total: 3 Cr.

ii (1) Capital cost for EMS (Environmental Management System):0.3 Crores

(2) Recurring cost towards the environmental protection measures: 0.07 Crores per Annum.

Iii Total Plot area ( sq. meter)

Existing: 1612.8 Proposed: - Total: 1612.8

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

Existing: 266 Proposed: 266 Total: 532

Sr. Particulars Details

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Page 125 of 137

no.

A Water i

Source of Water Supply (GIDC, Bore well, Surface water etc...) G.I.D.C, Panoli

Status of permission from the concern authority. Permission obtained.


Existing KL/day


KL/day


KL/day

(I) Domestic 2.0 1.35 3.35

(J) Gardening - 2.0 2.0

(K) Industrial

Process - 6.95 6.95

Washing - 0.3 0.3

Boiler 2.5 - 2.5

Cooling 3.0 - 3.0

Scrubbing - 0.34 0.34

Total (A+B+C) 7.5 10.94 18.44




KL/day


(F) Domestic 1.5 1 2.5

(G) Industrial

Process - 1.3 1.3(0.9 L + 0.4 H)

Washing - 0.3 0.3

Boiler - 0.3 0.3

Cooling - 0.4 0.4

Scrubbing - - -

Total Industrial waste water - 2.3 2.3


ETP: 5 KLD CETP (ZLD), ACPTCL: 1250 KLD


Domestic: Soak Pit

Industrial: ACPTCL(ZLD)

vi Reuse/Recycle details (KL/day) 1.0

vii

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


SR

.

no

Source of emission

With Capacity e.g.

Stack

Height

Name

of the

Quantity of

Fuel MT/hr&

Type of

emission

s i.e. Air

APCM

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Page 126 of 137

. Boiler (8 TPH) (meter) fuel MT/Day Pollutants

EXISTING

1 Baby Boiler

(800 Kg/Hr) 9.0

Natur

al Gas 600 m3/day

SPM

SO2

NOX

adequate

stack

height is

provided 2 Thermic Fluid

Heater(4 Lack Kcal) 9.0

PROPOSED

1 D. G. Set

(125 HP)

HSD

25

Lit/hr

10

meter

Adequate

stack height

will be

provided

SPM

SO2

NOX

adequate

stack

height will be

provided

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

Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height (meter) APCM

1

Vent

Attached to

Reactor

HCl

HBr

NH3

12 Water

scrubber

v Fugitive emission details with its mitigation measures.

Sources of fugitive emissions include storage of chemicals, solvents storage, loading and unloading section, raw material handling and, hazardous waste storage area. Mitigation Measures

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

• Hazardous chemicals will be stored as per standard criteria.

• Periodically monitoring will be carried out as per the post project monitoring plan.

• Proper ventilation in storage & production area shall be ensured

• All materials must be stored in suitable packing to

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prevent contamination of air .

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

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

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

• Good housekeeping will be maintained in the plant.

C 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


Category and

Schedule as

per HW Rules.

Quantity (MT/Annum) Disposal

Existing

Proposed

Total

1.

Discarded Containers/ Barrels/ Liner

Raw material storage

area

33.1 40 60 100 Collection, Storage, Reuse after decontamination or sent to authorized recycler.

2. Used Oil Machinerie

s 5.1 12 25 37

Sale to CPCB Registered Recycler / Re-use for machine Lubrication.

3. Process Residue

Process 28.1 - 138.5 138.5 Sent to CHWIF for the incineration.

4. Spent Charcol

Process 28.3 - 0.17 0.17 Sent to TSDF for landfilling.

5. Spent Solvent

Process 28.6 - 3.12 3.12 Sent to Common Incineration Plant for the incineration.

6. Distillation residue

Solvent Recovery

36.1 - 0.52 0.52 Sent to Common Incineration Plant for the incineration.

7. ETP Sludge

ETP 35.3 - 28.8 28.8 Sent to TSDF for the landfill.

ii Membership details of CETP, TSDF, CHWIF, Common MEE etc. • TSDF & CHWIF of BEIL is obtained.

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

-

D

i Solvent management (If any) Details of Solvent recovery (As per respective ToR)

97% Recovery will be carried out.



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month of 16thMarch 2017 to 15th June 2017 to determine the prevailing status of ambient air, land use,

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

was measured at eight locations. Monitoring was carried out for PM10, PM2.5, SO2, NOx, CO, HBr,

HCl, NH3 and VOC within10 km radius from the project site. The maximum concentrations of PM10,

PM2.5, SO2, NOx,CO, HBr, HCl, NH3 and VOC at each ambient air monitoring locations were

compared with NAAQS for industrial, residential, rural and other areas. Concentration of PM10 ranged

from 65.83µg/m3 to 80.59µg/m3. Concentration of PM2.5 recorded from minimum 25.01µg/m3 to

maximum 32.79µg/m3. Concentration of SO2 recorded ranged from minimum 6.93µg/m3 to maximum

10.71µg/m3. Concentration of NO2 recorded ranged from minimum 11.57µg/m3 to maximum

19.65µg/m3. Concentration of COfounded less than1.00µg/m3.Concentration of HBrfounded less

than1.00µg/m3.Concentration of HClfounded less than1.00µg/m3.Concentration of NH3founded less

than20.00µg/m3.Concentration of VOCfounded less than1.00ppm.The incremental Ground Level




with NAAQ standards.Committee observed that PP has proposed Natural gas as fuel for babyBoiler

and thermic fluid heater. Unit has proposed water scrubber for vent attached to reactor. The total

industrial water consumption after expansion will be 18.44 KLD which will be sourced from GIDC. The

industrial wastewater generation will be 2.3 KLD and which will be treated in ETP and discharge to the

ACPTCL. The domestic wastewater generation will be 2.5 KLD. The domestic wastewater will be

disposed of through Soak pit/septic tank.Technical presentation was made by the project proponent.


expansion and asked PP for compliance of existing conditions of CCA, details of public

complaints/public litigation if any and action initiated by the GPCB against the industrial unit which was

addressed by PP.

It is noted that product 5-Methyl [1,2,4] triazolo [3,4-b][1,3]benzothiazoleare agrochemical intermediates

and hence committee asked PP to submit an undertaking for deletion of the product from the proposed

product list. It is noted that waste water quantity will be sent to ACPTCL,GIDC, Ankleshwar for pursuing

complete zero liquid discharge.Committee deliberated on air pollution control measures for flue gas and

process emission, hazardous waste generation and management and risk assessment based on worst

case scenario. For the process gas emission, after scrubbing, bleed liquor management is not

addressed and hence PP is asked to incorporate details of bleed liquor under the Haz. and other

Waste(Management and Transboundary) Rules 2016. After going through presentation, committee

found all the TORs addressed satisfactorily.



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1. Readdress hazardous waste details considering bleed liquor from scrubber under the Hazardous and other Waste (Management and Transboundary)Rules, 2016.

2. Submit undertaking for deletion of 5-Methyl [1,2,4] triazolo [3,4-b][1,3]benzothiazole products which are intended for being used as Agrochemical intermediate.

3. Detailed Leak Detection and Repairing Programme (LDAR) for all the volatile organic solvents proposed for use in-house with detailed chemical properties including vapor pressure. LDAR shall endeavor prevention of losses of solvents to the best minimum extent.

20 SIA/GJ/IND2/71540/2017 M/s. Sahjanand Enterprise Plot No.434, Phase-II, GIDC-Vatva,Ahmedabad

Appraisal



• PP has submitted online application vide no. SIA/GJ/IND2/71540/2017dated 12/01/2018 for obtaining Environmental Clearance.

• The SEAC has recommended ToR to SEIAA and SEIAA has issued TOR to PP vide letter dated 01/05/2017.

• Project proponent has submitted EIA Report prepared by M/s: Excel Enviro Tech, Ahmedabad based on the TOR issued by SEIAA.

• This is an existing unit engaged in Synthetic Organic Manufacturingand now proposes for expansion as tabulated below:

Sr. no.

Name of the Products

CAS no. / CI no.


1 Spray drying of herbal & food products

--- 150 75 225 Textile and

paper dyeing

2 Blending & Mixing of Dyes

--- 50 --- 50 Textile and paper dyeing

3 Reactive Yellow ME4GL (Crude)

129898-77-7 Nil 5.0 5.0

Textile and paper dyeing

4 Reactive Golden Yellow R (Crude)

--- Nil 5.0 5.0 Textile and paper dyeing

5 Reactive Orange ME2RL(Crude)

79809-27-1 Nil 5.0 5.0


6 Reactive Orange MBRL(Crude)

35642-64-9 Nil 5.0 5.0


7 Reactive Black B(Crude)

12225-25-1 Nil 5.0 5.0


8 Reactive Black 22(Crude)

17095-24-8 Nil 5.0 5.0


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Page 130 of 137

9 Reactive Red HE8B(Crude)

71870-80-5 Nil 5.0 5.0


10 Reactive Red 45(Crude)

12226-22-1 Nil 5.0 5.0


11 Reactive Blue HER(Crude)

77907-32-5 Nil 5.0 5.0


12 Reactive Blue 49(Crude)

12236-92-9 Nil 5.0 5.0


Total 200 125 325

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


• During the meeting dated 15/03/2018, technical presentation made during the meeting by project proponent.


Sr. no.

Particulars Details


Existing:71 Lacs Proposed:20.42 Lacs Total:91.42

(1) Capital cost for EMS (Environmental Management System): 6.75 Lacs (2) Recurring cost towards the environmental protection measures: 51.73 Lacs per

Annum.


Existing: 740 Sq. m. Proposed: -- Total: 740 Sq. m.


Existing: 225 Sq. m. Proposed: -- Total: 225 Sq. m.


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

2. Indirect

D Water i


Vatva Industries Association, GIDC Water Supply

Status of permission from the concern authority. VIA/2017-18/407/122 Dt. 16/09/2017


Existing KLD



(A) Domestic 1.00 1.00 2.00

Process 0 18.0 18.00

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Boiler 0 1.00 1.00

Scrubber 0 1.00 1.00

Washing 1.00 5.00 6.00


Grand Total (A+B) 2.00 26.00 28.00

1) Total water requirement for the project: 28 KLD 2) Quantity to be recycle: -- 3) Total fresh water requirement: 28 KLD





(A) Domestic 0.80 0.80 1.6

Process 0 1.60 1.60

Boiler 0 0.20 0.20

Scrubber 0 0.20 0.20

Washing 1.00 5.00 6.00

Total Industrial 1.00 7.00 8.00

Total (A+B) 1.80 7.80 9.60

-

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

ETP : 10 KL/day and spray drier : 10 KL/day


Industrial: In house ETP and common spray drier or in house spray drier


common spray drier or in house spray drier

Membership of Common facility (CF) We will obtaining membership of CF.

vii Reuse/Recycle details (KLD) ---



Sr.

no.

Source of

emission

With Capacity

e.g. Boiler (8

TPH)

Stack

Height

(meter)

Name

of the

fuel

Quantity of

Fuel

MT/hr&

MT/Day

Type of

emissions

i.e. Air

Pollutants

APCM

1

Hot Air

Generator

(6 Lac Kcal/hr)

11 Natural

gas

PNG=600

SCM/day

PM

SO2

NOx

Dust Collector

followed by Bag

filter

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2

Hot Air

Generator (6

Lac Kcal/hr)

11 Natural

gas

PNG=600

SCM/day

PM

SO2

NOx

Dust Collector

followed by Bag

filter

3

Boiler (800

kg/hour) 12

Natural

gas

PNG=600

SCM/day

PM

SO2

NOx

Adequate stack

height


Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height

(meter)

APCM

Emission

Standards

1

Spray drier

(with HAG

running on

PNG)

PM 15 m

Cyclone Separator

Followed by Wet

Scrubber

PM<150

mg/Nm3

2

Spray drier

(with HAG

running on

PNG)

PM 15 m

Cyclone Separator

Followed by Wet

Scrubber

PM<150

mg/Nm3

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

For proposed products unit would be using Natural gas as a fuel in Boiler, which is eco friendly& less polluting. So, there will be no APCM is required. Adequate stack height is provided.


i

Sr. no.


waste


Category and

Schedule as per

HW Rules.

Quantity (MT/Annum)

Disposal Method

1 ETP

Sludge ETP

Process 35.3

20.0 MT/Annum

Collection,Storage,Transportation& disposalatTSDF

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2 Discarded

Containers/Drums

Mfg. process

33.1 1.8

MT/Month

Collection,Storage,Decontamination,

transportation&disposalbyselling to authorizedrecycler

3 Spent Oil Mfg.

process 5.1

17.0 Lit/year

Collection,Storage,Transportation,

disposalbysellingtoregistered refiners

4 Spray Dried

Waste Mfg.

process 26.2

1.0 MT/Month

Collection, Storage & Reuse in Blending Mixing of Dyes.


ii Membership details of TSDF, CHWIF etc. Membership for TSDF at Eco Care Infrastructure Pvt Ltd


As per local rules and regulation


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

The solvents get totally consumed in the product manufacturing; and there is no generation of spent solvent. Hence, there is no requirement of solvent recovery.


Not applicable





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

level topography, meteorology, ecology & socioeconomic outline. Baseline ambient air quality was

measured at six locations. Monitoring was carried out for PM10, PM2.5, SO2 and NOx within 5 km

radius from the project site. The maximum concentrations of PM10, PM2.5, SO2 and NOx at each

ambient air monitoring locations were compared with NAAQS for industrial, residential, rural and other

areas. Concentration of PM10 ranged from 72.72µg/m3 to 79.36µg/m3. Concentration of PM2.5

recorded from minimum 32.81µg/m3 to maximum 37.99µg/m3. Concentration of SO2 recorded ranged

from minimum 17.40µg/m3 to maximum 20.91µg/m3. Concentration of NO2 recorded ranged from

minimum 23.47µg/m3 to maximum 28.49µg/m3.The incremental Ground Level Concentration (GLC)

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

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

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

standards.Committee observed that PP has proposed natural gas as fuel for proposed boiler and hot air

generator. Unit has proposed cyclone separator followed by wet scrubber for spray dryer each. The

total industrial water consumption will be 28 KLD; which will be sourced from GIDC. The industrial

wastewater generation will be 8.0 KLD and will be treated in ETP followed by spray dryer. The domestic

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wastewater generation will be 1.6 KLD. The domestic wastewater will be disposed of through Soak

pit/septic tank.

PP mentioned that there was no previous EC and only CCA has been accorded. Further it is noted that

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

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

initiated by the GPCB against the industrial unit which was addressed by PP. Further it is informed that

entire quantity of 9.60 KLPD of treated waste water will be evaporated througha common spray drier or

in house spray drier. Deliberation regardingprocess gas emission, flue gas emission, air pollution

control measures, hazardous waste generation, its management and risk assessment based on worst

case scenario made by the committee. After going through presentation, committee found all the TORs

addressed satisfactorily.



1. Clarification of zero liquid discharge for entire quantity of treated waste water( 9.60 KLPD) to be made in-house or to be sent to common spray drying facility with necessary membership certificate of the common spray drying facility mentioning quantity of treated waste to be spray dried.

2. Validity of the data collected covered under the air, water, soil chapters with details of GPS coordinates, dates and other associated supporting documents.

21 SIA/GJ/IND2/18607/2017 M/s:Heubach Colour Pvt. Ltd. (Unit-1) GIDC Industries Estate, Plot No. 9002-9010,Phase IV, Ankleshwar, Bharuch

Reconsideration

Category of the unit : 5(f)

The aforementioned proposal obtained TOR from SEIAA on 01/05/2017. Proposal was

subsequentlyconsidered in SEAC meeting on 30/11/2018 for appraisal. After deliberation proposal was

recommended to SEIAA for grant of EC vide letter EIA-10-2017-7875-E-116 dated 16/01/2018. During

meeting of SEIAA on 31/01/2018,the proposal was referred back vide letter no. Dated 31/01/2018 by

mentioning the following point.

1. To verify the treatability and feasibility of stream wise & stage wise quality of waste water with

respect to RO and direction issued under section 18 (1)(b).

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2. To verify the utilization of excess steam generated from proposed boiler & detailed stream wise

steam balance.

3. To verify the quantification of spent sulphuric acid generation & its captive consumption each

product wise.

4. To verify the adequacy of ammonia scrubbing system with respect to CPC blue plant.

5. To verify the generation of ammonium sulphate & its disposal (if any) in CPC Blue Plant.

6. To verify the aspects of proposed CPP in the revised EIA report.

7. To verify the reduced water consumption in gardening with respect to increased gardening area

along with scientific calculation.

8. To explore the Possibilities for thermal destruction/evaporation of waste water generation from

proposed activity.

9. To verify details of revised EIA report submitted on 04/12/2017.

10. To verify the details of Hazardous waste generation with respect to its in-house utilization and

disposal as per Hazardous Waste Management Rules,2016.

Considering the aforementioned points, PP submitted reply on 14/02/2018. PP invited on 15/03/2018

for justification of points raised by SEIAA mentioned above. During presenting the queries, various

aspects were deliberated in depth and committee felt that aforementioned queries could not be

addressed satisfactorily by PP or their consultant, hence Committee asked PP to readdress the

aforementioned queries with technical justification in order to process the environmental clearance

application expeditiously.

Hence, committee decided that after submission of reply of aforementioned queries with proper

justification,proposal will be considered in one of the upcoming SEAC meeting.

22 SIA/GJ/IND2/18600/2017 M/s:Heubach Colour Pvt. Ltd. (Unit-2) Ankleshwar GIDC Estate, Plot No. A-406,444-446, GIDC, Ankleshwar, Bharuch.

Reconsideration


The aforementioned proposal obtained TOR from SEIAA on 01/05/2017.PP submitted final EIA on

22/09/2017.Earlier PP was called in SEAC meeting on 30/11/2018.Earlier Proposal was

consideredduring SEAC meeting held on 30/11/2018 for appraisal. Proposal was recommended to

SEIAA vide letter EIA-10-2017-7877-E-118 dated 16/01/2018 for grant of EC. SEIAA referred back the

proposal vide letter no. SEIAA/GUJ/EC/5(f)/20/2018 dated 31/01/2018 by mentioning the following

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point.

1. To verify the proposed Debottlenecking/modernization methods along with scientific report to no

increase in water consumption and waste water generation.


Considering the aforementioned points, PP submitted reply on 14/02/2018. PP invited on 15/03/2018

for justification of points raised by SEIAA mentioned above. During presenting the queries, various

aspects were deliberated in depth and committee felt that aforementioned queries could not be

addressed satisfactorily by PP or their consultant, hence Committee asked PP to readdress the

aforementioned queries with technical justification in order to process the environmental clearance

application expeditiously.


justification, proposal will be considered in one of the upcoming SEAC meeting.

23 SIA/GJ/IND2/18604/2017 M/s:Heubach Colour Pvt. Ltd. (Unit-3) GIDC Industries Estate, Plot No. 6105-6107-6111, Ankleshwar, Bharuch.

Reconsideration


The aforementioned proposal obtained TOR from SEIAA on 01/05/2017.PP submitted final EIA on

22/09/2017. PP was called in SEAC meeting on 30/11/2018 for appraisal. Subsequently, proposal was

recommended to SEIAA vide letter EIA-10-2017-7876-E-128 dated 16/01/2018. SEIAA referred back

the proposal vide letter no. SEIAA/GUJ/EC/5(f)/21/2018 dated 31/01/2018 by mentioning the following

point.

1. To verify the treatability and feasibility of stream wise & stage wise quality of waste water with

respect to RO and direction issued under section 18 (1)(b).

2. To verify the quantification of spent sulphuric acid generation & its captive consumption each

product wise.

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3. To explore the Possibilities for thermal destruction/evaporation of waste water generation from

proposed activity.


5. To verify the details of Hazardous waste generation with respect to its in-house utilization and

disposal as per Hazardous Waste Management Rules,2016.

Considering the aforementioned points, PP submitted reply on 14/02/2018. PP invited on 15/03/2018for

justification of points raised by SEIAA mentioned above. During presenting the queries, various aspects

were deliberated in depth and committee felt that aforementioned queries could not be addressed

satisfactorily by PP or their consultant, hence Committee asked PP to readdress the aforementioned

queries with technical justification in order to process the environmental clearance application

expeditiously.


justification, proposal will be considered in one of the upcoming SEAC meeting

Meeting ended with thanks to the Chair and the Members.

--------------------------------

Minutes approved by:


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


4. Shri Rajesh I. Shah, Member, SEAC.


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