minutes of the 550 meeting ofthe state level expert ... minutes of the 550th i.pdf · 1 550 th...

1

550th meeting of SEAC-Gujarat, dated 19.09.2019

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Minutes of the 550thmeeting ofthe State Level Expert Appraisal Committee held on 19/09/2019 at

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

The 550thmeeting of the State Level Expert Appraisal Committee (SEAC) was held on 19thSeptember

2019 at Committee Room, Gujarat Pollution Control Board, Sector 10A, Gandhinagar. Following

members attended the meeting:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

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

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

The regular agenda of Appraisal, Reconsideration&ToR cases were taken up. The Committee considered

the applications made by project proponents, additional details submitted as required by the SEAC/SEIAA

and details furnished in the Form-1, PFR, EIA-EMP reports.

Proposal No. Name and Address of the Unit Remarks

1 SIA/GJ/IND2/38454/2018 M/s. Ven Petrochem & Pharma India

Pvt Ltd

Plot No.2903,05,07,09,10,& 2704 to

2708, GIDC, Sarigam, Taluka :

Umbergaon, District : Valsad.- 396155

Appraisal

Category of the unit : 5(f)

Project status: Expansion

• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/38454/2018dated

30/08/2019 for obtaining Environmental Clearance.

• SEIAA issued TOR to PP vide their letter dated 10/01/2019.

• Project proponent has submitted EIA Report prepared by Anand Environmental Consultants Pvt Ltd,

Ahmedabadbased on the TOR issued by SEIAA.

• This is an expansion project for manufacturing of synthetic organic chemical as tabulated below.

Sr.

no.

Name of the Products CAS no. /

CI no.

Quantity (MT/Month) End-use of the

products Existing Proposed Total

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1 Acebrophylline

179118-73-

1

0.0

1.0 1.0 Anti-mucolytic

(for cough)

2 Ambroxol Hydrochloride 23828-92-4 0.0 6.6 6.6 Anti-mucolytic

(for cough)

3 Bromhexine Base

3572-43-8 0.0 1.0 1.0 For manufacture

of Bromohexine

Hydrochloride

4 Bromhexine

Hydrochloride

611-75-6 3.0 3.0 6.0 Anti-mucolytic

(for cough)

5 Timolol Maleate 26921-17-5 0.0 1.2 1.2 Anti –

Glaucoma

(for eye drops)

6 2-Amino-N-Methyl-N-

Cyclohexyl

Benzenemethanamine

57365-08-9 0.0 1.2 1.2 For manufacture

of Bromohexine

Hydrochloride

7. Sodium Bromide* 7647-15-6 10.7 93.2 103.9 Photographic

Chemical

8. Dimethyl Hydantoin* 77-71-4 0.5 1.1 1.6 For manufacture

of Dibromo

Dimethyl

Hydantoin

Total

14.2 108.3 122.5

• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006.

• PP was called for presentation in the SEAC meeting dated 19/08/2019.

• Salient features of the project are as under:

Sr.

No.

Particulars Details

A Total cost of Proposed Project

(Rs. in Crores):

Existing : INR 4.50 Crores

Proposed : 20 Crores

Total : INR 24.50 Crores

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B Total Plot area

( sq. meter)

Existing: 9690 .Sq. m.

Proposed: 2300 Sq. m. (from 9690 sqm)

Total: 9690 Sq. m.

Green belt area

( sq. meter)

Existing: 970.67. Sq. m.

Proposed: 240 Sq. m.

Total: 1210.67 Sq. m.i.e. 1211 Sq. m

C Employment generation Existing:83

Proposed:62

Total:145

D Water

i Source of Water Supply

(GIDC Bore well, Surface water, Tanker

supply etc...)

G.I.D.C

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

Obtained.

ii Water consumption (KLD)

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 4 4 8 --

(B) Gardening 1 1 2 --

(C) Industrial

Process 2.0 3.4 5.4 --

Washing 1.1 0.9 2.0 --

Boiler 12 12 24 --

Cooling 6 2 8 --

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Others 0.1 0.2 0.3 --

Industrial Total 21.2 18.5 39.7 --

Grand Total

(A+B+C)

26.2 23.5 49.7 --

1) Total water requirement for the project: 49.7KLD

2) Quantity to be recycled: 12KLD

3) Total fresh water requirement: 37.7KLD

iii Waste water generation (KLD)

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 2.4 2.4 4.8 --

(B) Industrial

Process 1.55 1.75 3.30 --

Washing 1.1 0.9 2.0 --

Boiler 4.5 3.5 8 Will be recycled

Cooling 3.0 1.0 4 Will be recycled

Others 0.1 0.2 0.3 --

Total Industrial waste

water

10.25 7.35 17.6 --

iv Treatment facility within premises with capacity

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

� Existing : Capacity of Incinerator – 250 kg/hour , 2.75 KLD incinerated within premises,

7.5 KLD recycled back

� Proposed: Capacity of Incinerator –500 kg/hour

� 2.85 KLD will be incinerated within premises / co processing, 4.5 KLD will be recycled back

after treatment.

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Treatment scheme including segregation at source.

� 4.8 KL / day domestic waste water generated will be disposed into septic tank /soak pit

system.

� 17.6 KL/day industrial waste water generated out of which 5.60 KL / day (3.30 KLDfrom

Process + 2.0 KLD from Washing + 0.3 KLD from Scrubber) will be incinerated in an

incinerator within premises or will be collected, stored, transported and disposed to cement

industries for co-processing AND 12 KL / day (8 KLD from boiler + 4 KLD from cooling) will

be recycled / reused back.

� Details are given in EIA report, Chapter – 2.

Note: (In case of CETP discharge) :

Management of waste water keeping in view direction under section 18 (1) (b) of the

Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding

compliance of CETP.

� Not Applicable.

Brief note on adequacy of ZLD (In case of Zero Liquid Discharge):

� Unit maintains ZLD by incinerating industrial waste water in an incinerator within premises

and the same practice will be continued after expansion or will be sent to cement

industries for co-processing.

v Mode of Disposal & Final meeting point

Domestic: 4.8 KL / day (existing + proposed) domestic waste water generated will be

disposed into septic tank /soak pit system.

Industrial: 5.60 KL / day (3.30 KLD from Process + 2.0 KLD from Washing + 0.3 KLD from

Scrubber) (existing + proposed) will be incinerated in an incinerator within

premises or will be collected, stored, transported and disposed to cement

industries for co-processing.

12 KL / day (8 KLD from boiler + 4 KLD from cooling) (existing + proposed) will

be recycled back.

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

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

� Not Applicable

Membership of Common facility (CF) - Not Applicable

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(For waste water treatment)

� Not Applicable

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

vii Reuse/Recycle details (KLD)

[Source of reuse & application area]

Total reuse 12 KLD

Source of waste water

for reuse with quantity in

KLD (From where it is

coming)

Application area

with quantity in

KLD (Where it is

used)

Characteristics of

waste water to be

reused (COD,

BOD,TDS etc.)

Remarks

regarding

feasibility

to reuse i.e.

Boiler condensate and

cooling water purge will be

the source of waste water

generated which is planned

to be used.

Approximately 8 KLD

of boiler condensate

and 4 KLD of cooling

purge water will be

reused back into the

boiler as well as back

for cooling makeup

� pH : 7- 8.5

� Suspended Solids : 150

– 200 mg/l

� TDS :1500 – 2000 mg/l

� Oil & Grease : 5 -10 mg/l

� COD : 80-100 mg/l

BOD : 10-20 mg/l

It is

completely

feasible to

use for

Boiler &

cooling

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.

4 recycle

Total water

consumption 37.7 (2nd day onwards)

(49.7-12)

Gardening

2

Domestic 8

Industrial 39.7

(27.7 +12)

Boiler 24

Process

5.40

Cooling make-up

8

To Incinerator / disposed to cement

industries for co-processing

5.60

Other (scrubbing)

0.3

Water from GIDC

Septic tank/soak pit

4.8

Washing

2

4 8 3.30 0.3 2

Recycle back

12

8 recycle 4 fresh 16 fresh

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Existing & Proposed

- Existing

Sr.

no. Source of

emission

With Capacity

Stack

Height

(meter)

Type

of Fuel

Quantity of

Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1. Boiler

1000 kg / hour

11 PNG 25 scm/hr PM

SO2

NOX

--

2.

D.G. Set

(250 KVA)

5 Diesel 25 lit/hr PM

SO2

NOX

--

3. Incinerator

(250 kg/hr)

30* PNG

25 scm/hr PM

SO2

HCl

Dust Collector

followed by

scrubber

- Proposed

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter

)

Type

of Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air Pollution

Control

Measures

(APCM)

1. Boiler

1000 kg /

hour

12 PNG 25 scm/hr PM

SO2

NOX

--

2.

D.G. Set

(250 KVA)

5 Diesel 25 lit/hr PM

SO2

NOX

--

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3. Incinerator

(500 kg/hr)

30* PNG

50 scm/hr

PM

SO2

HCl

Dust

Collector

followed by

scrubber

**This will be a common stack for existing as well as proposed expanded incinerator

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

Existing & Proposed

- Existing

Sr.

no.

Specific Source of emission

(Name of the Product &

Process)

Type of

emissi

on

Stack/Vent

Height

(meter)

Air Pollution

Control

Measures

(APCM)

1 Bromination Vessels (2 Nos).

(Bromohexine Hydrochloride &

During bromination reaction )

HBr

Br2

12 Two separate

two Stage Alkali

Scrubber

- Proposed

Sr.

no.

Specific Source of emission

(Name of the Product &

Process)

Type of

emissio

n

Stack/Ven

t

Height

(meter)

Air Pollution

Control

Measures

(APCM)

1 Bromination Vessels (2 Nos).

(Ambroxol Hydrochloride/

Acebrophylline & During

Bromination reaction,

Bromhexine base & During

Bromination reaction)

HBr

Br2

10 Two separate

two Stage Alkali

Scrubber

iii Fugitive emission details with its mitigation measures.

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� Concrete road is/will developed within plot premises to avoid fugitive dust due to vehicle

movement.

� Manufacturing activity will be carried out in closed reactors / vessels and regular checking and

maintenance of the same will be carried out to avoid any leakage and relative fugitive

emissions.

� All the raw materials will be stored in closed containers and in sealed bags and will be handled

through closed system to avoid the handling losses and relative fugitive emissions.

Water sprinkling will be done to avoid dust emission.

F Hazardous waste

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

2016).

Existing & Proposed

i Sr.

no

.

Typ

e/N

am

e o

f

hazard

ou

s

waste

Sp

ecif

ic

So

urc

e o

f

gen

era

tio

n

(Nam

e o

f th

e

Cate

go

ry a

nd

Sch

ed

ule

as Quantity (MT/Annum)

Man

ag

em

en

t

of

HW

Exis

tin

g

Pro

po

sed

To

tal

1. (a) ETP

Sludge

From Wet

Scrubbers

35.3 14.4 28.8 43.2 Collection,

Storage,

Transportat

ion and

Disposal at

TSDF –

BEAIL

Ankleshwar

/ VWEMCL

– Vapi.

(b) ETP

Sludge

From

treatment of

water to be

recycled

-- 24 24

Total (a+b) 14.4 52.8 67.2

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2.

Process

waste water

*

From

manufacturing

process of

Acebrophyllin

e, Ambroxol

hydrochloride,

Bromhexine

Base,

Bromhexine

Hydrochlorid,

Timolol

Maleate,

2-Amino-n-

methyl-n-

cyclohexyl

benzenemeth

anamine

28.1 -- 1680 168

0

Collection,

Storage,

Transportat

ion and

disposed to

cement

industries

for co-

processing

or

Incineration

.

Distillation

Residue

From

manufacturing

process

28.1 0.36 35.64 36 Collection,

Storage,

Transportat

ion and

disposed to

cement

industries /

RSPL –

Panoli for

co -

processing.

3. Used Spent

Oil

From

lubrication or

D.G. Set

5.1 0.08 11.92 12 Collection,

Storage,

Transportat

ion and

Disposal by

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selling to

registered

reprocesso

rs.

4. Empty

barrels /

containers /

liners

contaminate

d with

hazardous

chemicals /

wastes

From raw

materials

33.1 2.7 27.3 30 Collection,

Storage,

Decontami

nation,

Transportat

ion and

Disposal by

selling to

authorized

recycler.

5. Spent

Carbon

From

manufacturing

process of

Acebrophyllin

eAmbroxol

hydrochloride,

Bromhexine

Base,

Bromhexine

Hydrochloride

, Timolol

Maleate,2-

Amino-n-

methyl-n-

cyclohexyl

benzenemeth

anamine

28.3 1.2 13.2 14.4 Collection,

Storage,

Transportat

ion and

Disposed

to cement

industries /

RSPL -

Panoli.

6. Incineration

Ash*

From

Incinerator

37.2 35 51.4 86.4 Collection,

Storage,

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Transportat

ion and

Disposal at

TSDF site

of M/s.

BEAIL/

Ankleshwar

/ VWEMCL,

Vapi

7. Date expired

–off

specification

process

Expired

Products

28.4 0.005 0.115 0.12 Collection,

Storage,

Incineration

within unit.

8. Sodium

Bromide

Solution**

From

manufacturing

process

- 128.4 1118.4 124

7

Will be

collected,

stored,

transported

and sold to

authorized

end users

registered

under Rule

-9 and

users

having

PCB

Approvals.

9. Dimethyl

Hydantoin**

From

manufacturing

process

- 6 13.2 19.2 Will be

collected,

stored,

transported

and sold to

authorized

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end users

registered

under Rule

-9 and

users

having

PCB

Approvals.

10

.

Bleed Liquor From

Scrubbing

1.2 2.4 3.6 Will be

incinerated

in an

incinerator

within

premises.

Note* - generated if process waste is not disposed for co – processing and is incinerated within

premises.

**- By-Products

ii Membership details of TSDF, CHWIF etc.

(For HW management)

BEAIL,VWEMCL, RSPL

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 etc. (Details in Table Format)

Sr.

No.

Name of Product Name of Raw

Materials

/ Solvent

Raw Materials/

Solvent to be

Used

Raw Materials /

Solvent to be

Recovered

(MT/Month) (MT/Month) (%)

1. Bromhexine

hydrochloride

Industrial spirit 51200 49150 96

Methanol 18720 17800 95

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Mono

chlorobenzene 18000 17640 98

Toluene 76080 73110 96

2. 2-amino-n-methyl-n-

cyclohexyl

benzenemethanamine

Methanol 7488 7120 95

Mono


Toluene 16512 15860 96

3. Bromhexine base Industrial spirit 3036 2916 96

Methanol 3276 3115 95

Mono


Toluene 12964 12444.3 96

4. Ambroxol hydrochloride Acetone 3360 3180 95


Methanol 56160 53400 95

N-butanol 15840 15240 96

Toluene 103200 99060 96

5. Acebrophylline Acetone 970 922 95


Methanol 6180 5870 95

N-butanol 4840 4650 96

Toluene 17181 16459 96

6. Timolol maleate Acetone 7680 7220 94

Tert-butanol 5520 5280 96

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Toluene 12672 12048 95

Recovered solvents will be reused in process.

ii VOC emission sources and its mitigation measures

Closed loop systems, double mechanical seal pumps will be provided to reduce VOC emission

as much as possible.

H � Details regarding storage of Hazardouschemicals

Storage details Name of major Hazardous Chemicals Remarks

Storage tanks Hydrochloric acid

Drum/Barrel storage

Acetic acid, Acetone, Benzaldehyde, Benzoic

acid, Hydrazine hydrate, Industrial spirit,

Liquor ammonia, Maleic acid, Methanol,

Mono chlorobenzene, N-butanol, N-

methylcyclohexylamine, Ortho nitro

benzaldehyde, Ortho nitro toluene, Sodium

hydride, Sodium hydrosulphite, Soidum

borohydride, Tert-butanol, Theophylline,

Toluene, Trans-4-amino cyclohexanol

--

� Applicability of PESO : --

• During the meeting dated 19/08/2019, technical presentation made by the Project proponent.

• During the meeting, the project was appraised based on the information furnished in the EIA Report

and details presented during the meeting.

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

viz. air, noise, water, biological and socioeconomic aspect for the study area of 10 km radial distance

from project site for the period January 2019 to March2019. Ambient Air Quality monitoring was

carried out for PM10, PM2.5, SO2, NOx, HCl, HBr, & VOC as Benzene, Toluene & Xylene at eight

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

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

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

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

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

Ambient Air Quality Standards (NAAQS).

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

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

Emergency Plan has been covered in the RA report.

• During SEAC meeting on 19/08/2019, committee noted that the proposal is for expansion. This unit

has valid CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP ensured that

there are no court cases pending and no public complaints against the project. Source of water is

GIDC.PP mentioned that entire effluent generated after expansion from process, washing & scrubber

will be incinerated in in-house incinerator or will be sent to co-processing in cement industries. PP

mentioned that effluent generated from boiler blow down & cooling tower blow down will be recycled

back in the same process. Unit will maintain complete ZLD. PP has proposed one boiler & one

incinerator. Fuel used will be PNG. Committee noted that PP has not addressed LDAR (Solvent

Recovery) product wise and committee asked PP to submit revised LDAR product wise. Committee

also noted that PP has not addressed Hazardous Waste as per HWR – 2016 and was asked the

submit the revised table eliminating the by-product and incorporating the same in Hazardous Waste

Matrix. Committee also noted that PP has not satisfactorily address the likely impacts of project and

its mitigation measures along with technical details pertaining to best available technologies (BAT) for

the proposed project considering the expansion of existing products.

• After detailed discussion, it was decided to consider the proposal only after submission of the

following documents:

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

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

prevention of losses of solvents to the best minimum extent. Address all the solvents product wise

separately.

2. Technical Justification for direct recycle/reuse of utility effluent along with its treatability &

feasibility.

3. Technical details of the plant/s along with details on best available technologies (BAT), proposed

technology and reasons for selecting the same.

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

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significance and based on corresponding likely impacts VECs (Valued Environmental

Components) may be identified. Baseline studies may be conducted within the study area for all

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

order to identify mitigation measures.

5. Revised Hazardous Waste Matrix addressing the by-product in Hazardous Waste as per HWR –

2016.

2 SIA/GJ/IND2/39992/2018 M/s. Altis Fine Chem Pvt. Ltd.

Survey No. 192, Near Katwad Patiya,

Dalpur, Prantij, Sabarkantha.

Appraisal

Category of the unit : 5(f)


• Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/39992/2018dated

30/08/2019 for obtaining Environmental Clearance.

• SEIAA issued TOR to PP vide their letter dated 28/01/2018.

• Public Hearing of the Project was Carried Out at Project Site of M/s.Altis Fine Chem Pvt Ltd,

Located at Survey No. 192, Near Katwad Patiya, Dalpur, Prantij, Sabarkantha. by Gujarat Pollution

Control Board dated 18/06/2019.

• Project proponent has submitted EIA Report prepared by Bhagwati Enviro Care Pvt. Ltd,

Ahmedabadbased on the TOR issued by SEIAA.

• This is an expansion project for manufacturing of synthetic organic chemical 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 Quinine

Sulphate

207671-44-

1 1 0 1

Pharmace

uticals

Drugs &

Drugs

Intermedia

tes

2 Ethyl-5

(piperazine-

yl-

benzafuran 2

carboxylate

765935-67-

9 1 0 1

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HCL)

3 3(4-

chlorobutyl)-

1H-Indole-5-

carbonitrile

143612-79-

7 1 0 1

4 Alanyl-L-

Glutamine 39537-23-0

0 8 8 5 2,3

Dihydroxy

Phthalazine-

1,4-Dione

1445-69-8

6 Alpha Keto

Isoleucine

Calcium Salt

66872-75-1 0 3 3

7 Alpha Keto

Leucine

Calcium Salt

51828-95-6 0 3 3

8 Alpha Keto

Phenyl

Alamine

Calcium Salt

54865-40-6 0 3 3

9 Alpha Keto

Valine

Calcium Salt

51828-94-5 0 3 3

10 Alpha

Hydroxy

Methionine

Calcium Salt

135236-72-

5 0 3 3

11 Aripiprazole 129722-12-

9 0 24 24

Total 3 47 50

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• The project falls underCategory B of project activity 5(f) asper the schedule of EIA Notification 2006.

• The unit is located outside GIDC, Complying the three conditions as per the amendment with EIA

Notification, 2006 vide SO 1599 (E) dated 25/06/2014. [The Water consumption less than 25 m3/day

(22.4 KLD); Fuel consumption is less than 25 TPD (0.92 MT/day); and not covered in the category of

MAH units as per the Management, Storage Import of Hazardous Chemical Rules (MSIHC Rules),

1989]


• Salient features of the project are as under:

Sr.

no.

Particulars Details


(Rs. in Crores):

Existing: 3.57 Crore

Proposed: 5.9 Crore

Total: 9.47 Crore

Details of EMP

Sr.

No

System Approximate

recurring

cost per

annum

(in Lacs)

Approximate

capital cost

(Rs. In Lacs)

Basis for cost estimates

1

Air pollution

control

2.0 8.0

The capital cost would include

cost of providing adequate height

of the stack, ladder and platform,

Air Pollution Control Systems and

recurring cost would include cost

of monitoring of air environment.

2

Water

pollution

control

160.0 10.0

Capital cost would include cost of

ETP, Evaporation cost of Spray

Drying etc. In capital cost civil

work, mechanical work, Electrical

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work and piping work is included.

Recurring cost is for operational

phase.

3

Noise

pollution

monitoring

0.25 0.0

The recurring cost would include

cost of noise monitoring.

4

Solid and

hazardous

waste

management

3.0 10.0

Capital cost would include cost of

providing storage space for

hazardous waste and

membership of TSDF Fee.

Recurring cost would include cost

of land filling and transportation.

5

Environment

monitoring

and

management

1.0 1.0

The recurring cost would be

incurred on hiring of consultants

and payment of various statutory

fees to regulatory agencies.

6 Green belt 1.0 0.0

Development of Greenbelt

including Gardening and

Plantation.

7 Occupational

health (OHC) 1.5 1.0

Occupational health check up of

Employees and workers

Total 168.75 30

Details of CER as per OM dated 01/05/2018

9.6 Lacs for Three Year

(1.0 % of Total Project

Cost) For Brownfield

Project

M/s. Altis Fine Chem Pvt. Ltd. CER Budget:

9.6 Lacs (For Three Year)

Propose Planning for CER Activity (2019-2021)

21


of 106

Cost in Lacs/Yr

2019 2020 2021

− 1.5 Lacs for Education

at Primary School of

Dalpur village.

i.e. will be provided

stationary, Books,

UniformO

− 1.0 Lacs for drinking

water facility provided in

Vajapur.

_Providing drink.ing water

station

− 1.0 Lacs for drinking

water facility.

_Provide Drinking Water

Stand at Katwad Patiya

for local people (near

our industries).

− 1.0 Lacs for Drinking

Water facility provided

in Dalpur village.

_Provided Drinking

Water Station

in Dalpur village.

− 1.5 Lacs for Education at

Vajapur village.

(Aganwadi Center &

primary school -Vajapur)

− 2.2 Lacs for Trees

Plantation at Vajapur

village. (with help of

local people)

Trees Plantation at

nearHathmati Canal.

Greenbelt area develop

inMehsana Highway

with help oflocal NGO.

− 0.7 Lacs for Green belt

area develop at near

Katwad Patiya with

help of local people

− 0.7 Lacs for trees

Plantation in Dalpur

village.

_with help of local people &

local

NGO.

Total: 3.2 Lacs Total: 3.2 Lacs Total: 3.2 Lacs

B Total Plot area

( sq. meter)

Existing: 17806 Sq. m.

Proposed: 0

Total: 17806 Sq. m.

Green belt area

( sq. meter)

Existing: 800 Sq. m.

Proposed: 5200 Sq. m.

Total: 6000 Sq. m.

C Employment generation Existing: 22

22


of 106

Proposed: 50

Total: 72

D Water

i

Source of Water Supply

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

Borewell

Status of permission from the concern authority.

Applied to CGWA

ii

Water consumption (KLD)

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic 0.8

1.2 2.0

(B) Gardening

0 2.0 2.0

(C) Industrial

Process 1.4

14 15.4

Washing 0.5

0.5 1.0

Boiler 0.5

1.5 2.0

Industrial Total

2.4 16 18.4

Grand Total

(A+B+C)

3.2 19.2 22.4

1) Total water requirement for the project: 22.4 KLD

23


of 106

2) Quantity to be recycled: 0

3) Total fresh water requirement: 22.4 KLD

(Total water requirement = Fresh water + Recycled water)

iii

Waste water generation (KLD)

Category Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(A) Domestic

0.8 1.2 2.0

(B) Industrial

Process 1.2

14 15.2

Washing 0.5

0.5 1.0

Boiler 0.05

0.15 0.2

Total Industrial

waste water

1.75 14.65 16.4


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

etc..

� ETP (Cap-40 KLD Primary & Tertiary Treatment Unit)

Treatment scheme including segregation at source. (Give Characteristics of

each stream i.e. COD, BOD, TDS etc.)

� Industrial Effluent Generation: 16.4 KLD _ goes to ETP (Cap-40 KLD,

having Primary & Tertiary Treatment Unit) then send to Common Spray

Drying Facility at Chhatral Environment Management System Pvt. Ltd. -

Dhanot for Spray Drying.

24


of 106


Management of waste water keeping in view direction under section 18 (1) (b)

of the Water (Prevention and Control of Pollution) act, 1974 issued by CPCB

regarding compliance of CETP.

� Not Applicable











Domestic:

2.0 KLD discharge to Soak pit via septic

tank.

Industrial:

Industrial Effluent Generation: 16.4 KLD _

goes to ETP (Cap-40 KLD, having

Primary & Tertiary Treatment Unit) then

send to Common Spray Drying Facility at

Chhatral Environment Management

System Pvt. Ltd. - Dhanot for Spray

Drying.

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

CHWIF etc.

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

� Common Spray Drying Facility at Chhatral Environment System Pvt. Ltd. –

Dhanot

25


of 106

Membership of Common facility (CF)


Common Spray Drying Facility at Chhatral Environment System Pvt. Ltd. - Dhanot


vii Reuse/Recycle details (KLD)

[Source of reuse & application area]

Total reuse: 0

E Air


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

KVA etc.

Existing & Proposed

-

Sr.

no.

Source

of

emission

With

Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

26


of 106

1

Boiler

(800

kg/hr)

(Existing)

12

Extra

cted

Bark

Wast

e

0.4

Particulate

Matter

SOx

NOx

Dust

Collector

2

Boiler

(3 MT)

(Propose

d)

30

White

Coal

OR

Briqu

ettes

0.92

Particulate

Matter

SOx

NOx

Multi

Cyclone

Dust

Collector

followed by

Bag Filter

- We will dismantle our existing Boiler (800 kg/hr) after obtaining Environment

Clearance.


Existing & Proposed

- There will be no process gas emission in existing as well as proposed activity.


Fugitive emission will due to the leakages in pump, storage container, material

transferring, and packing.

Mitigation measures:

• Proper storage of raw materials, products and fuels

• Ensuring closed feeding and sampling.

• Establishing SOPs for start-up, shut down and maintenance operational

procedure

• Regular work place and ambient air quality monitoring will be done.

F Hazardous waste

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

Movement) Rules 2016.

Existing & Proposed

i

Sr

.

Type/Na

me of

Specific

Source

Categor

y and

Quantity

(MT/Annum)

Manageme

nt of HW

27


of 106

no

.

Hazardou

s waste

of

generati

on

(Name of

the

Activity,

Product

etc.)

Schedu

le as

per HW

Rules.

Existin

g

Propose

d

Tot

al

1

ETP

Waste

Effluent

treatment

plant

35.3 12 3 15 Collection,

Storage,

Transportat

ion &

Disposed at

TSDF

2

Spent

Oil/Used

Oil

Lubricatio

n of plant

machineri

es


Storage,

Transportat

ion &

Disposed

by reuse as

lubricant in

the plant

3

Discarded

Container

s (Bag,

Barrel,

Drum)

Raw

material

section


Storage,

Transportat

ion &

Disposed

by return

back to

supplier.

4 Process

Waste

(Bark)

From

Quinine

-- 310.5

6

0 310

.56

Collection,

Storage,

Transportat

28


of 106

Sulphate

mfg.

process

ion & sale

to Rule 9

authorized

industries.

5

Distillation

Residue

Generate

d from

distillation

process

of

Toluene,

Methanol,

MTBE,

MDC,

Ethyl

Acetate,

Acetone,

Di ethyl

ether, IPA

36.1 0 19.32 19.

32

Collection,

Storage,

Transportat

ion and

disposal to

CHWIF.

6

Spent

Solvent

Generate

d from

distillation

process

of

Toluene,

Methanol,

MTBE,

MDC,

Ethyl

Acetate,

Acetone,

Di ethyl

ether,

-- 0 1798.32 179

8.3

2

Collection,

Storage,

recover &

reuse in

manufacturi

ng process

at our

premises.

29


of 106

IPA.

-


(For HW management)

TSDF – Eco Care Infrastcture

Limited

iii Details of Non-Hazardous waste & its

disposal(MSW and others)

No




MT/MT (Batch Size 1 MT)

S

r.

N

o.

Product

Name

Solve

nt

Name

Prod

uct

Qty.

(MT/

M)

Solv

ent

use

Spent

Solve

nt

Lo

ss

Reco

ver

Solve

nt

Distilla

tion

Residu

e

Recov

ery %

1 Quinine

Sulphate

Tolue

ne 1 2 1.99

0.0

1 1.98 0.01 99.49

2

Ethyl-5

(piperazin

e-yl-

benzafura

n 2

carboxylat

e HCL)

Ethyl

Aceta

te

1 6.52 6.5 0.0

2 6.47 0.03 99.54

3

3(4-

chlorobutyl

)-1H-

Indole-5-

carbonitrile

MDC 1 8 7.98 0.0

2 7.93 0.05 99.37

4 Alanyl-L-

Glutamine

Metha

nol 8 6.51 6.5

0.0

1 6.46 0.04 99.38

30


of 106

5

Alpha Keto

Isoleucine

Calcium

Salt

MTBE 3 2.07 2.05 0.0

2 2.02 0.03 98.54

6

Alpha Keto

Leucine

Calcium

Salt

MTBE 3 2.1 2.07 0.0

3 2.04 0.03 98.55

7

Alpha Keto

Phenyl

Alamine

Calcium

Salt

MTBE 3 1.72 1.7 0.0

2 1.67 0.03 98.24

8

Alpha Keto

Valine

Calcium

Salt

Aceto

ne 3 0.97 0.94

0.0

3 0.92 0.02 97.87

Di

ethyl

ether

3 2.31 2.3 0.0

1 2.28 0.02 99.13

9

Alpha

Hydroxy

Methionine

Calcium

Salt

Metha

nol 3 1.85 1.83

0.0

2 1.8 0.03 98.36

1

0

Aripiprazol

e

Iso

Propy

l

Alcoh

ol

24 2.05 2.03 0.0

2 2 0.03 98.52


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

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

according implementation

H � Details regarding storage of Hazardous chemicals

31


of 106

Storage details Name of major

Hazardous chemicals

Remarks

Storage tanks

Toluene Tank Size: –

10 MT

Drum/Barrel storage

− Acetone

− Ethyl Acetate

− Hydrazine Hydrate

− Hydrochloric Acid

− Iso Propyl Alcohol

− Sodium Hydroxide

− Sulphuric Acid

− Titanium Tetra

Chloride

Drum – 50

kg, 100 kg,

150 kg, 200

kg

� Applicability of PESO :

� PESO Permission obtained for Storage of 15 KL Raw Material


• During the meeting, the project was appraised based on the information furnished in the EIA Report

and details presented during the meeting.

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

viz. air, noise, water, biological and socioeconomic aspect for the study area of 10 km radial distance

from project site for the period October 2018 to December2018. Ambient Air Quality monitoring was

carried out for PM10, PM2.5, (SO2), (NOx), HC, CO and VOCsat eight locations, including the project

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

Level Concentration (GLC) has been computed using AERMOD. The resultant concentrations are

within the NAAQS. The modeling study proved that the air emissions from the proposed plant would

not affect the ambient air quality of the region in any significant manner. The ambient air quality

around the proposed project site will remain within the National Ambient Air Quality Standards

(NAAQS).

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

32


of 106

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

Emergency Plan has been covered in the RA report.

• During SEAC meeting on 19/09/2019, committee noted that the proposal is for expansion. This unit

has valid CC&A for existing unit. Copy of CC&A, its compliance report is submitted. PP ensured that

there are no court cases pending and no public complaints against the project. Source of water is

Bore well.PP mentioned that entire effluent generated after expansion from process, boiler blow down

& washing shall be treated in in-house primary & tertiary ETP and treated effluent will be sent to

Common Spray Drying Facility at Chhatral Environment System Pvt. Ltd. – Dhanot. PP mentioned

that they will dismantle the existing boiler. PP has proposed one new steam boiler. Fuel used will be

White Coal. PP has addressed Hazardous Waste as per HWR – 2016.

• After detailed discussion, it was decided to forward the proposal to SEIAA, Gujarat for grant of

Environment Clearance.

3 SIA/GJ/IND2/37351/2018 M/s. Transworld Furtichem Pvt Ltd

Plot No. 353 to 367, Sector-4, KSEZ,

Gandhidham, Kutchh.

Appraisal

• PP remained absent in the EC – Appraisal presentation held on 19/09/2019.

• After detailed discussion, Committee decided to defer the proposal and consider the same in

one of the upcoming meeting of SEAC.

4 SIA/GJ/IND2/38556/2019 M/s. Anju Life Science

Plot No. C-261, G.I.D.C. Industrial

Estate, Saykha, Tal: Vagra, Dist.:

Bharuch, Gujarat – 391340.

Screening &

Scoping

• PP remained absent in the Screening & Scoping presentation held on 19/09/2019.

• After detailed discussion, Committee decided to defer the proposal and consider the same in

one of the upcoming meeting of SEAC.

5 SIA/GJ/IND2/40809/2019 M/s. Ooxylic Solutions

Plot No.33 & 36 GIDC Estate, Sojitra,

Anand.

Screening &

Scoping

Category of the unit: 5(f)

Project status: New

• This office has received an application vide their online proposal no. SIA/GJ/IND2/40809/2019 dated

33


of 106

29/08/2019 made by project proponent (PP) regarding grant of Terms of Reference [ToR] for

preparation of EIA/EMP report.

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

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

Sr.

No.

Name Of Product

CAS NO. Production

Capacity

MT/Month

End use of the product

as

1 Equilibrium Peracetic acid

(35%)

79-21-0 500 Cleaning agent in addition

to a cold disinfectant,

Synthesis of Alkenes &

Organic Compound

2 Distilled Peracetic acid (65

%)

79-21-0 100 Cleaning agent in addition

to a cold disinfectant,

Synthesis of Alkenes &

Organic Compound

3 2-Phenyl Propionic acid 492-37-5 20 2-Phenylpropionate is an

intermediate in alpha-

Methyl styrene (2-

phenylpropylene)

metabolism

4 Alpha Pinene Oxide

OR

Alpha Campholenic Aldehyde

1686-14-2

OR

110 Food additive, flavor

5 Sodium Acetate Powder 127-09-3 127 Sodium acetate is added

to food to help prevent

bacterial growth

6 Different Epoxides

1) Styrene oxide 96-09-3 50 Fragrance, Electronics,

Automotive

2) Limonene oxide 203719-54-4 Air fresheners, fragrance,

Cleaning, Washing, Food

Additive

34


of 106

3) Isopulegol epoxide 13834-13-4 Active compounds and

pharmaceuticals

4) Linalool oxide 1365-19-1 Fragrance

TOTAL 907 -

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


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

Sr.

no.

Particulars Details

A


(Rs. in Crores):

3.5Crore.

B Total Plot area ( sq. meter)

2107Sq. m.

Green belt area

( sq. meter)

710.11 Sq. m.

C Employment generation

12

D Water

i



GIDC Estate, Sojitra

Status of permission from the concern authority. GIDC, Sojitra. has allotted the plot

with commitment to provide

infrastructure facility and water

requirement

Ii


35


of 106

Sr. No. Water required for Quantity

(KLD)

Remark

1. Domestic 1.0 1.0 KLD Fresh Water

2. Gardening 1.0 1.0 KLD Fresh Water

3. Industrial

a. Process 0.0 DM water will be used.

b. Cooling 3.0 3.0 KLD Recycle Distillate

c. Washing 0.2 0.2 KLD Fresh Water

Total (a+b+c) 3.2 0.2 KLD Fresh Water

3.0 KLD Recycled Water

Total (1+2+3) 5.2 2.2 KLD Fresh Water

3.0 KLD Recycled Water

Note: Total Fresh Water Consumption: 5.2 KLD

Reuse: 3.0 KLD

After Reuse Fresh Water Consumption: 2.2 KLD

Iii


Sr. No.

Waste Water

Generation

Quantity (KLD) Remark

1. Domestic 0.8 Discharge to Soak pit

2. Gardening - -

3. Industrial

a. Process 10.6 7.6 KLD will be Reused

as DM water in to

Process & 3.0 KLD

Cooling as make up

b. Cooling 0.3 0.3 KLD will be treated

in To ETP

c. Washing 0.2 0.2 KLD will be treated

in To ETP

Total (Industrial to

ETP)

11.1 10.6 KLD will be

Recovered & reused in

36


of 106

Processand cooling

make up

+

0.5 KLD will be treated

in To ETP

� 0.8 KLD Domestic Effluent will be Discharge to be soak pit.

� 0.5 KLD Industrial Effluent will be treated in the ETP & evaporated by steam jacketed

evaporator.

� 10.6 KLD distillate water will generate during manufacturing of Sodium Acetate

Solution, 7.6 KLD will be recovered and reused in process and 3.0 KLD will be as

cooling tower makeup.

Iv Treatment facility within premises with capacity

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

� ETP (Primary) + Evaporator


� ETP (Primary) + Evaporator


Management of waste water keeping in view direction under section 18 (1) (b) of the

Water (Prevention and Control of Pollution) act, 1974 issued by CPCB regarding

compliance of CETP.

� No


� Treated effluent will be treated in ETP and evaporated by steam jacketed evaporator.

V Mode of Disposal & Final meeting point

Domestic: Soak pit

Industrial: ZLD

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

of CF

� NA

37


of 106



� NA

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

viii Reuse/Recycle details (KLD)

Total reuse : 10.6KLD

Source of waste

water for reuse

with quantity in

KLD (From where

it is coming)

Application

area with

quantity in

KLD (Where it

is used)

Characteristics of

waste water to be

reused (COD, BOD,

TDS etc.)

Remarks

regarding

feasibility to

reuse i.e.

Condensate from

distillation process

of manufacturing

Sodium Acetate

7.6 KLD in

Process

pH: 7.51

COD:9

BOD:3

TDS:100

It is distillate

can be used

as DM water

38


of 106

water- - - -

E Air



Sr.

No

.

Stack

Attached

to

Stack

Heig

ht

(m)

Fuel

Used

Quantity

of Fuel

Pollutants

Permissible

Limit

APCM

1.

TFH

5 Lac

Kcal

15 Natural

gas/

Agro

Waste

300

SCM/

0.8 TPD

PM/NOx-

/SO2

PM<150

mg/Nm3

SO2<100

PPM/

NOx<50 PPM

Adequate

Stack

Height/

Dust

Collector

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

� No Process gas emission

iii Fugitive emission details with its mitigation measures:

As below:

Proposed project is of manufacturing of S. O. Chemicals. Followings Measures will take for

existing & proposed project.

� Maintaining the house keeping regularly

� Transferring the liquid materials by pump

� To carry out regular leak detection and repair activities

� Proper routine maintenance of equipment reduces the likelihood of leaks

F Hazardous wastes

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

Rules 2016.

i

Sr.

No. Waste

Category

as HWM

Rules 2016

Source

Quantity

(MT/

Year)

Management Facility

39


of 106

1 ETP sludge

34.3

ETP 2

Collection, storage,

transportation, disposal at

the approved TSDF site

2 Distillation

Residue SCH-I/ 20.3

Solvent

Recovery

1


transportation, disposal at

the approved CHWIF site

3 Spent

Solvent SCH-I/ 28.6

Manufacturi

ng process

of

Campholeni

c Aldehyde,

2-Phenyl

Propionic

acid, Alpha

Pinene

Oxide

Alpha

Campholeni

c Aldehyde,

Different

Epoxides

464 Collection, storage,

transportation & reusing in

next batch.

4 Discarded

Containers 33.1

Materials

container

0.5


transportation, disposal by

selling to Registered

recycler.

5 Used Oil 34.3 Machinery

0.01


transportation, disposal by

selling to Registered

recycler.


(For HW management)

Membership of TSDF/CHWIF site

will be carried out before starting

the production activity.

iii Details of Non-Hazardous waste & its disposal Non Hazardous recycling waste

40


of 106

(MSW and others) will be sold to the registered

recycler.


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

(Details in Table Format)

Type of Solvent Details of Solvent

Recovery

% of Recovery Reuse of

Solvent

Toluene Distillation 99.97 Recycle in next

batch

Dichloroethane Distillation 99.80 Recycle in next

batch


� VOC will be observing due to the use of solvent. To minimize the VOC level below

the CPCB norms we will be taken action as follows.

� Pump and pipes will be provided for transferring of solvent.

� Raw materials will be kept in closed container.

� Regular monitoring of the storage container and transferring system.


Storage details Name of major Hazardous

chemicals

Remarks

Storage tanks

Alpha Piene,

Toluene

Ethylene Dichloride

� 24 tanks X 2000 liters



Drum/Barrel storage

Peracetic Acid,

Isopulegol,

Styrene Monomer,

Sulfuric Acid

HDPE container

� Applicability of PESO : Not Applicable


41


of 106

• Committee noted that this proposal is new in GIDC Sojitra. Source of Water is GIDC. PP mentioned

that condensate effluent will be generated from process which will be reused back in process and

cooling tower make up, while effluent generated from washing & cooling tower blow down will be

treated in proposed in-house primary ETP followed by steam jacketed evaporator. Unit will maintain

complete ZLD. PP has proposed one thermic fluid heater. Fuel used will be Natural Gas/Agro Waste.

PP has addressed Hazardous Waste as per HWR – 2016.

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

of Terms of Reference.

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

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

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

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

distance from the project boundary.

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

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

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

activities therein. The details of fund allocation and activities for CER shall be incorporated

in EIA/EMP report.

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

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

modes of alternative eco-friendly sources of energy like solar water heater, solar lighting

etc. Measures proposed for energy conservation.

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

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

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

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

during unloading, storage, transportation, handling and processing of Solvents.

5. Status of all the applicable Rules, Acts, Regulation, Clearances in a tabular form.

6. Technical Justification for no waste water generation from process and use of condensate

in process and cooling tower make up along with its treatability & feasibility.

• 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

42


of 106

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

• Further Project Proponent may be advised to submit final EIA Report with EC application within 100

days from the date of issuance of this ToR to expedite processing of Environment Clearance

application.

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

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

6 SIA/GJ/IND2/40919/2019 M/s. Perivinc Pharmaceuticals Pvt

Ltd.

Plot No.: 257, GIDC Estate, Hansalpur,

Viramgam, Dist.: Ahmedabad.

Screening &

Scoping







• This is an existing unit for chemical manufacturing and now proposes for expansion in manufacturing

of new synthetic organic chemicals as tabulated as below:

Sr.

No.

Name of the

Products CAS.NO

Existing Proposed Total after

Expansion Uses

MT/Month MT/Month MT/Month

1 Herbal Extract

(Vinea Alkaloids) - 0.5 -0.5 0.0 -

2 Trihexy Phenidyl-

HCl 52-49-3 0.0 0.70 0.70

Healthcare 3 Procyclidine-HCl 1508-76-5 0.0 0.40 0.40

4 Pantoprazole

Sodium 164579-32-2 0.0 2.8 2.8

5 Levosulpride 23672-07-3 0.0 1.834 1.834

43


of 106

6 Bromhexine-HCl 611-75-6 0.0 1.5 1.5

Total 0.5 7.234 7.234




Sr.

no.

Particulars Details


(Rs. in Crores):

Proposed: Approx Rs. 300 Lacs

B Total Plot area (sq. meter)

2248.5 Sq.m

Green belt area

( sq. meter)

744 Sq. m

C Employment generation

Proposed: 25 people

D Water

i



GIDC water supply

Status of permission from the concern authority. Required permission obtained

ii


Sr.

No.

Source

Water Consumption (KL/Day)

Existing

Quantity

Proposed

Quantity

Total

Quantity

1. Domestic 3 0 3

2. Gardening - 2.5 2.5

3. Industrial

A. Process 14.0 -13.4 0.6

44


of 106

B. Boiler 5.0 -3.0 2.0

C. Washing 3.0 -1.0 2.0

D. Cooling - +2.0 2.0

Total Industrial 22.0 -15.4 6.6

Total

(Domestic + Industrial) 25.0 -12.9 12.1

Total water requirement for the project: 12.1 KLD

Quantity to be recycled: 0 KLD

Total fresh water requirement: 12.1 KLD

iii


Sr.

No.

Source

Waste Water Generation (KL/Day)

Existing

Quantity

Proposed

Quantity

Total

Quantity

1. Domestic 2.5 0 2.5

2. Gardening - - -

3. Industrial

A. Process 3.0 -1.7 1.3

B. Boiler 0.5 -0.2 0.3

C. Washing 3.0 -1.0 2.0

D. Cooling - 0.3 0.3

Total Industrial 6.5 -2.6 3.9

Total

(Domestic + Industrial) 9.0 --2.6 6.4


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

ETP: 10 KLD, Stripper: 0.5 KL/hr


Domestic: Septic Tank/soak pit system

45


of 106

Industrial:

Treated effluent will be sent to Common Spray

Drying Facility developed by M/s. Chhatral

Environmental Management System Pvt. Ltd.

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

of CF

Unit has already obtained membership for disposal of treated effluent at Common Spray

Drying Facility developed by M/s. Chhatral Environmental Management System Pvt. Ltd.



Obtained


Fresh Water (12.1) (First Day)

Domestic

0.30

Septic Tank

2.0

Process

(0.6)

0.3

Washing(2

.0)

Boiler(2.0) Cooling

(2.0)

ETP (3.9)

Gardening Industrial (6.6)

Treated Effluent will be sent to Spraying Drying Facility Developed by M/s.

Chhatral Common Environment Management Facility

1.3

Stripper

46


of 106


Total reuse: 0 KLD of water

E Air



Sr

.

N

o.

Stack

Attached

to

Type of Fuel &

Rate of Consumption Stack

Heigh

t (m)

APC

M

Parameter &

Permissible

Limit

Existing Proposed

after

expansion

1

Steam

Boiler

(1 No.)

Wood –

200

Kg/day

Agro waste

Briquettes –

800 Kg/day

32 Bag

Filter

PM < 150

mg/Nm3

SO2< 100 ppm

NOx< 50 ppm

Proposed

Sr.

No

.

Stack

Attached to

Type of Fuel

&

Rate of

Consumption

Stack

Height

(m)

APCM

Parameter &

Permissible

Limit

2

D.G Set -

1 Cap.

250 KVA

HSD: 10

lit/hr 12

Acousti

c

Enclos

ure

PM < 150

mg/Nm3

SO2< 100

ppm

NOx< 50 ppm


Existing: There is no process emission from the production of existing product.

Proposed: For Fugitive emission

Sr.

No. Stack Attached to

Stack

Height

(m)

APCM Parameter &

Permissible Limit

47


of 106

1 Solvent Storage Area & Process

Area 8 meter

Packed

Carbon

Column

-


As below:

� Regular sprinkling of water is carried out & green belt is provided within premises to

prevent fugitive emissions due to vehicular movement. Regular maintenance of vehicles.

� Management to ensure proper handling of the spillages during transfer, charging operation

and provision of a Dust Collection System for collection of the air borne material wherever

applicable.

� Preventive maintenance of flange connections and glands of pumps.

� Management will also ensure proper usage of the Personnel Protective Equipment by the

workers.

� Closed handling system shall be provided for chemicals.

� Reflux condenser to be provided over the reactor.

� The raw materials shall be taken from storage tanks to reactor through closed pipeline.

Storage tanks shall be vented through trap receiver

� Fugitive emissions in the work zone environment, product raw material storage area will be

monitored regularly.

-

F Hazardous wastes

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

2016.

48


of 106

i Sr

.

No

.

Type of

Waste

Categ

ory

Existin

g

Quanti

ty

Propose

d

Quantity

Total after

expansio

n

Mode of Disposal

1. Used Oil 5.1 -- 0.5

MT/YEAR

0.5

MT/year

Collection, Storage ,

Transportation , Reuse and/or

Disposal by selling to Registered

Re-refiners

2.

Empty Barrels

Glass Bottle

Liners,

Containers

33.1

2.28

MT/YE

AR

3.72

MT/Year

6.0

MT/Year

Collection, Storage,

Decontamination, transportation,

disposal by selling to authorized

recycler.

3.

Process

Wastes,

Residues &

Wastes

21.1

29.5

MT/Ye

ar

-29.5

MT/Year Nil


Transportation, Disposal at

Registered TSDF or Disposal by

co-processing or Incineration

4. Spent Solvent 26.4

540

MT/Ye

ar

195.84

MT/Year

735.84

MT/Year

Collection and

Distillation in-house/recovery &

reused

5. Distillation

residue 26.3 --

6.0

MT/Year

6.0

MT/Year


Transportation, Disposal by co-

processing or Incineration

6.

Chemical

Sludge from

wastewater

treatment

35.3

9.36

MT/Ye

ar

-4.36

MT/Year

5.0

MT/ Year


transportation and disposal at

any registered TSDF site.


(For HW management)

Will be obtained before

going for production

iii Details of Non-Hazardous waste & its disposal

(MSW and others)

--


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

49


of 106

Name of

Product

Reacti

on

Stage

Name of

Solvent

Input Recovery

%

Recovery

Machiner

y End

Use Kg/

Mont

h

Kg/

Month Used

Trihexy

Phenidyl-HCl

I & II Methanol 2870 2660 92.68% Separate

distillation

Col. With

Reactor

Re

used

in

next

batch

II Toluene& THF 3500 1645 94.00%

Procyclidine-

HCL

I & II Methanol 2050 1900 92.68%

II Toluene& THF 2500 2350 94.00%

Pantoprazol

e Sodium

I Methanol 8800 8160 92.73%

II Acetone 9600 8920 92.92%

III Acetone 1120

0 10560 94.29%

Levosulpride I

Ethylene

Glycol 3850 3696 96.00%

Methanol 1155

0 10850 93.94%

Bromhexine-

HCL I Methanol 5400 5040 93.33%


� Breather valves will be provided on solvent tanks.

� To eliminate chances of leakages from glands of pumps, mechanical seal will be provided

at all solvent pumps.

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

pressure and temperature.

� Periodic monitoring of work area will be carried out to check the VOC emission.

Solvent recovery system will be provided with chilled water condenser system


• Committee noted that the name of the Project is “SELF REGISTRATION” and asked PP to clarify

about the same. PP mentioned that they have made an error while applying the application and they

will submit the required documents for the name change/correction of the same.

• Committee noted that this proposal is for expansion. Unit is located at GIDC, Hansalpur. Unit has

50


of 106

valid CC&A. Unit has submitted Compliance of CC&A. PP ensured that there is no court case and

public complaint against this unit. Source of water is GIDC. PP mentioned that they will surrender

existing products hence all the effluent coming out from existing plant will be NIL. PP mentioned that

effluent generated after expansion from process, washing, cooling tower blow down & boiler blow

down will be treated in in-house primary ETP and treated effluent will be sent to Common Spray

Drying Facility developed by M/s. Chhatral Environmental Management System Pvt. Ltd for final

treatment and disposal. Committee noted that PP has not satisfactorily addressed water balance

diagram and water consumption and generation table. PP has proposed one standby D.G. Sets. Fuel

used will be HSD. Committee noted that PP has not addressed process stack considering the mass

balance of product profile and have not incorporated any APCM for the same. Committee also noted

that PP has not addressed Bleed Liquor in Hazardous Waste which will be coming out of process

stack.

• After detailed discussion, it was decided to consider the proposal only after satisfactory

submission of the following details.

1. Revised Water Balance Diagram Considering Expansion scenario and addressing the Water

Consumption & Generation Table Considering the Same.

2. Addressing the Process Stack Considerig the Expansion in Product Profile along with its APCM.

3. Revised Hazardous Waste Matrix Considering Bleed Liquor from APCM of Process Stack and

Sound Management of the Same.

4. Authenticated Documents for change of name of Project from “Self Registration” to “Perivinc

Pharmaceuticals Pvt Ltd”.

7 SIA/GJ/IND2/40968/2019 M/s. Paras Pharma Chem

Plot No. C-235, GIDC Indu. Estate,

Saykha, Vagra, Bharuch.

Screening &

Scoping


Project status: New





51


of 106


Sr.

No

Product Name CAS No. Proposed

Quantity

(MT/Month)

End Use Of Product

1. 1,3 DICHLORO DIMETHYL

HYDANTOIN

112-36-7

750

Pharma & Water Treatment

2. 1,3 Dibromo-5,5- Dimethyl

Hydantion

77-48-5 Pharma Industries

3. 5,5 Dimethyl Hydantion 77-71-4 Pharma Industries

4. 2,2-Azobisisobutyronitrile 78-67-1 Pharma, Polymer,Paint And

Pesticides Industries

5. Benzoyl Peroxide 94-36-0 Paint & Polymer Industries

6. MEK Peroxide 1338-23-4 Paint & Polymer Industries

7. LABSA 27176-87-0 Use In Detergents Industries

8. Methyl Methacrylate (MMA) 80-62-6 Acrylic Resin, Paint & Plastic

Industries

9. Acrylic Emulsion 25067-01-0 Textile , Paper & Leather

Industries,

10. VAM Emulsion 108-05-4 Textile, Paint Industries

11. Sodium Hypochlorite 7681-52-9

350

Textile & Paper Bleaching

12 Calcium Chloride 7440-70-2 Paint & Dyes Industries

13 Benzalkonium Chloride (BKC-50) 8001-54-5 Clinical Products

14 Benzalkonium Chloride (BKC-80) 8001-54-5 Clinical Products

15 Amine Oxides 1643-20-5 Clinical Products

16 Pearl Essence 8039-79-0 Used in Paint and Plastic

Industries

17 Cobalt Octate 13586-82-8 Paint & FRP Plastic

Industries

18 TRO Turky Red Oil 8002-33-3 Antifoaming Agent & Textile

Industries

19 Coco Diethanolamide 68603-42-9 Cosmetic & Toiletries

20 Solvent Based Paints ---- Use in Wooden,Metal,

52


of 106

Household & Industrial Use

TOTAL: 1100




Sr.

no.

Particulars Details

A


(Rs. in Crores):

9.50 Crores

B Total Plot area ( sq. meter) 8304.338 Sq. m.

Green belt area ( sq. meter) 2689.11 Sq. m.

C Employment generation 80

D Water

i


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

GIDC Water Supply

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

permission letter from

GIDC.

Ref

No:GIDC/EE(W/D)/BRH/

585


Category

Quantity

KLD

Remarks

(D) Domestic 3.0

(E) Gardening 10.0

(F) Industrial

Process 37.0

Washing 30.0

Boiler 9.5

53


of 106

Cooling 8.5

Scrubber 2.0

Industrial Total 87.0

Total (A + B + C) 100.0

7) Total water requirement for the project: 100 KLD

8) Quantity to be recycled: 68 KLD

9) Total fresh water requirement: 32 KLD


Category Waste water

KLD

Remarks

(C) Domestic 2.0

(D) Industrial

Process 40.0 Stream-I: Low COD &

TDS: 69 KLD

Stream-II:Utilites: 2 KLD

Washing 29.0

Boiler 1.0

Cooling 1.0

Scrubber 2.795 Reuse and sell end users

having permission under

rule-9


water

73.795

Total [A + B + C] 75.795

-

Iv Treatment facility within premises with capacity


etc.

� ETP (Primary,Secondary& Tertiary): 69 KLD


Stream I (RAW EFFLUENT Stream) (69 KLD)

54


of 106

First all non-toxic and biodegradable (streams I) of wastewater shall pass through

Oil & Grease Removal Tank (OGRT-01) where floating O & G shall be removed

manual from top and collected in O & G Collection Tank (OGCT-01).

Then effluent shall be collected in Equalization cum Neutralization Tank (ENT-01)

where the continuous addition and stirring of Lime solution is done to maintain

neutral pH of wastewater from Lime Dosing Tanks (LDT-01-A/B) as per

requirement with help of Lime Dosing Pumps. Then after, neutralized wastewater

shall go to Flash Mixer (FM-01) by gravity. Alum shall be dosed from Alum Dosing

Tanks (ADT-01-A/B) with help of Dosing Pumps. Then after, coagulated

wastewater shall be settled in Primary Settling Tank-1 (PST-01).

Clear supernatant from PST-01 shall be passed in Aeration Tank (AT-01). Here,

biodegradation of organic matter of the wastewater shall be carried out by bacteria

(suspended growth) in the AT-01 and for that oxygen shall be supplied by 2 nos.

of air blowers (B-02) through diffusers. Air blowers also keep MLSS in

suspension.

Then after, wastewater shall go to Secondary Settling Tank (SST-01). Here, the

suspended solids shall be settled at bottom. Sludge shall be removed from bottom

of SST-01 and pumped to AT-1 to maintain MLSS and excess activated sludge

shall be sent to Sludge Sump (SS-01). Clear supernatant from SST-01 shall be

collected in Intermediate Sump (IS-01) by gravity.

Thereafter, the wastewater shall be passed through Pressure Sand Filter (PSF-

01) to remove left out TSS and Activated Carbon Filter (ACF-01) for final effluent

polishing. After tertiary treatment, effluent shall be collected in Treated Effluent

Sump (TES-01) before sent to RO-01 for further treatment. RO-01 permeate

water shall be collected in RO Treated Water Tank (ROTWT-01) before reuse in

plant. RO-01 reject shall be sent to Single Stage Evaporator (SSE-01).

Condensate water from SSE-01 shall be reuse/recycle in boiler or cooling for

future treatment.

Sludge settled in PST-01 and excess sludge from SST-01 shall be collected in

Sludge Sumps (SS-01) then sludge shall be pumped to Centrifuge (CF-01) where

55


of 106

poly shall be mixed from poly Dosing Tank-2 (PDT-02) with sludge to increase

efficiency of centrifuge sludge dewatering. Then, dewatered sludge shall be

stored in in HWSA and then ultimate disposal to TSDF. Leachate from CF-01 and

backwash from PSF-01 and ACF-01 shall be collected in Drain Pit and pumped

back to ENT-01 for further treatment.


Management of waste water keeping in view direction under section 18 (1)

(b) of the Water (Prevention and Control of Pollution) act, 1974 issued by

CPCB regarding compliance of CETP.

� Not Applicable


� Source of water will be met through Saykha GIDC Water Supply.Total water

requirement will be 100 KL/Day (Fresh Water: 32 KL/Day +RO Permeate: 60

KL/Day +Condensate Water:8 KL/Day).

� Total 75.795 KL/Day (73.795 KL/Day: Industrial + 2.0 KL/Day: Domestic) of

effluent shall be generated.

� Stream-I: 69 KL/day low COD & TDS stream (from process & Washing) will

be treated in ETP giving primary, secondary & Tertiary treatment then sent to

RO for further process.

� Stream-II: 2 KL/day utilities stream (from Boiler, cooling) will be send to RO.

Total 71 KL/day (from Boiler, cooling & Treated effluent from ETP ) will be

treated in RO & 60 KL/day RO permeate will be reused in Industrial Water

requirement & RO reject will be sent to Inhouse Single Stage Evaporator and

than pass through condense. Condensate water shall be reuse/recycle in

boiler or cooling.

� 2.795 KL/Day Scrubber wastewater Will be reused or sold to end users having

permission under Rule-9.

� 2 KL/Day Domestic waste water will be sent to Septic Tank & Soak Pit.


Domestic: Domestic waste water (2.0 KL/day) will be disposed by septic tank

or soak pit system

56


of 106

Industrial: � Stream-I: 69 KL/day low COD & TDS stream (from process

&Washing) will be treated in ETP giving primary, secondary &

Tertiary treatment then sent to RO for further process.

� Stream-II: 2 KL/day utilities stream (from Boiler, cooling) will

be send to RO.

Total 71 KL/day (from Boiler, cooling & Treated effluent from

ETP ) will be treated in RO & 60 KL/day RO permeate will be

reused in Industrial Water requirement & RO reject will be sent

to Inhouse Single Stage Evaporator and than pass through

condense. Condensate water shall be reuse/recycle in boiler or

cooling.

� 2.795 KL/Day Scrubber wastewater Will be reused or sold to end

users having permission under Rule-9.

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

etc. Name of CF

� Not Applicable, Unit has Zero Liquid Discharge.


57


of 106

Note:

When CETP, Saykha will be operational then after unit will discharge effluent to CETP,

Saykha for further treatment after primary, secondary & Tertiary treatment in ETP.


Total reuse: 34.0 KLD

Source of waste

water for reuse

with quantity in

Application

area with

quantity in

Characteristics of

waste water to be

reused (COD, BOD,

Remarks

regarding

feasibility

Raw Water: 100

Dom: 3.0

Process Boiler Cooling

Septic Tank & Soak

Pit: 2

Ind: 87 Gardening: 10

1 40 2.795

Washing

29

Other : 2

1

Will be reused or

sold to end users

having permission

under Rule-9.

RO Reject : 11

ETP (69)

(Primary, Secondary, Tertiary)

RO:71 RO Permeate :60

Reuse/recycle

Single Stage Evaporator

Condenser Condensate water: 8

Reuse/Recycle in

Salt to sludge drying

Steam: II 2

KLD Utilities

Steam-I 69 KLD Low

COD & TDS Steam

58


of 106

KLD (From

where it is

coming)

KLD (Where it

is used)

TDS etc.) to reuse i.e.

RO Permeate: 60

KLD

Condensate

Reuse Water:8

KLD

Industrial

Water: 60 KLD

Boiler &

Cooling:8 KLD

COD: 70 mg/l

BOD: 30 mg/l

TDS: 2000 mg/l

COD: 50 mg/l

BOD: 20 mg/l

TDS: 150 mg/l

E Air



KVA etc.

-

Sr.

no

.

Source

of

emissio

n

With

Capacity

Stack

Height

(meter

)

Type of

Fuel

Quantit

y of

Fuel

MT/Day

Type of

emission

s i.e. Air

Pollutant

s

Air Pollution

Control

Measures

(APCM)

1

Boiler

(Capacit

y: 500

KG/PH)

18 Briquette

s of Bio-

Coal/

Coal

1

MT/Day

/ 0.8

MT/Day

SPM

SO2

NOx

Multi-cyclone

Separator with

Bag Filter

2

Boiler

(Capacit

y: 1

TPH)

18 Briquette

s of Bio-

Coal/

Coal

5

MT/Day

/ 4

MT/Day

SPM

SO2

NOx

Multi-cyclone

separator with

bag filter

3 Thermic

fluid

18 Briquette

s of Bio-

4

MT/Day

SPM Multi-cyclone

separator with

59


of 106

heater

(Capacit

y: 1 Lakh

Kcal/ Hr)

Coal/

Coal

/ 3

MT/Day

SO2

NOx

bag filter

4

D. G. Set

(125

KVA)

11 HSD 300

Lit/Day

SPM

SO2

NOx

Adequate Stack

Height

5

D. G. Set

(125

KVA)

11 HSD 300

Lit/Day

SPM

SO2

NOx

Adequate Stack

Height

-

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

etc.)

-

Sr.

no.

Specific Source

of emission

(Name of the

Product &

Process)

Type of

emissio

n

Stack/Ven

t

Height

(meter)

Air Pollution Control

Measures

(APCM)

1

Process Vent

(Chlorination)

(Product Name:

AIBN, DDH,

DCDH)

Cl2

HCl

11 Two Stage Water +

Caustic Scrubber

2

Process Vent

(Sulphonation)

(Product Name:

MMA and LABSA)

SO2 11 Two Stage Caustic

scrubber

3 Process Vent

(Ammoniation)

NH3 11 Two Stage Acid scrubber

60


of 106

(Product Name:

DMH)

-


As below:

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

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

spraying water or providing enclosures.

2. Adequate ventilation will be provided.

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

be done to prevent leakages and thus minimizing the fugitive emissions.

4. Entire process will be carried out in the closed reactors with proper

maintenance of pressure and temperature.

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

emission.

6. Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be

equipped with on-line pH meter with hooter system for better operational

control.

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

tank vents will be connected to vent chillers.

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

9. Regular inspection of floating roof seals and proper preventive maintenance of

roofs and seals for tanks.

10. Fugitive emission over reactors, formulation areas, centrifuges, chemical

loading, transfer area will be collected through hoods and ducts by induced

draft and controlled by scrubber/ dust collector.

11. Dedicated scrubber will be provided are used for fugitive emissions to

control.

12. For dust emissions bag filter will be provided.

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

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

and control by scrubber / dust collector to be ensured.

F Hazardous wastes

61


of 106

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


i

Sr.

no

.

Type/Name of

Hazardous

waste

Specific

Source of

generation

(Name of

the Activity,

Product

etc.)

Categor

y &

Schedul

e as per

HW

Rules.

Quantit

y

(MT/

Annum)

Management of HW

1 Discarded

Drums/Bags

Raw

Material

and

Storage

Sch-I/

33.1

45 Collection, Storage,

Transportation and

sell to Register Re-

processors after

decontamination.

2 Used / Spent

Oil

Equipment

&

Machinery

Sch-I/

5.1

200 Lit/

Year


Transportation and

sell to registered

recycler.

3 ETP Sludge ETP Sch-I/

35.3


Transportation and

sent to common

TSDF of M/s. BEIL.

4 Distillation

Residue

Distillation Sch-I/

20.3

100.68 Collection, Storage,

Transportation and

sent for co-

processing in cement

industries or sent to

common incineration

of M/s. BEIL.

5 Spent Catalyst Process

(Product

Sch-I/

28.3


Transportation and

sent to registered

62


of 106

No:9,10) regenerator under

Rule-9 permission.

6 HCl (10%) Scrubber SCH-

1/26.1

263 Collection, Storage &

210 MT/Month (2520

MT/year)will be

reused within

premises in the

manufacturing of

Calcium Chloride.

7 NaOCl (12%) Scrubber SCH-

1/26.1

270 Collection, Storage &

convert to product

and than sell as main

product.

8 Sodium

Sulphite (25%)

Scrubber Sch-II/

B36

316.8


Transportation and

sold to end user

having permission

under rule-9.

9 Spent Sulphuric

Acid (50%)

Process

(Product

No:7,8)

Sch-I/

26.3

2529

10 Ammonium

sulphate (15%)

Scrubber

Sch-II/

B15

1350

11 Ammonium

bisulphate

(50%)

Process

(Product

No:8)

Sch-I/

26.3

1350

12 Spent Solvent Process

(Product

No;17)

Sch-I/

28.6

3045


Distillation and Reuse

within premises.

13

.

Off

Specification

Products

From mfg.

Process

(Batch

Sch-I/

28.4

20


Transportation and

sent for co-

processing in cement

63


of 106

failure) industries or Disposal

at common

incineration site.

14

.

Evaporator

Salt

Condeser SCH-

1/26.1


Transportation and

sent to common

TSDF of M/s. BEIL.

-


(For HW management)

Unit has membership of

CETP,Dahej.

Ref. No: BEIL/ANK/2019

dated13/09/2019


(MSW and others)

There will be no

generation of Non-

Hazardous waste.




Only one solvent is Used in process. Other Solvent is to be used as reactant.

Solvent

Boiling

Point

(0C)

Vapor

Pressure

Inpu

t

(MT/

mon

th)

Outpu

t

(MT/m

onth)

Loss %

Recovery

%

Loss

Toluene 110.6°C

3.8 kPa

(@

25°C)

420 400 39 95.25 1.85


During operation stage, leakage through valves/pumps, leakage and emission

from open drum containing chemicals, open feeding, storage tanks, etc. will be

major sources of fugitive emissions and VOCs. Excess use of solvent/s may also

results fugitive emission from the process vessels.

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

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


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

filtrate tank vents will be connected to vent chillers.

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

loading, transfer area, will be collected through hoods and ducts by

induced draft and controlled by scrubber/dust collector.

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

• Control by having proper scrubbing system.

• Condenser to trap VOC.

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

raw materials in particular solvents through hoods and ducts by induced

draft, and control by scrubber/dust collector to be ensured.

• Proper maintenance schedule will be adhered to avoid emissions through

flange joints, pump seals etc.

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

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

extent possible pumps with mechanical seal.

• All the raw materials will be pneumatically transfer to the reactor.

• All rotating equipments like pumps will be installed with mechanical seals

to arrest any sort of emissions.

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

rectify all gaskets and joints etc. as a part of ISO systems to ensure no

fugitive emissions take place.

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

emission.

• Solvent tank vents will be connected to vent chillers.

• Adequate ventilation will be provided.

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


• Breather valves will be provided on solvent tanks.


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Storage details Name of major Hazardous chemicals Remarks

Storage tanks

Acetone cynohydrin, Benzoyl

Chloride,Hydrochloric Acid,Sulphuric

Acid , Methanol or Toluene

Drum/Barrel storage

Liquid Ammonia, Hydrazine Hydrate,

Hydrogen peroxide, Dibuthyl Phthalate,

Acetone,IPA, Diethylamine, 2-

Ethylhexanoic acid

Cylinder,Bottle or

Tonner

Bromine and Chlorine

� Applicability of PESO : If Applicable, company will take permission.


• Committee noted that this proposal is new in GIDC Saykha. Source of Water is GIDC. Committee

noted that PP has addressed product profile considering end-use of some products in pesticides

industry and asked PP to clarify the same, PP mentioned that they will submit revised product profile

considering the same. PP mentioned that effluent generated from process, washing will be treated in

in-house ETP consisting of Primary, Secondary & Tertiary treatment followed by RO, while effluent

generated boiler blow down, cooling tower blow down will be directly treated in RO. PP mentioned that

RO – Permeate will be mixed with fresh water and reused/recycled back while RO – Reject will be fed

to Single Stage Evaporator, Condensate from Evaporator will be reused back in utility while

residue/salt will be disposed at approved TSDF.Committee noted that treatment characteristic

proposed by PP is not satisfactory. PP has proposed two Steam Boiler & one Thermic Fluid Heater.

Fuel used will be Briquette of Bio-Coal/Coal. PP has addressed Hazardous Waste as per HWR –

2016.

• After detailed discussion, it was decided to consider the proposal only after satisfactory

submission of the following documents:

1. Revised Product Profile eliminating the end-use of Products pertaining to Pesticides & Pesticides

Specific Intermediates (Address Water Balance Diagram, Consumption & Generation Details

along with Flue Gas Stack & Process Stack, Hazardous Waste Details).

2. Properly Addressing Characteristic of Waste Water Based on Treatment Technology with

Technical Justification for % Reduction of Load (pH, COD, BOD, SS).

3. Technical Justification for use of Single Stage Evaporator Instead of Multiple Effect Evaporator

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Considering the Product Profile and Characteristic of Waste Water to be generated.

8 SIA/GJ/IND2/38383/2019 M/s. Ketul Chem Pvt Ltd

Plot No. D2/CH/132, GIDC-Dahej-II,

Bharuch.

ToR –

Reconsideration


Project status: New






SR.N

O NAME OF PRODUCTS CAS NO.

Quantity

(MT/Month) END USE

Pharma Intermediate Group-1

1 1, 1-Cyclohexane diacetic

acid monomide 99189-60-3

70

Pharma Intermediate/Gabapentin

2 1,1- Cyclohexane diacetic

acid (Di-Acid) 11/7/4355 Pharma Intermediate/Gabapentin

3 2-Cyanoacetamide 107-91-5 Pharma Intermediate/pregablin

4 Ethyl cyanoacetate 105-56-6 Pharma Intermediate/pregablin

5 Methyl cyanoacetate 105-34-0 Pharma Intermediate/pregablin

6

± 3-(Carbamoyl methyl)-5-

methyl hexanoic acid

(CMMHA)

181289-15-6 Pharma Intermediate/pregablin

7

3R-(-)-3-(Carbamoyl

methyl)-5-methyl hexanoic

acid

181289-33-8 Pharma Intermediate/pregablin

8 2-Cyano pyrazine 19847-12-2 Pharma Intermediate/pyrazinamide

9 2-Cyano pyridine 100-70-9 Pharma Intermediate/bromazepine

10 4-Cyano pyridine 100-48-1 Pharma Intermediate/bromazepine

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of 106

11 Cyanoacetic acid 372-09-8 Pharma Intermediate/pregablin

Pharma Intermediate Group-2

12 4-hydroxy Acetophenone 99-93-4

75

Pharma Intermediate/atenolol

13 4-Hydroxy phenyl

acetamide 17194-82-0 Pharma Intermediate/atenolol

14 2-(4-Hydroxyethyl)phenol 56718-71-9 Pharma Intermediate/Metoprolol

15 2-{4-(2-Methoxy ethyl)

phenoxy} methyl oxirane 56718-70-8 Pharma Intermediate/Metoprolol

16 4-(2-Methoxy ethyl Phenol)

OR MEP 501-94-0 Pharma Intermediate/Metoprolol

17 2-Chloro ethanol 107-07-3 pharma intermediate/ thiodiglycol

18 4'-Methyl-2-cyanobiphenyl 114772-53-1 pharma intermediate/ losartan

19 4'-(bromomethyl)-[1,1'-

biphenyl]-2-carbonitrile 114772-54-2 Pharma Intermediate/losartan

20

4'-methyl-2-biphenyl

carboxylic acid methyl

ester

114772-34-8 pharma intermediate/ valsartan

21 2-(Thiophen-2yl) ethanol 5402-55-1 Pharma Intermediate/clopidogrel

22 4-Hydroxy benzaldehyde 123-08-0 pharma intermediate/ Pioglitazone

23 2,4-Dichloro-5-fluoro

acetophenone 704-10-9 Pharma Intermediate/ketaconazole

24 2',4'-dichloroacetophenone 2234-16-4 Pharma Intermediate/ketaconazole

25 Ethyl ethoxy methylene

malonate 87-13-8

Pharma

Intermediate/glibenclamide

26 N-Acetyl thiazolidine-4-

caboxylic acid 5025-82-1

Pharma Intermediate/ Folcisteine

27 Methyl Isobutyryl acetate 42558-54-3 Pharma Intermediate/ atorvastatin

28 D (-) P-Hydroxyphenyl

glycine methyl ester 57591-61-4 Pharma Intermediate/amoxicillin

29 5-Methyl-2-pyrazine

carboxylic acid 5521-55-1 Pharma Intermediate/glipizide

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30 Iminostilbene carbonyl

chloride 33948-22-0

Pharma

Intermediate/carbamazepine

31 10-Methoxy Iminostilbene 4698-11.7 Pharma

Intermediate/oxcarbamezepine

32 2-Chloro-4-(4-chloro

phenoxy) acetophenone. 119851-28-4

Pharma

Intermediate/difenoconazole

33 2-Amino-4-Hydroxy

Acetophenone 90033-64-0 Pharma Intermediate/ractopamine

34 2-Bromo-4’-hydroxy


35 2-Chloro-4’-hydroxy


Bulk Drugs Group-1

36 Pregabalin 148553-50-8

30

api/anti covulsant

37 Albendazole 54965-21-8 api/anti worm

38 Atenolol 29122-68-7 api/beta bocker

39 Atorvastatin Calcium 134523-00-5 api/cardiovascular

40 Carbamazepine 298-46-4 api/anti epileptic

41 Gabapentin 60142-96-3 api/anti covulsant

42 Ketoconazole 65277-42-1 api/anti fungal

43 Losartan potassium 124750-99-8 api/hypertension

44 Metoprolol Succinate 98418-47-4 api/hypertension

45 Metoprolol Tartrate 37350-58-6 api/hypertension

46 Oxcabazepine 28721-07-5 api/anti epileptic

47 Pantaprazol Sodium 138786-67-1 api/anti ulcer

48 Ractopamine hydrochloride 90274-24-1 api/beta agonist

49 Ritonavir 155213-67-5 api/antiretroviral

50 Rivaroxaban 366789-02-8 api/anticoagulant

51 Salmeterol xinafoate 94749-08-3 api/anti asthamatic

52 Saxagliptin Monohydrate 945667-22-1 api/anti diabetic

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53 Soterenol 13642-52-9 api/anti asthamatic

54 Sitagliptin 486460-32-6 api/anti diabetic

55 Valsartan 137862-53-4 api/hypertension

56 Glipizide 29094-61-9 api/anti diabetic

57 Rosuvastatin Calcium 147098-20-2 api/cardiovascular

58 Sofosbuvir 1190307-88-

0 api/anti viral

59 Telmisartan 144701-48-4 api/hypertension

60 Mirtazapine 61337-67-5 api/anti histamine

61 Nevirapine 129618-40-2 api/HIV/AIDS curing

62 Octopamine 104-14-3 api/veternary

63 Tranexamic acid IP 1197-18-8 api/antifibrinolytics

Specialty Chemicals

64 p-Chloro phenol 106-48-9

120

Raw material for

4,2(Methoxyethyl)phenol

65 o-Chloro phenol 95-57-8 Raw material for 2-

Chlorobenzaldehyde

66 2,6-Dichloro toluene 118-69-4 Raw material for 2 methyl 3

biphenyl methanol

67 Hydrazine hydrate 10217-52-4 Raw material for 1,2,4-Triazole

68 1,2,4-Triazole 288-88-0 Raw material for 1-Methyl-1,2,4-

Triazole

69 3-Cyano pyridine 100-54-9 Raw material for nictonic

acid/nictonamide

70 Phenyl Ethyl Alcohol (PEA) 60-12-8 Raw material for Phenyl Methyl

Alcohol

71 Phenyl ethyl methyl ether

(PEME) 3558-60-9

Raw material for Phenyl ethyl

methyl ether

72 Triclosan 3380 -34-5 Raw material for Irgasan

73 2–Amino–4, 4’ – Dichloro

Diphenyl Ether 121-27-7 Raw material for Yellow acid

74 2–Hydroxy–4, 4’–Dichloro 3380-44-7 Raw material for Tinosan

70


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Diphenyl Ether

75 Decabromo diphenyl oxide 1163-19-5 Raw material for Saytex

76 Alpha phenyl ethyl amine dl 618-36-0 Raw material for R+ 1

phenylethylamine

77 (R)-(+)-1-Phenylethylamine 3886-69-9 Raw material for R- carbommoyl

methyl 5 methyl hexanoic acid

78 (S)-(-)-1-Phenylethylamine 2627-86-3 Raw material for (S)-3-Cyano-5-

methylhexanoic acid

79 L-(+)-Mendelic acid 17199-29-0 Raw material for Dulexotine

Hydrochloride

80 Malononitrile 109-77-3 Rawmaterial for 2

chlorobenzaldehyde malononitrile

81 2,4-Difluoro aniline 367-25-9 Raw material for 2,4-difluoro-5-

chloronitrobenzene

82 2,2-Dibromo-2-

Cyanoacetamide 10222-01-2 Raw material for Bioban (dbnpa)

83 2-(4-tert-butyl)phenyl)

ethanol 5406-86-0

Raw material for 2-Benzoxazol-2-

yl-1-(4-tert-butylphenyl)ethanol

Total 295



• Technical presentation was made by the project proponent with consultant/expert Aqua Air

Environmental Engineers Pvt. Ltd during SEAC meeting dated 13/08/2019.

• Committee noted that this proposal is for new unit located at GIDC Dahej-II.

• Committee deliberated on size of group products in product profile and end use of each group

products are not adequate and hence committee insisted to PP for submit adequate revised product

profile proposal. Committee asked about compliance of Ozone Depleting Substances Rules for

proposed Page 82 of 82 539thmeeting of SEAC-Gujarat, Dated 13.08.2019 Page 82 of 82 product

namely 1,1,1,2-Tetrafluoroehtane etc. Committee asked for clarification regarding 2,4-Difluoro aniline ,

2,6-Dichloro toluene, 2,-3-Dichloro pyridine etc as pesticide inter mediate, PP could not explain

regarding it. Committee asked about waste water management, PP informed low COD effluent after

ETP treatment will be sent to CETP and high COD effluent after primary treatment will be sent to

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common MEE of M/s SEPPL, Dahej. Committee asked about readdressed worst case scenario as per

revised product profile for water consumption and waste water management.

• After deliberation, SEAC unanimously decided to defer the project and consider the proposal

after submission of the following details.

1. Revised product profile with respect to production capacity, size of group products and its end use

in agro chemicals.

2. Readdressed water consumption and waste water generation considering worst case scenario for

revised product profile.

3. Technical justification for compliance of ODS (Ozone Depleting Substances) Rules 2000 and its

amendments time to time for proposed product 1,1,1,2-Tetrafluoroehtane etc.

• Project proponent presented for the following points in SEAC meeting dated 19/09/2019 for the above

mentioned points.

• PP has replied as below:

1. PP presented revised product profile eliminating the production capacity, size of group products

and also eliminating the products pertaining to agro chemicals.

2. PP presented water consumption and waste water generation considering worst case scenario for

revised product profile.

3. PP mentioned that they have eliminated the products pertaining to ODS (Ozone Depleting

Substance) Rules, 2000.

• The case was reconsidered in the SEAC meeting dated 19/09/2019. During the said

meetingCommittee observed that reply submitted by PP is satisfactory.

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

Sr.

no.

Particulars Details

A


(Rs. in Crores):

22.0 Crores

B Total Plot area ( sq. meter) 13,923 Sq. m.

Green belt area ( sq. meter) 4,177 Sq. m.

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D Water

i



GIDC Water Supply

Status of permission from the concern authority. GIDC/DEE(WS)/BRH/235


Category

Quantity

KLD

Remarks

(G) Domestic 10.0

(H) Gardening 2.0

(I) Industrial

Process 136.4

Washing 20.0

Boiler 40.0

Cooling 10.0

Scrubber 4.0

Industrial Total 210.4

Total (A + B + C) 222.4

10) Total water requirement for the project:222.4 KLD

11) Quantity to be recycled: 9.6 KLD

12) Total fresh water requirement: 212.8 KLD


Category Waste Remarks

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water

KLD

(E) Domestic 8.0

(F) Industrial

Process 114.2 Low COD & TDS: 103.8 KLD (ETP-1)

High COD & TDS: 10.4 KLD (ETP-2)

Washing 20.0 Low COD & TDS: 20.0 KLD (ETP-1)

Boiler 10.0 RO: 12 KLD, RO Reject of 2.4 KLD will

be treated with ETP-1. Cooling 2.0

Scrubber 5.33 Reuse and sell under rule-9

permission


water

151.5

Total [A + B] 159.5

-



etc.

� ETP-1 (Primary, Secondary, Tertiary) : 126.2 KLD

� ETP-2 (Primary) : 10.4 KLD

� ETP-3 (RO) : 12.0 KLD


� Stream I (Low COD & TDS Stream) (123.8 KLD + 2.4 RO Reject)

� First all non-toxic and biodegradable streams (low & medium COD & TDS)

of wastewater shall pass through oil & grease removal tank (ogrt-01) where

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floating o & g shall be removed manual from top and collected in o & g

collection tank (ogct-01). Then effluent shall be collected in collection cum

equalization tanks-01 (cets-01). Pipe grid is provided at bottom of the cets-

01 to keep all suspended solids in suspension and to provide proper mixing.

2 nos. Of air blowers (1w+1 stand-by) shall supply air through to pipe grid.

� Then after, equalized wastewater shall be pumped to neutralization tank-1

(nt-01-b) where the continuous addition and stirring of lime solution is done

to maintain neutral ph of wastewater from lime dosing tanks (ldt-01-a/b) as

per requirement with help of lime dosing pumps. Then after, neutralized

wastewater shall go to flash mixer (fm-01) by gravity. Alum shall be dosed

from alum dosing tanks (adt-01-a/b) with help of dosing pumps. Then

coagulated effluent shall be collected in flocculator (fl-01) where

polyelectrolyte shall be dosed from polyelectrolyte dosing tank-1 (pedt-01)

with help of pumps to carry out flocculation with help of flocculator

mechanism. Then after, coagulated wastewater shall be settled in primary

clarifier-1 (pcl-01).

� Clear supernatant from pcl-01 shall be passed in aeration tank-1 (at-01).

Here, condensate from MEE and ATFT through condensate storage tank

(cst-01) mix with effluent. Here, biodegradation of organic matter of the

wastewater shall be carried out by bacteria (suspended growth) in the at-01

and for that oxygen shall be supplied by 2 nos. of air blowers (b-02) through

diffusers. Air blowers also keep MLSS in suspension.

� Then after, wastewater shall go to secondary clarifier-1 (scl-01). Here, the

suspended solids shall be settled. Sludge shall be removed from bottom of

scl-01 and pumped to at-1 to maintain MLSS and excess activated sludge

shall be sent to sludge sump (ss-01).

� Clear supernatant from scl-01 shall go to aeration tank-2 (at-02). Here

biodegradation of left out organic matter of the wastewater shall be carried

out by bacteria (suspended growth) and for that oxygen shall be supplied by

two nos. Of blowers (b-03) with help of diffusers. Then after, wastewater

shall go to secondary clarifier-2 (scl-02) from at-2. Here, the suspended

solids shall be settled. Activated sludge shall be removed from bottom of scl-

02 and pumped to at-02 to maintain MLSS and remaining will be sent to ss.

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Nutrients will be added from nutrient dosing tanks (ndts-01) to aeration tank-

1 & 2 for growth of bacteria. Clear shall be collected in intermediate sump

(is-01) by gravity.

� Thereafter, the wastewater shall be passed through multi grade filter (mgf-

01) to remove left out TSS and activated carbon filter (acf-01) for final

effluent polishing. After tertiary treatment, effluent shall be collected in

treated effluent sump-01 (tes-01) before sent to CETP Dahej for further

treatment.

� Sludge settled in pcl-01, pcl-02 and excess sludge from scl-01-b/02-b shall

be collected in sludge sumps (sss-01-a/b) then sludge shall be pumped to

centrifuge (cf-01) where poly shall be mixed from poly dosing tank-2 (pdt-02)

with sludge to increase efficiency of centrifuge sludge dewatering. Then,

dewatered sludge shall be stored in in HWSA and then ultimate disposal to

TSDF. Leachate from cfs-01 and backwash from mgf-01 and acf-01 shall be

collected in drain pit and pumped back to cet-01-a/b for further treatment.

� Stream II (High TDS stream) (10.4 KLD Process)

� All high TDS streams of wastewater shall be collected in equalization cum

neutralization tank-01 (ent-01). Here caustic shall be added from ldt-01 by

gravity. Mixer is provided at bottom of the ent-01 to keep all suspended

solids in suspension and for proper mixing.

� Then, neutralized wastewater shall be pump to flash mixer-02 (fm-02) where

alum and polyelectrolyte shall be dosed from alum dosing tank (adt-01) and

polyelectrolyte dosing tank (pedt-01) respectively by gravity. Then it will go

into pst-01 where solids are allowed to settle and clear supernatant from pst-

01 shall be collected in treated effluent sump (tes-01) before sent to

common MEE M/s. BEIL for further treatment.

� Stream-III (12 KL)

� All utilities streams of wastewater shall be passed through duel media filter

(dmf-01) to remove left out TSS. After treatment, effluent shall be collected

in RO feed tank (roft-01) before sent to RO-01 for further treatment. RO-01

permeate water shall be collected in RO permeate tank (ropt-01) before

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reuse in process & RO-01 reject shall be sent to ETP for further treatment.


Management of waste water keeping in view direction under section 18 (1)

(b) of the Water (Prevention and Control of Pollution) act, 1974 issued by

CPCB regarding compliance of CETP.

� Unit has proposed ETP to achieve CETP norms, and then after unit will

discharge the effluent to CETP, Dahej through Pipeline.


� Low COD & TDS effluent will be discharge into CETP, Dahej after treated

in Primary, Secondary and tertiary treatment. High COD & TDS effluent

will be treated in primary treatment and then sent to CMEE of BEIL, Dahej

and waste water from Cooling and boiler will be treated in RO and reuse

within premises.


Domestic: Septic tank/Soak Pit System

Industrial: Low COD & TDS: Effluent will be treated in Primary, Secondary and

tertiary treatment, after that sent to CETP, Dahej.

High COD & TDS: Effluent will be treated in in primary treatment

and then sent to CMEE of BEIL, Dahej.

Waste water from Cooling and boiler will be treated in RO and reuse

within premises.

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

etc. Name of CF

� CETP, Dahej, CMEE of BEIL,Dahej


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GIDC/BRH/DEE (DRG)/362



Total reuse: 9.6 KLD

Source of waste

water for reuse

with quantity in

KLD (From

where it is

coming)

Application

area with

quantity in

KLD (Where it

is used)

Characteristics of

waste water to be

reused (COD, BOD,

TDS etc.)

Remark

s

regardin

g

feasibilit

y to

reuse

i.e.

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RO Permeate: 9.6

KLD

Boiler: 9.6 KLD COD: 120 mg/l

BOD: 30 mg/l

TDS: 300 mg/l

E Air



KVA etc.

-

Sr.

no.

Source

of

emission

With

Capacity

Stack

Height

(meter)

Type of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

1 Boiler (4

TPH) 30 Coal 4

SPM <

150

mg/Nm3

SO2 < 100

ppm

NOx < 50

ppm

Multi

Cyclone

Separator

with Bag

Filter &

Water

Scrubber

4

D. G Set

(750

KVA)

11 HSD 2

SPM <

150

mg/Nm3

SO2 < 100

ppm

NOx < 50

ppm

Adequate

stack

Height

-

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

79


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etc.)

-

Sr.

no.

Specific Source

of emission

(Name of the

Product &

Process)

Type of

emission

Stack/Vent

Height

(meter)

Air Pollution

Control

Measures

(APCM)

1 Process Vent

(Ketoconazole) HCl 11

Two stage

Water

scrubber

2 Process Vent

(Valsartan) SO2 11

Two stage

Alkali

scrubber

3 Process Vent

(Ketoconazole) HBr 11

Two stage

Water

scrubber

4

Process Vent

(4-Hydroxy Phenyl

Acetamide)

NH3 11

Two stage

Water

scrubber

-


As below:

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

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

by spraying water or providing enclosures.

2. Adequate ventilation will be provided.

3. Regular maintenance of valves, pumps, flanges, joints and other

equipment will be done to prevent leakages and thus minimizing the

fugitive emissions.

4. Entire process will be carried out in the closed reactors with proper


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

emission.

6. Stand by pumps will be provided on all scrubbers. Besides, scrubbers

will be equipped with on-line pH meter with hooter system for better

operational control.

7. Close feeding system will be provided for centrifuges. Centrifuge and

filtrate tank vents will be connected to vent chillers.

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

9. Regular inspection of floating roof seals and proper preventive

maintenance of roofs and seals for tanks.

10. Fugitive emission over reactors, formulation areas, centrifuges, chemical

loading, transfer area will be collected through hoods and ducts by

induced draft and controlled by scrubber/ dust collector.

11. Dedicated scrubber will be provided are used for fugitive emissions to

control.

12. For dust emissions bag filter will be provided.

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

of raw materials in particular solvents through hoods and ducts by

induced draft, and control by scrubber / dust collector to be ensured.

F Hazardous wastes

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


i Sr.

No

.

Type Of Waste Source Of Generation Category Quantity

(MT/Annu

m)

Mode Of

Treatment

And Disposal

1 Spent carbon ± 3-(Carbamoyl

methyl)-5-methyl

hexanoic acid

(CMMHA),

4-Hydroxy phenyl

acetamide, Triclosan,

Schedule

-(I)-(28.3)

504 Collection,

Storage,

Transportation

and sent for

co-processing

in cement

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Sitagliptin, Nevirapine industries or

sent to

Incineration

site of M/s.

SEPPL.

2 Sulphuric Acid

(50-65%)

1,1- Cyclohexane

diacetic acid (Di-Acid),

2–Hydroxy–4, 4’–

Dichloro Diphenyl

Ether, Triclosan,

Schedule

-(I)-(28.1)

13,629 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

3 HCl (30%) 4-hydroxy

Acetophenone,

2,6-Dichloro toluene,

Saxagliptin

Monohydrate

& Scrubber

Schedule

-(I)-(28.1)

1,402 Collection,

Storage and

Reuse in 3R-(-

)-3-(Carbamoyl

methyl)-5-

methyl

hexanoic acid

(Reqd Qty.

5712

MT/Annum)

4 Dil. Formic Acid 1,2,4-Triazole Schedule

-(I)-(28.1)

2,706 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

5 NaCl Salt Cyanoacetic acid, 2–

Amino–4, 4’ –

Schedule

-(I)-(28.1)

1,872 Collection,

Storage,

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Dichloro Diphenyl

Ether, Malononitrile,

Pregabalin

Transportation

and sell to end

users Having

Rule-9

permission.

6 Discarded

Drums/Bags/Lin

ers

Raw Material and

Storage

Schedule

-(I)-(33.1)

1,500 Nos. Collection,

Storage,

Decontaminati

on, Reuse,

Transportation

and sale to

authorized

vendor.

7 Spent Catalyst 4-(2-Methoxy ethyl

Phenol) OR MEP,

Phenyl Ethyl Alcohol

(PEA), Ritonavir

Schedule

-(I)-(28.2)

72 Collection,

Storage,

Transportation

and Sell to

Regenerator

Having Rule-9

permission.

8 Organic Waste Saxagliptin

Monohydrate,

Rosuvastatin Calcium

Schedule

-(I)-(28.1)

1,020 Collection,

Storage,

Transportation

and sent for

co-processing

in cement

industries or

sent to

common

incineration

site of M/s.

83


of 106

SEPPL.

9 Iron Sludge 2–Amino–4, 4’ –

Dichloro Diphenyl

Ether

Schedule

-(I)-(28.1)

756 Collection,

Storage,

Transportation

and Disposal to

co-processing

in cement

industries or

sent to TSDF

site.

10 Inorganic Waste 2',4'-

dichloroacetophenon

e, Soterenol,

Triclosan,

Octopamine

Schedule

-(I)-(28.1)

3,372 Collection,

Storage,

Transportation

and Disposal to

co-processing

in cement

industries or

sent to TSDF

site.

11 Spent Solvent Manufacturing

Process

Schedule

-(I)-(28.6)

31,500 Collection,

Storage and

reuse within

premises after

distillation.

12 Distillation

Residue

Distillation plant Schedule

-(I)-(20.3)

948 Collection,

Storage,

Transportation

and sent for

co-processing

in cement

industries or

sent to

84


of 106

common

incineration

siteof M/s.

SEPPL.

13 Off Specification

Products

Failure of Batch Schedule

-(I)-(28.4)

24 Collection,

Storage,

Transportation

and sent for

co-processing

in cement

industries or

sent to

common

incineration

siteof M/s.

SEPPL.

14 Used Oil From Moving

Machineries

Schedule

-(I)-(5.1)

12 Collection,

Storage,

Transportation,

Reuse and

sale to

authorized

recycles.

15 Sodium Acetate

(25%)

Atorvastatin Calcium Schedule

-(I)-(28.1)

18 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

16 Sodium Sulphate

(95%)

Ritonavir Schedule

-(I)-(28.1)

45 Collection,

Storage,

Transportation

85


of 106

and Sell to end

users Having

Rule-9

permission.

17 Sodium Bromide

(95%)

2,2-Dibromo-2-

Cyanoacetamide,

Telmisartan

Schedule

-(I)-(28.1)

144 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

18 Sodium Bisulfite

(30-40%)

Triclosan Schedule

-(I)-(28.1)

726 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

19 KCl (50%) Sofosbuvir Schedule

-(I)-(28.1)

492 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

20 Ammonium

Chloride (10-

15%)

Sofosbuvir Schedule

-(I)-(28.1)

15 Collection,

Storage and

Reuse in

Sofosbuvir

(Reqd Qty.

14.4

MT/Annum)

excess qty will

86


of 106

be sold to end

users having

rule-9

permission.

21 Magnesium

Sulphate Salt

1,2,4-Triazole &

Scrubber

Schedule

-(I)-(28.1)

144 Collection,

Storage and

Reuse in

Sofosbuvir

(Reqd Qty.

144

MT/Annum)

22 Liq. Ammonia

(20-25%)

1,2,4-Triazole &

Scrubber

Schedule

-(I)-(28.1)

1,836 Collection,

Storage and

Reuse in

Hydrazine

Hydrate (Reqd

Qty. 3000

MT/Annum)

23 Potassium

Acetate (50%)

Telmisartan Schedule

-(I)-(28.1)

72 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

24 HBr (30-35%) 2-Amino-5-nitro

thiazole

Schedule

-(I)-(28.1)

84 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

25 Sodium Sulphite Scrubber Schedule 504 Collection,

87


of 106

(28%) -(II)-B36 Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

26 Dil. Hydrogen

Bromide (25%)

Scrubber Schedule

-(II)-B36

480 Collection,

Storage,

Transportation

and Sell to end

users Having

Rule-9

permission.

27 ETP Sludge ETP Treatment Schedule

-(I)-(35.3)

1,680 Collection,

Storage,

Transportation

and Disposal to

co-processing

in cement

industries or

sent to TSDF

site of M/s.

SEPPL.


(For HW management)

Proponent has applied for

membership


(MSW and others)

There will be no

generation of Non-

Hazardous waste.




88


of 106

Solvent

Boiling

Point

(0C)

Vapor

Pressur

e

Input

(MT)

Output

(MT) Loss

%

Recovery

%

Loss

EDC 83.47

100 mm

Hg @

300C

513 492 21 95.91 4.09

MDC 39.6

400 mm

Hg @

24.10C

389 379 10 97.43 2.57

Toluene 111

22 mm

Hg @

200C

654 629 25 96.18 3.82

Methanol 64.7

96 mm

Hg @

200C

803 765 38 95.27 4.73

Phenol 181.7

0.4 mm

Hg @

200C

615 597 18 97.07 2.93

IPA 82.2

82.2 mm

Hg @

200C

356 346 10 97.19 2.81

Xylene 139.3

8.3 mm

Hg @

200C

543 528 15 97.24 2.76

Ethyl

Acetate 96.5

10 mm

Hg @

200C

750 732 18 97.60 2.40

Acetone 76.4

11.1 mm

Hg @

200C

687 663 24 96.51 3.49

DMF 153 3.7 mm 369 353 16 95.66 4.34

89


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Hg @

250C


During operation stage, leakage through valves/pumps, leakage and emission

from open drum containing chemicals, open feeding, storage tanks, etc. will be

major sources of fugitive emissions and VOCs. Excess use of solvent/s may also

results fugitive emission from the process vessels.

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

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


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

tank vents will be connected to vent chillers.

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

loading, transfer area, will be collected through hoods and ducts by induced

draft and controlled by scrubber/dust collector.

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

• Control by having proper scrubbing system.

• Condenser to trap VOC.

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

raw materials in particular solvents through hoods and ducts by induced

draft,

and control by scrubber/dust collector to be ensured.

• Proper maintenance schedule will be adhered to avoid emissions through

flange joints, pump seals etc.

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

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

extent possible pumps with mechanical seal.

• All the raw materials will be pneumatically transfer to the reactor.

• All rotating equipments like pumps will be installed with mechanical seals to

90


of 106

arrest any sort of emissions.

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

rectify all gaskets and joints etc. as a part of ISO systems to ensure no

fugitive

emissions take place.

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

emission.

• Solvent tank vents will be connected to vent chillers.

• Adequate ventilation will be provided.

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


• Breather valves will be provided on solvent tanks.


Storage details Name of major

Hazardous chemicals

Remarks

Storage tanks

HCl, H2SO4, Methanol,

Toluene, Ethylene Oxide,

Chloroform, Liq. Ammonia

Drum/Barrel storage Ammonium Chloride,

Chloro Acetyl Chloride,

Phenol, Methyl

Cynoacetate,

Cylinder Chlorine, Hydrogen,

Nitrogen

� Applicability of PESO : Yes Applicable





91


of 106








in EIA/EMP report.












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




application.



9 SIA/GJ/IND2/37751/2019 M/s. Valencia Life Sciences

Plot No.1108 ,GIDC. Bamanbore ,

Chotila, Dist.: Surendranager.

ToR –

Reconsideration


Project status: New

92


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Sr

No

Name of Product Production

MT/M

CAS No End use of Product

1 1,3-Dichloroacetone 10 534-07-6 Famotidine &Nizatidine

2 2-Amino-5-Methyl

Thiazole

5 7305-71-7 Meloxicam & Piroxicam

3 4-Bromomethyl-2-

cyanobiphenyl

10 114772-54-2 Irbesartan, Losartan,

Valsartan, Azilsartan &

Telmisartan

4 4-Hydroxy, 2-Methyl-

2H, 1,2-Benzothiazine

Carboxylic Acid

Isopropyl Ester, 1,1-

Dioxide


5 4-Hydroxy, 2-Methyl-

2H, 1,2-Benzothiazine

3-Carboxylic Acid

Methyl Ester, 1,1-

Dioxide


6 Benzocaine 10 94-09-7 Local anaesthetic

7 Cetylpyridinium

Chloride

5 3473-63-0 Cetrimide

8 Cis Bromo Benzoate 13 61397-56-6 Ketoconazole

9 Cis Tosylate 10 154003-23-3 Ketoconazole & Itraconazole

10 Febuxostat 2 144060-53-7 Xanthine Oxidase Inhibitor

11 Fexofenadine

Hydrochloride

1 83799-24-0 Antihistamine

93


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12 Fluconazole 5 86386-73-4 Antifungals

13 Lidocaine Hydrochloride 10 137-58-6 Local anaesthetic; Class I

antiarrhythmic

14 Lidocaine 5 6108-05-0 Local anaesthetic; Class I

antiarrhythmic

15 Meta Bromo Anisole 10 2398-37-0 Tramadol HCl

16 Meta Bromo Nitro

Benzene

13 585-79-5 Meta Bromo Anisole

17 Meta Chloro Anisole 5 2845-89-8 Tramadol HCl

18 n-Butyl Bromide 10 106‐65‐9 Alkylating agent

19 Tetra Butyl Ammonium

Bromide

10 1643-19-2 Phase transfer catalyst

20 Tri Ethyl Benzyl

Ammonium Bromide

5 554-68-7 Phase transfer catalyst

21 Pregabalin 2 148553-50-8 Anticonvulsant

Total Production 151

By-Product

1 Basic Chromium

Sulphate

64.609 39380-78-4

Lather industry



• Technical presentation was made by the project proponent with consultant/expert T R Associates

during SEAC meeting dated 24/07/2019.

• Committee noted that this proposal is for new unit located at GIDC.

• Committee deliberated on location of the proposed project, product profile, waste water & Hazardous

waste management etc.

• While discussing regarding waste water management, PP informed that they will maintain zero liquid

discharge (ZLD). However, consultant as well as PP could not satisfactorily reply about treatability and

adequacy of ZLD.

• After deliberation, SEAC unanimously decided to consider the proposal after submission of

94


of 106

the following details.

1. Technical justification for Basic Chromium Sulphate as By-Product.

2. Treatability and adequacy of ZLD considering worst case scenario based on mass balance.

• Project proponent presented for the following points in SEAC meeting dated 19/09/2019 for the above

mentioned points.

• PP has replied as below:

1. PP presented technical justification for basic chromium sulphate and addressed the same in

hazardous waste as per hazardous waste rule.

2. PP presented treatability and adequacy of ZLD considering worst case scenario based on mass

balance.

• The case was reconsidered in the SEAC meeting dated 19/09/2019. During the said

meetingCommittee observed that reply submitted by PP is satisfactory.

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

Sr.

no.

Particulars Details

A Total cost of Proposed Project (Rs. in Crores) 2.50 Cr

B Total Plot area ( sq. meter) Plot Area :4617Sq.m

Green belt area,/Tree Plantation area ( sq. meter) 1391 Sq.m within premise.


D Water

i


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

Status of permission from the concern authority. Not applicable.


Sr No Description Water Consumption KL/Day

A Domestic 1.5

B Industrial

a. Process (including Scrubber) 17.528

B DM plant( for backwash) 4.382

b. Boiler 1.50

c. Cooling 2.00

95


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d. Washing 2.00

Total B 27.410

C Gardening 3.00

Total (A+B+C) 31.91

D RO permeate 23.95

Ultimate fresh water required(C-

D) 7.76

Source of fresh Water : GIDC water Supply

Quantity to be recycle : 23.95 KL/Day(RO permeate)

Total Fresh water requirement : 31.91KL/Day -23.95 KL/Day= 7.76 KL/Day


CATEGORY WISE WASTEWATERGENERATION

Description Waste Water

Generation KL/Day

Mode of Disposal

A Domestic 1.30 Soak Pit

B Industrial

a. Process 22.703 MEE

B DM plant( from backwash) 4.382 ETP & RO

b. Boiler 0.200 ETP & RO

c. Cooling 0.250 ETP & RO

d. Washing 2.000 ETP & RO

Total (B) 29.535

C RO permeate reuse in process,

Washing, and Cooling

23.95 Reuse

Domestic waste water will be disposed in to Soak Pit. Treated waste water will be evaporated in

MEE to maintain Zero Discharge.


In-house ETP (Primary, Secondary,RO Plant, MEE).

• Domestic waste water will be discharged in to soak pit.

• Industrial wastewater will be segregated in two stream i.e dilute stream and

concentrated stream which will be collect separately in collection cum neutralization

tank.

96


of 106

• Concentrated stream will be passed through VOC stripper to remove VOC content from

w.w, Generated stream from VOC stripper will be evaporated in MEE. Generated

Condensate equalised with dilute stream. After pH correction, wastewater will be given

polyelectrolyte treatment. Then wastewater will be collet in settling tank. Bottom Sludge

will be collected will be stored in bags and ultimately disposed of at TSDF site. Treated

waste water from settling tank and will be treat in aeration tank and then clarifier. Then

after , it will be passed through RO. Permeate of RO will be reuse in washing activity.

RO Reject water will be send to MEE .Evaporation residue from evaporator will be send

to ETP sludge. Condensate of MEE will be send to ETP for treatment. Thus, unit will

maintain Zero Effluent Discharge.

Treatment plant units

ETP unit Cap Nos

Collection cum neutralization Tank for dilute

Stream

5 KL 1

VOC stripper - 1

Filter Nutch 1

Collection tank for concentrated stream 30 KL 2

Equalization tank 30 KL 2

Coagulation Tank 10 KL 1

Sedimentation Tank 20 KL 1

Aeration Tank 45 KL 1

Clarifier 30KL 1

RO Plant 3.00 KL/Hr 1

MEE 3.00 KL/Hr 1

VOC Stripper 1

Treatment Scheme including segregation at source

• Domestic waste water will be disposed in to Soak Pit.

• Generated industrial waste water will be treat in P+S treatment plant and pass through

RO. Permeate of RO will be reuse in process. RO reject will be evaporated in MEE

within premises.

Note (in case of CETP discharge )

Management of waste water keeping in view direction under section 18 (1) (b) of the Water

97


of 106

(Prevention and Control of Pollution) act, 1974 issued by CPCB regarding compliance of CETP.

Not applicable as there is no CETP in Bamanbore industrial estate. Unit will maintain Zero

Discharge.


Domestic: Go to soak pit via septic tank

Industrial:

Treated waste water will be evaporated in MEE within premises to maintain

Zero Discharge.

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

of CF : Not applicable as unit will maintain Zero Discharge

Membership of Common facility (CF).

(For waste water Treatment )

Unit will maintain Zero Discharge

vii Simplified water balance diagram with reuse/Recycle details (KLD)

Water Consumption: Industry will need 31.91 KL/Day (Domestic: 1.5 KL/Day, Industrial: 27.410

KL/Day and Gardening 3.00 KL/Day) water for the proposed production which will be met by

water supply from GIDC Service.

Waste Water Generation: Domestic waste water (1.30 KL/Day) will be discharged in to soak pit.

21.910

4.382

17.528 0.2 0.25 2

Soak Pit (1.3)

6.832

Attach to Recovery System 22.703

Loss 21.95 4.835

4.78 23.95

Permeate Reuse

0.7 T MEE Sludge to TSDF

Water Balance Diagram

Domestic (1.5) RO Followed by

DM Plant Boiler(1.5) Cooling (2) Washing(2)

Gardaning

(3)

Process(17.528)

P+S+T (28.790)

RO Plant

MEE (22.603+4.835=

27.438)

VOC sripper

First Day : Fresh Water(31.910)

From Second Day : 31.910-23.95=7.96 KL/Day

98


of 106

The industrial waste water generation will be 29.535 KL/Day (Process-22.703 +Reject Water

4.382 + 0.005+Cooling blow down-0.250 + boiler blow down-0.200 +washing-2.00).

Mode of Disposal : Treatment and evaporation ( i.e ZLD)

viii Reuse/Recycle details (KLD) Source of reuse & application:

Source of waste

water for reuse with

quantity in KLD

(From where it is

coming)

Application

area with

quantity in

KLD

(Where it is

used)

Characteristics of

waste water to be

reused (COD, BOD,

TDS etc.)

Remarks

regarding

feasibility to reuse

i.e.

RO permeate Process pH : 6.5-7.5

TSS <120 mg/Lit

TDS<300 mg/Lit

COD <150 mg/Lit

RO permeate

suitable for use in

process and

washing activity

E Air


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

SR.N

O.

STACK

ATTAC

HED TO

STAC

K

HEIGH

T (M)

FUEL

REQUIRE

MENT

Quantit

y of

Fuel

MT/Day

EXPECTED

POLLUTAN

T

APC

SYSTEM

1

Steam

Boiler

(1 TPH)

30

White

Coal

/Briquette

600

Kg/Day SPM ≤150

mg/Nm3

SO2 ≤100

ppm

NOX ≤ 50

ppm

Dust

collector

followed by

Bag Filter

2 D.G. set

(65 HP) 6.5 Diesel

40 L/Hr Inbuilt

Acoustic

enclosure


SR. STACK STACK APC EXPECTED CONCENTRA

Gardening

(2)

Gardening

(2)

99


of 106

NO ATTACHED TO HEIGHT

(M)

SYSTEM POLLUTANT TION

1

Reactor of CIS

Bromo Benzoate,

Meta Bromo Nitro

Benzene

12

Two stage

alkali

scrubber

Bromine <2 mg/NM3

2 Reactor of

Pregabaline 12

Water

scrubber Ammonia <150 mg/NM3

3

Reactor of

Fexofenadine

Hydrochloride

and Fluconazole

12 Water

Scrubber

Hydro Chloric

Acid <20 mg/NM3

4 Solvent Recovery

system 12

Activated

Carbon

column

VOC BDL


As below:

Sources of fugitive emissions include storage of chemicals, 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.

F Hazardous waste

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

2016.

100


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i

Sr

No

Name of

Hazardous

Waste

Categ

ory

T/Year Source Mode of disposal

1

Aluminum

Chloride

C2 of

Sch-II

60.5

T/Year

Manufacturing process

of Fexofenadine

Hydrochloride and

Fluconazole

Collection ,Storage

,transportation and

Partially (15.06

T/Year reuse)

remaining will be sold

out of actual end

users

2

Distillation

Residue 28.1

261.24

T/Year


of

• 2-Amino-5-Methyl

Thiazole

• 4-Bromomethyl-2-

cyanobiphenyl

• 4-Hydroxy, 2-

Methyl-2H, 1,2-

Benzothiazine

Carboxylic Acid

Isopropyl Ester,

1,1-Dioxide

• 4-Hydroxy, 2-

Methyl-2H, 1,2-

Benzothiazine 3

Carboxylic Acid

Methyl Ester, 1,1-

Dioxide

• Benzocaine

• Cetylpyridinium

Chloride

• Cis Bromo

Collection ,Storage

,transportation and

send to CHWIF for

incineration

101


of 106

Benzoate

• Cis Tosylate

• Febuxostat

• Fexofenadine

Hydrochloride

• Fluconazole

• Lidocaine

Hydrochloride

• Lidocaine

• Meta Bromo

Anisole

• Meta Chloro

Anisole

• n-Butyl Bromide

• Pregabalin

3

Inorganic

Solid waste

28.1 5.16

T/Year


of Fexofenadine

Hydrochloride

4

Spent

Carbon

28.3 36

T/Year


of

• Benzocaine

• Cetylpyridinium

Chloride

• Febuxostat

• Fexofenadine

Hydrochloride

• Fluconazole

• Lidocaine

Hydrochloride

• Lidocaine

Collection ,Storage

,transportation and

send to CHWIF for

incineration

5

Spent HBr D2 of

Sch-II

324,532

T/Year


of

Collection ,Storage

,transportation and

102


of 106

• 4-Bromomethyl-2-

cyanobiphenyl

• Cis Bromo

Benzoate

• Meta Bromo Nitro

Benzene

sale to actual end

user having

permission under

Rule-9

6

Spent

Hydrochloric

Acid

D2 of

Sch-II

424.332

T/Year


of

• 1,3-Dichloroacetone

• Cis Bromo Benzoate

• Fexofenadine

Hydrochloride

Collection ,Storage

,transportation and

sale to actual end

user having

permission under

Rule-9

7

Spent

Sulphuric

Acid

D2 of

Sch-II

7912.96

T/Year


of Meta Bromo Nitro

Benzene

And n-Butyl Bromide

Collection ,Storage

,transportation and

sale to actual end

user having

permission under

Rule-9

9

ETP Waste 35.3 360

T/Year

Effluent treatment

plant

Collection ,Storage

,transportation and

send to TSDF for safe

dispsposal

10

MEE Salt 35.3 218.400

T/Year

Multi Effect evaporator Collection ,Storage

,transportation and

send to TSDF for safe

disposal

11

Discarded

Containers 33.1

1.00

T/Year

Raw Material Collection ,Storage

,transportation and

sale to authorized

recycler

12

Used Oil 5.1 0.2

KL/Year

Production machinery Collection ,Storage

,transportation and

sale to authorized

103


of 106

rerefiner recycler

13 Off

Specificatio

n

28.4 2 T/Year

Process Collection ,Storage

,transportation and

send to CHWIF for

incineration

14

Date Expiry

Products 28.5 2 T/Year

Process Collection ,Storage

,transportation and

send to CHWIF for

incineration

15

Basic

Chromium

Sulphate

A4 LE

II

775.308

T/Year


of 1,3-Dichloroacetone

Collection ,Storage

,transportation and

sale to actual end

users having

permission under

rule-9

ii Membership details of TSDF, CHWIF etc. Will become a member of

SEPPL,Kutch after getting TOR.


(MSW and others) -


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

Name of Solvent used in

process Recovered Loss Total

%

Loss

Acetone 26.509 0.657 27.166 2

Acetonitrile 6.24 0.21 6.45 3

Benzene 5.195 0.105 5.3 2

Chloroform 18.24 0.96 19.2 5

Dichloromethane 84.683 4.083 88.766 5

Diethyl Amine 27.467 1.171 28.638 4

Dimethyl Formamide 3.569 0.095 3.664 3

Ethyl Acetate 26.318 0.81 27.128 3

104


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imidazole 11.481 0.597 12.078 5

Isopropyl Alcohol 34.568 0.643 35.211 2

MDC 142.252 3.056 145.308 2

Methanol 110.683 3.657 114.34 3

Methyl Isobutyl Ketone 4.87 0.1 4.97 2

n-Hexane 4.144 0.216 4.36 5

Toluene 119.878 2.543 122.421 2


The unit will provide solvent recovery system/distillation for the recovery of solvent. The

solvent will be recovered and reused back in manufacturing process. The solvent will be

recovered through distillation process. The distillation is a process where because of

difference in boiling point solvent will be recovered.












in EIA/EMP report.









105


of 106




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




application.



Following proposal for which additional details sought in previous SEAC meeting was reviewed

and found that reply is still awaiting from the project proponent even after considerable time has

been lapsed.

Committee unanimously decided to delist the following proposals from the pending application

list of SEAC. It was decided to reopen the file upon submission of additional detail by the Project

Proponent.

1 SIA/GJ/IND2/35239/2019 M/s. Dharti Industries

Plot No.57/1,Sr.No.453, Katosan road,

Detroj, Dist -Ahmedabad

Screening and scoping

2 SIA/GJ/IND2/34081/2010 M/s. Gulshan Polyols Ltd.

Plot No.762, 762/1, 762/2, 762/3, 769/1 &

769/2, GIDC-Jhagadia, Bharuch.

Appraisal

3 Offline Application (B2

Category)

M/s. Mirash industries pvt. Ltd. (UNIT-I)

PLOT NO. D2/14, GIDC Dahej-II, Ta:-

Vagra, Dist:-Bharuch

Screening & Scoping

106


of 106

Meeting ended with thanks to the Chair.

Minutes approved by:

1. Dr. Dinesh Misra, Chairman, SEAC

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

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

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

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