seiaa.gujarat.gov.in Minutes of the 112VCth...Page 1 of 232 112th meeting of SEAC-Gujarat, Dated...

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112th meeting of SEAC-Gujarat, Dated 17.12.2020

Page 1 of 232

Minutes of the 112th meeting of the State Level Expert Appraisal Committee held on 17th

December 2020 through Video Conference (VC) on National Informatics Centre (NIC).

In the wake of recent crisis of COVID-19, lockdown situation, the agenda of the present meeting

was mailed to expert Committee in advance and a Video conference meeting on NIC was

organised in this regard on 17/12/2020 at 13.30 hrs.

The 112th meeting of the State Level Expert Appraisal Committee (SEAC) was held online by

Video conferencing on 17th December 2020 at 13.30 hrs. Following members joined the meeting:

1. Shri Akshay Kumar Saxena, Chairman, SEAC

2. Dr. S. C. Pant, Vice Chairman, SEAC

3. Dr. M. N. Patel, Member, SEAC

4. Shri D. C. Chaudhari, Member, SEAC

5. Shri J. K. Vyas, Member, SEAC

6. Shri Anand Zinzala, Member, SEAC

7. Shri B. M. Tailor, Member, SEAC

8. Shri A. V. Shah, Secretary, SEAC

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, EMP reports

etc.

1. SIA/GJ/IND2/173344/2020 M/s Hitesh corporation

Plot No. 6504,Near Hoeschst Chowkadi,

GIDC Estate Ankleshwar, Dist-Bharuch

Appraisal

Category of the unit: 5(f)

Project status: New

Project proponent (PP) submitted online application vide no. SIA/GJ/IND2/173344/2020 on dated

05.10.2020 for obtaining Environmental Clearance.

Project proponent has submitted Form – 1, Pre-Feasibility Report & Environment Management Plan as

per Notification issued by MoEF&CC vide S.O. 1223(E) dated 27th March, 2020 regarding consideration

of proposals or activities in respect of Active Pharmaceuticals Ingredients (API) as B2 category.

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This is a new unit proposes for manufacturing of synthetic organic chemicals [API and API Intermediates]

as tabulated below,

Sr

.

N

o.

Products API OR

INTERMEDIATE CAS No.

Qty.

(MT/

Mont

h)

End Use

1 BetaMethasone Sodium

Phosphate API 151-73-5

20

Corticosteroid

2 BetaMethasone Valerate API 2240-28-0 Medication-

Corticosteroid

3 BetaMethasone Dipropionate API 5593-20-4 Corticosteroids

4 DexaMethasone Sodium

Phosphate API 2392-39-4 Anti-inflammatory

5 Clobetasol Propionate API 25122-46-

7

Medicine -

corticosteroid to treat

skin conditions such

as eczema, contact

dermatitis, seborrheic

dermatitis, and

psoriasis.

6 Progesterone API 57-83-0

Treating abnormal

uterine bleeding

associated with

hormonal imbalance.

7 Progesterone Acetate API 302-23-8

Tablets are indicated

to treat secondary

amenorrhea, reduce

the incidence of

endometrial

hyperplasia in

postmenopausal

women, and to treat

abnormal uterine

bleeding due to

hormonal imbalance,

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not organic

pathology.

8 Mifepristone API 84371-65-

3 Abortion

9 Pyridoxine HCl API 58-56-0

It is used to prevent

or treat low levels of

vitamin B6 in people

who do not get

enough of the vitamin

from their diets.

10 Nandrolone Decanoate Ip. BP. API 360-70-3

Anemia, chronic renal

failure, osteoporosis

and AIDS.

11 In-house R & D ----- ----- 0.1 ----

TOTAL 20.1

ENDUSE OF PRODUCTS

Sr.

No.

Name of

the

Product

CAS No.

(Product)

Type/

Category of

Product

(API/

Intermediate)

In case of Intermediate stage of

API

Said API is

used for/End

Use of said API

Stage of

Intermediat

e

n-1, n-2,

etc

Name of API

in which

Intermediate

Used/ End

use of said

Intermediate

CA

S

No

.

(A

PI)

1 Beta

Methas

one

Sodium

Phosph

ate

151-73-5 API --- --- ---

Corticosteroid

2. BetaMet 2240-28- API --- --- --- Medication-

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hasone

Valerate

0 Corticosteroid

3. BetaMet

hasone

Dipropio

nate

5593-20-

4

API --- --- ---

Corticosteroid

s

4. DexaMe

thasone

Sodium

Phosph

ate

2392-39-

4

API --- --- ---

Anti-

inflammatory

5. Clobeta

sol

Propion

ate

25122-

46-7

API --- --- --- Medicine -

corticosteroid

to treat skin

conditions

such as

eczema,

contact

dermatitis,

seborrheic

dermatitis, and

psoriasis.

6. Progest

erone

57-83-0 API --- --- --- Treating

abnormal

uterine

bleeding

associated

with hormonal

imbalance.

7. Progest

erone

Acetate

302-23-8 API --- --- --- Tablets are

indicated to

treat

secondary

amenorrhea,

reduce the

incidence of

endometrial

hyperplasia in

postmenopaus

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al women, and

to treat

abnormal

uterine

bleeding due

to hormonal

imbalance, not

organic

pathology.

8. Mifepris

tone

84371-

65-3

API --- --- --- Abortion

9. Pyridoxi

ne HCl

58-56-0 API --- --- --- It is used to

prevent or

treat low levels

of vitamin B6

in people who

do not get

enough of the

vitamin from

their diets.

10

.

Nandrol

one

Decano

ate Ip.

BP.

360-70-3 API --- --- --- Anemia,

chronic renal

failure,

osteoporosis

and AIDS.

The project falls under Category B2 of project activity 5(f) as per the schedule of EIA Notification 2006

and amendment dated 27th March, 2020.

The proposal was considered in the SEAC video conference meeting dated 17.12.2020

Salient features of the project including Water, Air and Hazardous waste management as below,

Sr.

no.

Particulars Details

A

A-1 Total cost of Proposed Project

(Rs. in Crores):

3.4 Crores

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Break-up of proposed project Cost:

Details Project Cost

(Rs. In Crores)

Land 1.0

Building 0.7

Machinery 0.8

Environment

Protection and

Safety

0.87

A-2 Details of Environmental Management Plan (EMP) As below:

Component Capital Cost of EMP Recurring Cost of EMP

(per Month)

Cost 87 Lakh 8 Lakh

Sr.N

o.

Unit

Detail

Capital Cost

[Rs. in

Crore]

Operating

Cost [Rs.

in Crore]

Maintenan

ce Cost

[Rs. in

Crore]

Total

Recurring

Cost (Rs.

In Crore)

1 Waste Water 8 KLD 0.10 0.06 0.0020 0.06

2 Air - 0.15 0.0034 0.003

3

Hazardous

Management -

0.13 0.01 0.01

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4 Fire & Safety - 0.15 0.0008 0.001

5 AWH Monitoring - 0.02 0.0007 0.001

6

Green Belt

Development 40 %

0.04 0.0002 0.0002

7

Occupational

Health -

0.06 0.0050 0.0050

8 CER Activity 4% of total

Cost 0.136 0.0000 0.00000

9 PLC System - 0.08 0.0002 0.0002

Total 0.87 0.07 0.012 0.085

Summary

Cost of Project in Crores per

Annum:

3.4 Crore

EMP Capital Cost in Crores per

Annum and Percentage:

0.87 Crore[25%]

EMP Recurring Cost in Crores

per Annum and Percentage:

1.0 Crore

A-3 Details of CER as per OM dated 01/05/2018 (In case of project falls under CPA/SPA, CER

fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA

and 2 times for CPA in case of Environmental Clearance as per the mechanism published

vide MoEF&CC‘s OM vide 31.10.2019.)

% as per the OM Rs. in Crores

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4% 0.136 Cr

Brief note on proposed activities:

Unit has planned 4% of the total cost of the proposed project (3.4 Cr.) So unit use

13.6 Lakhs in CER Activities.

CER Budget : 13.6 lakh (for Three Years 2021-2023)

Activity Amount

We will provide required instruments in Civil hospital for

medical treatment and improve facilities in Civil hospitals.

Hospital Bed,Instruments,Laboratory

13.6 Lakh

B Land / Plot ownership details:

B-1 Plot area

Total Plot area

1888 Sq. m.

B-2 Brief note on Area adequacy in line to proposed project activities:

➢ Land Area Break-ups

Sr. No. Land Use

Proposed

Area

(Sq. MT)

% First Floor Second

Floor

1 Production plants 160 8.5 160 160

2 Administration 24.91 1.3 24.91

3 OHC 28.62 1.5

4 Lab 25.59 1.4

5 ETP 73.8 3.9

6 Utilities 30 1.6

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7 Raw Material Storage 90 4.8

8 Finished Product Storage 50 2.6

9

Hazardous Waste

Storage Area 81 4.3

10 Solvent Storage Area 72 3.8

11 Under Ground Tank Area 24.38 1.3

12 Green Belt 755 40.0

13 Road & Security cabin 472.7 25.0

Total 1888 100

As per calculation Unit will manufacture capacity of 20.1 MT/Month. So, Adequate Area will

be available to manufacture the proposed product. Production plant area will be 160 Sq. m.

B-3 Green belt area

Total (Sq. meter)

Area in Sq. meter 755

% of total area 40 %

C Employment generation

Total

10 Nos.

D Water

D-1 Source of Water Supply

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

Status of permission from the concern authority.

➢ we are attached here Annexure.[No.:NTA/ANK/DEE(WS)/1286

D-2 Water consumption (KLD)

Category

Quantity

KLD

Remarks

(A) Domestic 1.0

(B) Gardening 1.0

(C) Industrial

Process 3.2

Washing 1.0

Boiler 3.0

Cooling 2.0

Others 0.3+0.02 Scrubber & R&D

Industrial Total 9.52

Grand Total (A+B+C) 11.52

Brief Note on worst case scenario for water consumption:

➢

Product Water consumption Wastewater

Generation

Betamethason

e Dipropionate

3.2 KLD 3.9 KLD

Summary of Quantity KLD Remarks

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water

requirement

Total water

requirement for

the project (A)

11.52

Quantity to be

recycled (B)

1.5

Total fresh

water

requirement (C)

10.02

Ensure Total water requirement = Fresh water +

Recycled water i.e. A = B + C

Reuse/Recycle details (KLD) with feasibility. [Source of reuse

& application area]

Source

of waste

water for

reuse in

KLD

(From

where it

is

coming)

Application

area with

quantity in

KLD (Where

it is used)

Characteristi

cs of waste

water to be

reused

(COD, BOD,

TDS etc.)

Remarks

regarding

feasibility to

reuse

Boiler

Condens

ate

1.5 KLD

Cooling &

Washing

[1.0KLD+1.5

KLD]

PH:6.5-8.0

COD:100-

200 mg/L

TDS:400-

500 mg/L

In case of no reuse/recycle of waste water, Give brief note on

justification as why no reuse/recycle.

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➢ Not Applicable

D-3 Waste water generation (KLD)

Category Waste water KLD Remarks

(A) Domestic 0.5

(B) Industrial

Process 3.9

Washing 1.0

Boiler 0.5

Cooling 0.5

Others 0.31+0.02 Scrubber & R&D

Total Industrial waste

water

6.23

Total [A + B] 6.73

-

Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative):

QUALITATIVE AND QUANTITATIVE ANALYSIS OF EACH WASTE STREAM :-

Sr.

No.

Source of

WasteWater

Generation

Quantity in

KL/Day

Parameter

Quality Final load

at ETP in

Kg/day

1 Boiler 0.5 pH 6.5-8.0 --

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blowdown

COD 200-300 mg/L 0.15

TDS 600-700 mg/L 0.35

2 Cooling Tower

blow down

0.5 pH 6.0-8.5 --

COD 400-500 mg/L 0.2

TDS 700-800 mg/L 0.4

3 Washing 1.0 pH 5.0-6.5 ---

BOD 200-400 mg/L 0.4

COD 600-700 mg/L 0.7

TDS 800-1000 mg/L 1.0

4 Process 3.9 pH 3.0-6.5 ---

BOD 6000-8000 mg/L 31.2

COD 20000-25000 mg/L 97.5

TDS 30000-35000 mg/L 136.5

Total Industrial

Effluent

5.9

CHARACTERISTICS OF WASTEWATER BEFORE & AFTER TREATMENT

(ETP-P+CMEE-BEIL)

Sr.

No. Parameter Unit Before

Treatment

After Primary Treatment

1. pH -- 3.0-6.5 5.0-8.0

2. BOD mg/L 5,000-6,000 4,000-5,000

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3. COD mg/L 15,000-20,000 12,000-17,000

4. TDS mg/L 20,000-25,000 23,000-28,000

Brief justification in case of no process effluent generation or no industrial effluent generation or no

high concentration effluent generation from proposed project (If any applicable to proposal).

-Not Applicable

D-4 Mode of Disposal & Final meeting point

-

Domestic: ● Domestic wastewater will be sent to the primary ETP.

Industrial: ● Industrial waste water will be collected and treated into the primary ETP treatment plant and treated effluent will be sent to BEIL-CMEE for further treatment and disposal.

● Scrubbing water will go along with the product which will be sold to authorized end users registered under rule-9.

-

Clearly mention about final disposal

D-5 Treatment facilities

For Domestic wastewater:

Capacity of STP: Not Applicable [0.5 KLD will be sent to the primary ETP.]

For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary,

Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation

at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream

segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.

For Proposed, Industrial waste water will be collected and treated into the primary ETP treatment

plant and treated effluent will be send to BEIL-CMEE for further treatment and disposal.

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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 [CMEE-BEIL,Ankleshwar]

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

➢ Applicable

➢ For Proposed new project, Industrial waste water will be collected and treated into the

primary ETP treatment plant and treated effluent will be sent to BEIL-CMEE for further

treatment and disposal.

D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF

etc. Name of Common facility (CF) (For wastewater treatment)

➢ CMEE-BEIL,Ankleshwar

Membership of Common facility (CF) mentioning total capacity, consented quantity,

occupied capacity and spare capacity and norms of acceptance of effluent from member

units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706

dated 08/01/2020.

➢ We are attached here as Annexure.[Ref.BEIL/ANK/2020].

D-7 Simplified water balance diagram with reuse / recycle of waste water

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E Air

E-1 Brief Note on fuel based heat energy requirement and worst case scenario thereof:

Considering the Calorific Value of the fuel and other parameters, requirement of the heat,

we will use consumption of fuel in MT/Day

E-2 Flue gas emission details

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

(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism

published in the MOEFCC‘s OM vide dated 31.10.2019)

-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)

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1 Boiler

[1 TPH]

20 m Natural

Gas

1900

Nm3/Day

PM

SO2

NOx

Adequate

Stack

Height

2

Thermic

Fluid

Heater

[Cap. 2

Lac

K.cal/Hr]

20 m Natural

Gas

800

Nm3/Day

PM

SO2

NOx

Adequate

Stack

Height

3 D.G. Set

[250 KVA]

12 m Diesel 500

litre/day

PM

SO2

NOx

Adequate

Stack

Height

-

E-3 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

emission

Stack/Vent

Height

(meter)

Air Pollution

Control

Measures

(APCM)

1 Reaction Vessel

[Product Sr. No.-1,4]

HCl 15 Two Stage

Water Scrubber

Note:

⮚ Details of gaseous raw materials used in proposed project

⮚ Estimation of process gas emission (Product wise and Total)

⮚ Requirement of the scrubbing media (KL per Day) considering solubility (Product

wise and Total)

⮚ Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and

its sound management in HW matrix.

Details of scrubbing media are attached as Annexure-I.

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iii Fugitive emission details with its mitigation measures:

As below:

➢ Minimum Joints & flanges

➢ Pumps with mechanical seals

➢ Proper ventilation

➢ Adequate PPEs

F Hazardous wastes

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

Rules 2016.

Note:

⮚ Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle

within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.

⮚ Quantification of hazardous waste shall be based on mass balance and calculations

shall be incorporated in EMP details separately.

⮚ Disposal to scrap vendors/vendors/traders is not allowed

Note:- Details are attached as Annexure-I.

F-1 Hazardous waste management matrix

Sr.

no.

Type/Name of

Hazardous

waste

Specific

Source of

generation

(Name of

the Activity,

Product etc.)

Category

and

Schedule as

per HW

Rules.

Quantity

(MT/Annum

)

Management of HW

1. Empty barrels/

containers/line

rs

contaminated

with

hazardous

chemicals

Raw Material

and

Packaging

33.1 40 Collection, Storage,

Transportation, reuse or

send back to supplier or

sold to Authorized

Vendors.

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/wastes

2. Used Oil From

Machinery

5.1 1 Collection,

Storage,Transportation

and sold to authorized

Recyclers.

3. ETP Sludge ETP 35.3 45 Collection, Storage,

Transportation and sent

to TSDF site- BEIL

Ankleshwar.

4. Distillation

Residue

From

solvent

Distillation


Transportation, Co-

Processing or sent to

CHWIF.

5. Spent Carbon From

Process

Sr.

No.5,9,10


Transportation and

send to Co-Processing

or CHWIF.

6. Spent Catalyst From

Process

Sr. No.2,3,5


Recycle / Regeneration

/ Reuse and/or sent to

CHIWF.

7. Hyflo From

Process Sr.

No.5


Transportation,

CoProcessing or

disposal at CHWIF.

8. Salt

[Lithium Salt

of Methane

Sulphonic

Acid]

From

Process

Sr. No.5


Transportation and sent

to TSDF site

9. HCl Solution

[Hydrochloric

Acid Solution

Scrubber

Sr.

No.1,4,5,10

--- 115 Collection, Storage,

Transportation and sell

to authorized end users

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28%-30%] registered under rule-9.

10. Spent Solvent From

Solvent

Distillation


Recovery and recycle in

process or send

regenerator end user or

sell to authorized end

users registered under

rule-9.

11. Off-

Specification

Products

From

Process


Transportation,

CoProcessing or

disposal at CHWIF.

-

F-2 Membership details of TSDF, CHWIF etc.

(For HW management)

Details of Membership letter no. & Date with spare capacity of the Common Facility.

➢ Membership Certificate No.BEIL/ANK/2020, Dated 03 October 2020.

F-3 Details of Non-Hazardous waste & its disposal

(MSW and others)

Not Applicable

Not Applicable

Sr. no. Type/Name of Other

wastes

Specific Source

of generation

(Name of the

Activity, Product

etc.)

Quantity

(MT/Annum)

Management of

Wastes

1 -------------------------

G Solvent management, VOC emissions etc.

G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered

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Solvents etc.

Sr. No. Product

Name Solvent Name

Solvent

Consumption

[MT/Month]

Solvent

Recover Qty

[MT/Month]

% Rec.

1 BMSP Tetrahydrofuran

(THF) 4.8 4.6 95

Methanol 8.0 7.6 95

Isopropyl Alcohol 4.0 3.8 95

2 BMV MDC 20.0 19.2 96

Acetone 16.0 15.2 95

Methanol 12.0 11.4 95

3 BMD MDC 12.0 11.6 97

Acetone 16.0 15.2 95

Methanol 8.0 7.6 95

4 DMSP TetraHydrofuran

[THF] 4.0 3.8 96

Methanol 4.0 3.8 96

IPA 10.0 9.6 96

5 CP MDC 8.0 7.8 98

Acetone 12.0 11.5 96

Methanol 5.2 5.0 96

6 PS Pyrrolidine 4.8 4.6 96

Methanol 8.0 7.6 95

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Toluene 12.0 11.5 96

7 PSA Acetic Acid 8.0 7.6 95

Vinyl Alcohol 5.2 5.0 96

Chloroform 7.2 6.8 95

8 MP Acetic Acid 20.0 19.0 95

MDC 10.0 9.6 96

9 PDH Methanol 8.0 7.7 96

10 ND Acetone 30.0 28.4 95

n-Pentane 10.0 9.6 96

Pyridine 20.0 19.0 95

A highly efficient and full fledge solvent recovery system is installed to recover maximum possible

solvent and will be reused back in process. Detailed process is as described below:

For the efficient solvent recovery system, chilled water circulation jacketed, chilled water traps will be

installed on the vent for arresting any escape of vapors from the reaction and distillation unit. The

reactors will be connected to water condenser system. The receiver will also be jacketed with

circulation of water. The recovered solvents will then be stored and reused. Proper planning and

maintenance will enable to have an efficient solvent recovery from the system.

The recovery efficiency of every solvent used is approximately 95% - 98%.

● The solvent distillation system shall be designed so as to achieve minimum 95.0 % recovery of solvent.

● Two condensers will install with cooling water and chilled brine to recover the solvent. ● Primary Condenser HE-01: Cooling Tower water or Chilled water (at 10 0C) will be used to

condense the solvents depend on the vapor pressure at its operating conditions and the non-condensed vapours will be condensed in a Secondary Condenser.

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● VOC Trap Condenser HE-02: Chilled Brine at -5 0C will be used to trap any traces of Solvent which is slipped from Secondary condenser

G-2 Brief Note on LDAR proposed:

Leak Detection and Repair (LDAR) for Solvent:

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To prevent losses of these solvents in atmosphere, following infrastructure shall be used in addition

to LDAR program

● Leak Free Pumps & Valve for transfer of solvents

● MSW Gaskets in solvent pipelines to prevent leakage from flanges

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

● To eliminate chances of leakages from glands of pumps, double mechanical seal will be

provided at all solvent pumps.

● All the rotating equipment like pumps will be installed with double Mechanical Seals to arrest

any sort of emissions.

● Condenser post Reactor with cooling arrangement and chilling Arrangement. Flanges will be

sealed so less losses will be there.

● Down the Temperature of Chilling tower to -15°C.

● Closed loop system.

G-3 VOC emission sources and its mitigation measures

● Minimum joints/flanges ● Adequate Condenser ● Brine will be utilised as chilling agent ● Pumps with double mechanical seals ● Proper Ventilation ● PPEs

H SAFETY details

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H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent

acid and spent solvent tanks)

Sr. no Name of

Chemical

Capacity of

Tank

Number of

Tanks

Hazardous Characteristics of

Chemical

1 ------- ------- ------- -------

Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags

etc.

➢ Hazardous chemicals bags/drums are stored and handled in Dispensing room for taking out

samples from the container for quality check up purposes or for the partial use. This activity

for Hazardous material handling is carried out by using all PPE with proper ventilation &

under supervision.

➢ Drum handling trolleys is used for transportation of drums up to plant

➢ Materials are transferred by pumping through pipelines or by vacuum from drums.

Safety details of Hazardous Chemicals:

Type of Hazardous

Chemicals

Safety measures

Toluene It is important to keep toluene away from sources of heat or

ignition. This chemical should be stored in a tightly closed

container in a dry, well-ventilated, and secure place, preferably

one designed for the storage of flammable liquids. Toluene should

be kept away from incompatible materials, like oxidizing agents.

Methanol Methanol is a colourless liquid that boils at 64.96 °C (148.93 °F)

and solidifies at −93.9 °C (−137 °F). It forms explosive mixtures

with air and burns with a nonluminous flame. It is completely

miscible in water.

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Do not handle or open near flame, sources of heat, or sources of

ignition. Wear personal protective equipment. Use only in well-

ventilated areas. Provide sufficient air exchange and/or exhaust in

work rooms. Avoid contact with skin, eyes and clothing. Do not

breathe vapors or spray mist. Do not ingest. When using, do not

smoke. To avoid ignition of vapors by static electricity discharge,

all metal parts of the equipment must be grounded. Keep away

from incompatible materials. Handle in accordance with good

industrial hygiene and safety practice. Wash thoroughly after

handling. Containers of this material may be hazardous when

empty since they retain product residues (vapors, liquids).

HCl Wear a chemical-resistant apron, chemical-resistant gloves and

chemical splash goggles at all times when handling HCl to protect

your eyes and skin. Concentrated Hydrochloric acid is toxic if

inhaled, so avoid breathing it in and always handle it while under a

fume hood.

⮚ Applicability of PESO :Not Applicable

H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process,

Nitration process, Chlorination process, Exothermic Reaction etc.)

-

Type of Process Safety measures including Automation

----- ------

● There is no hydrogenation process, Nitration process, Chlorination process, Exothermic

Reaction etc. during our production.

H-3 Details of Fire Load Calculation

Total Plot Area: 1888 Sq. m.

Area utilized for plant activity: 160 Sq. m.(per Floor, total Floors :G+2)

Area utilized for Hazardous Chemicals 90 Sq. m.

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Page 27 of 232

Storage: Number of Floors:

Water requirement for firefighting in

KLD :

5 KLD

Water storage tank provided for

firefighting in KLD:

150 KLD

Details of Hydrant Pumps: 3 Nos.

[1]Main Fire Pump

[2]Diesel Driven Pump

[3]Jockey Pump

Frequency 50/60Hz

Voltage 380 VAC

Phase 3 Phase

Medium

Temperature

-15 deg C to 120 deg C

Max. Working

Pressure

2.5 Mpa

Ambient

Temperature

Less than 40 deg C

Nearest Fire Station : DPMC Fire Station Ankleshwar

Plot No. G/S-3, Near Jayaben Modi Hospital,

GIDC, Ankleshwar, Gujarat 393002

Applicability of Off Site Emergency

Plan:

Not Applicable

-

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Page 28 of 232

H-4 Details of Fire NOC/Certificate:

We will obtain it soon.

H-5 Details of Occupational Health Centre (OHC):

Number of permanent Employee : 10

Number of Contractual

person/Labour :

10

Area provided for OHC: 28.62 Sq. m.

Number of First Aid Boxes : 10 Nos.

Nearest General Hospital : Jayaben Modi Hospital

624/1, Valia Road, Ankleshwar

GIDC, Gujarat 393002

Name of Antidotes to be store in

plant :

Paracetamol

During the meeting dated 17.12.2020, the project was appraised based on the information furnished in

Form – 1, Pre-Feasibility Report, Environment Management Plan and details submitted by e-mail.

Project proponent (PP) and Technical expert of PP, M/s. Vasundhara Enterprise remains present during

video conference meeting.

Committee noted that the proposal is for Greenfield project in GIDC Ankleshwar. PP submitted details

regarding area adequacy. Source of water is GIDC. Product profile along with end use discussed in

depth. Looking to layout plan, Committee insisted for submit revised layout plan with mentioning

adequate raw material and solvent storage area and its area adequacy with land breakup which is later

on submitted by PP.

Committee noted that PP has submitted waste water management and total industrial effluent will be

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treated in ETP and treated effluent will be sent to CMEE of M/s. BEIL for evaporation. Domestic sewage

will be treated in ETP. Committee discussed regarding stage wise reduction of BOD, COD and TDS in

ETP.

PP submitted that they have proposed boiler and DG set. Fuel used will be Natural gas for boiler and

thermo pack. Two stage scrubbers will be provided as APCM with process reactor stack. Committee

insisted for revised fuel consumption of natural gas as per capacity of boiler for which PP is agreed upon

and later on submitted revised fuel consumption details. PP submitted Hazardous Waste Matrix as per

Hazardous Waste Rules – 2016.

Upon asking regarding provision of fire hydrant network and proposed fire extinguishers details, PP has

addressed the Site Plan/layout plan with provision of fire hydrant network, periphery road with entry and

exit separately, proposed fire extinguishers details, adequate fire water reservoir and fire load

calculation. Committee noted that PP has addressed fire evacuation plan, worker‘s safety and

occupational Health centre (OHC) and process hazard and its safety control measures. Committee

insisted for 150 KL fire water tank and fire trolley pump which details submitted later on by PP.

Committee deliberated on storage and safety aspects of hazardous chemicals, green belt area, EMP,

CER, LDAR and solvent recovery etc. Looking to green belt area mentioned only 36%, Committee

insisted for submit proposal of green belt area as per CEPI mechanism and PP later on submitted

revised green belt area of 40%.

Committee found submission of project proponent satisfactory.

After detailed discussion, Committee unanimously decided to recommend the project to SEIAA,

Gujarat for grant of Environment Clearance

SPECIFIC CONDITIONS:

1. Project Proponent (PP) shall strictly abide by the outcome/decision of Hon‘ble Supreme Court of

India in Civil Appeal no. 8478/2020 regarding operation of the Hon‘ble NGT orders dated 10/07/2019

& 14/11/2019.

2. PP shall comply conditions of any subsequent amendment or expansion or change in product mix,

after the 30th March 2021, considered as per the provisions in force at that time as mentioned in the

Notification vide S.O. 1223 (E) dated 27/03/2020 and S.O. 3636 (E) dated 15/10/2020.

3. PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients (API) as

per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any subsequent

amendments.

4. PP shall submit six monthly compliance report of Environmental Clearance without fail and the same

shall be critically assessed by the regulatory authority.

5. Wastewater shall be sent to CMEE only after providing adequate treatment in such a way that no

pollutant get air borne during evaporation to avoid adverse impact on Human Health & Environment.

6. The PP shall develop green belt within premises (755 Sq. m i.e. 40 % of the total plot area) as per

the undertaking submitted before SEAC. Green belt shall be developed with native plant species that

are significant and used for the pollution abatement as per the CPCB guidelines. It shall be

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implemented within 3 years of operation phase in consultation with GPCB.

7. Domestic wastewater generation shall not exceed 0.3 KL/day for proposed project and it shall be

treated in ETP. It shall not be disposed off in soak pit and septic tank.

8. Close loop solvent recovery system with adequate condenser system shall be provided to recover

solvent vapours in such a manner that recovery shall be maximum and recovered solvent shall be

reused in the process within premises.

9. Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB

guidelines. LDAR Logbooks shall be maintained.

10. The unit shall submit the list of authorized end users of hazardous wastes along with MoU signed

with them at least two months in advance prior to the commencement of production. In the absence

of potential buyers of these items, the unit shall restrict the production of the respective items.

11. Unit shall obtain all required permissions from the Narcotics Control Bureau for manufacturing,

storage and handling of Acetic Anhydride & any such chemicals.

12. Safety and Health:

a) PP shall obtain PESO permission for the storage and handling of hazardous chemicals. (If

applicable)

b) PP shall provide Occupational Health Centre (OHC) as per the provisions under the Gujarat

Factories Rule 68-U.

c) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the concern

authority as per the prevailing Rules / Gujarat Fire Prevention and Life Safety Measures Act,

2016.

d) Unit shall adopt functional operations/process automation system including emergency

response to eliminate risk associated with the hazardous processes.

e) PP shall carry out mock drill within the premises as per the prevailing guidelines of safety and

display proper evacuation plan in the manufacturing area in case of any emergency or

accident.

f) PP shall install adequate fire hydrant system within premises and separate storage of fire

water and foam for the same shall be ensured by PP. Also PP shall provide alarm system in

nearby fire station for emergency of any fire in plant area.

g) PP shall take all the necessary steps for control of storage hazards within premises ensuring

incompatibility of storage raw material and ensure the storage keeping safe distance as per

the prevailing guidelines of the concerned authority.

h) PP shall take all the necessary steps for human safety within premises to ensure that no any

harm is caused to any worker/employee or labor within premises.

i) Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.

j) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.

k) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam

pouring system etc. to restrict cascade fire emergency in solvent tank farm.

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2. SIA/GJ/IND2/173392/2020 M/s. Anil Synthetics

Plot No. 285/3, GIDC Estate - Ankleshwar,

Dist.: Bharuch

Appraisal


Project status: New






This is a new unit and proposes for manufacturing of synthetic organic chemicals [API and API

Intermediates] as tabulated below,

Sr. No.

Name of the Products

API OR INTERMEDIATE

CAS no. Quantity MT/Month

*End-use of products

1. 1-4-Chloro Benzhydryl Piperazine

Intermediate

303-26-4

30 TPM [Sr No. 1

to 30]

An antihistamine used to relieve allergy symptoms such as watery eyes, runny nose, itching eyes/nose, sneezing, hives, and itching. It works by blocking a certain natural substance that your body makes during an allergic reaction.

2. 1-[2,3 Di Chloro Phenyl] Piperazine Hydrochloride

Intermediate

119532-26-2

An antipsychotic- used in the treatment of schizophrenia and bipolar disorder and other uses include as an add-on treatment in major depressive disorder

3. Dibenzo[b,f][1,4]Thiazepin-11[10H]-One

Intermediate

3159-07-7

30 TPM [Sr No. 1

to 30]

Anti-psychotic -used to treat certain mental/mood conditions.

4. 4 Methyl Acetophenone

Intermediate

122-00-9 Anti-inflammatory-t is used to treat the pain and inflammation in osteoarthritis.

5. Bis (2-Chloroethyl) Amine Hydrochloride

Intermediate

821-48-7 An antifungal- used to treat certain infections caused by fungus

6. 8-Chloro-11-(4-methyl-1-piperazinyl)-5H-dibenzo [b,e][1,4] diazepine

Intermediate

5786-21-0

An antipsychotic medicine. It works by changing the actions of chemicals in the brain.Reduce the risk of suicidal behavior in people

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Page 32 of 232

with schizophrenia or similar disorders.

7. 2-[2-3(S)-3-[2-(7-chloro-2-quinolinyl) -ethyl]phenyl]-3-hydroxypropyl] phenyl-2-propanol

Intermediate

142569-70-8

Used in the treatment of asthma

8. 3,4-dimethoxybenzoyl chloride

Intermediate

3535-37-3

It is used for the treatment of Gastro esophageal Reflux Disease, Functional Dyspepsia, and other associated motility disorders.

9. 5-amino-2,4,6-triiodobenzene-1,3-dicarbonyl chloride

Intermediate

35453-19-1

It contrast agents are used to allow blood vessels, organs, and other non-bony tissues to be seen more clearly on a CT scan or other radiologic (x-ray) examination. it is used to help diagnose certain disorders of the heart, brain, blood vessels, and nervous system.

10. Methyl-5-bromo-2-hydroxy-3-propanoylbenzoate

Intermediate

91983-31-2

It is used to treat certain bladder/urinary tract symptoms. It is a smooth-muscle relaxant. It helps to reduce leaking of urine, feelings of needing to urinate right away, frequent trips to the bathroom, and bladder pain.

11. 5-Amino-2,4,6-triiodoisophthalic acid

Intermediate

37441-29-5

30 TPM [Sr No. 1

to 30]


12. 1-Acetyl-4-(4-hydroxyphenyl) Piperazine

Intermediate

67914-60-7

It is used to treat skin infections such as athlete's foot, jock itch, ringworm, This medication is also used to treat a skin condition known as pityriasis, a fungal infection that causes a lightening or darkening of the skin of the neck, chest,

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Page 33 of 232

arms, or legs.

13. 3-(3-chloropropyl)-7,8-dimethoxy-1,3-dihydro-2H-3-benzazepin-2-one

Intermediate

85175-59-3

It is used to treat heart failure.

14. 2-Butyl-4-Chloro-1H-imidazole-5-carbaldehyde

Intermediate

83857-96-9

It is used to treat high blood pressure (hypertension) and to help protect the kidneys from damage due to diabetes. It is also used to lower the risk of strokes in patients with high blood pressure and an enlarged heart.

15. 4-(4-aminophenyl) morpholin-3-one

Intermediate

438056-69-0

It is used to prevent or treat a type of blood clot called deep vein thrombosis (DVT), which can lead to blood clots in the lungs.

16. 6-Hydroxy-3,4-dihydroquinolin-2(1H)-one

Intermediate

54197-66-9

30 TPM [Sr No. 1

to 30]

It is used to improve the symptoms of a certain blood flow problem in the legs (intermittent claudication). cilostazol can decrease the muscle pain/cramps that occur during exercise/walking.

17. 1-(3-Chlorophenyl)-4-(3-Chloropropyl) Piperazine Hydrochloride

Intermediate

52605-52-4

It is used an antidepressant that increases serotonin activity in the brain. Trazodone is used for depression, anxiety, sleep and pain.

18. 1-(4-Fluorophenyl) Piperazine

Intermediate

2252-63-3

It is used to treat life-threatening low blood pressure that can occur with certain medical conditions or surgical procedures. Norepinephrine is often used during CPR (cardio-pulmonary resuscitation)

19. 2,6-Dimethylphenyl chloroacetamide

Intermediate

1131-01-7

Used to prevent and relieve pain -used to reduce pain or discomfort caused by skin irritations such as sunburn, insect bites, poison ivy, poison oak, poison sumac, and minor cuts, scratches, or burns

20. 4,4'[2-Pyridinylmethylene] Bisphenol

Intermediate

603-41-8 Used as a treatment for constipation or to prepare the large bowel before colonoscopy or surgery.

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21. Trans 4-Amino Cyclohexanol

Intermediate

27489-62-9

used in the treatment of respiratory diseases associated with viscid or excessive mucus

22. 3-[Aminomethyl]-5-Methyl Hexanoic Acid

Intermediate

128013-69-4

Used to treat epilepsy, neuropathic pain, fibromyalgia, restless leg syndrome, and generalized anxiety disorder.

23. 6 chloro-4- hydroxy- 2- methyl- 2H thieno [2,3-e] [1,2] thiazine- 3- carboxylate- 1,1- dioxide

Intermediate

70415-50-8

30 TPM [Sr No. 1

to 30]

Used for the treatment of various types of pain, especially resulting from inflammatory diseases of the joints, osteoarthritis, surgery, sciatica, and other inflammations.

24. 2-Amino 5-Methyl Thiazole

Intermediate

7305-71-7

Anti-inflammatory-used to treat pain and inflammation in rheumatic diseases and osteoarthritis.

25. 1-(3-Chlorophenyl) Piperazine

Intermediate

6640-24-0

It is an antidepressant that increases serotonin activity in the brain. It is used for depression, anxiety, sleep and pain.

26. 2-[2-(piperazin-1-yl)ethoxy]ethanol

Intermediate

13349-82-1

It is used to treat certain mental/mood conditions (such as schizophrenia, bipolar disorder, sudden episodes of mania or depression associated with bipolar disorder). Quetiapine is known as an anti-psychotic drug.

27. 4,4,4-trifluo-1-(4-methylphenyl) butane-1,3-dione

Intermediate

720-94-5 It works by reducing hormones that cause inflammation and pain in the body. it is used to treat pain or inflammation caused by many conditions such as arthritis, ankylosing spondylitis, and menstrual pain

28. 1-(4-methoxyphenyl)piperazine hydrochloride

Intermediate

38869-47-5

It is used in adults to treat infections caused by fungus. This includes infections in any part of the body including the lungs, mouth or throat, toenails, or fingernails. Some brands of itraconazole are not for use

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in treating fungal infections of the fingernails or toenails.

29. 3-(dimethylamino)-1(thiophen-2yl)propan-1-ol

Intermediate

132335-49-0

30 TPM [Sr No. 1

to 30]

Duloxetine is used to treat depression and anxiety. In addition, duloxetine is used to help relieve nerve pain (peripheral neuropathy) in people with diabetes or ongoing pain due to medical conditions such as arthritis, chronic back pain, or fibromyalgia (a condition that causes widespread pain).

30. 1-[2,4-d-Difluorophenyl]-2,3-epoxypropyl-1H-1,2,4-triazole methanesulfonate

Intermediate

86386-77-8

An antifungal medication used for a number of fungal infections.

Total 30 MT/Month

# Brief Note of Product Profile:

1. No of Manufacturing Plants: 1no’s

2. Brief Note regarding number of Products to be manufactured considering plant capacity:

Unit will manufacture any 2 products from above mention product [i.e. 1 to 30] as per

quantity mentioned hence at a time unit will manufacture 2 Products and total

production capacity will not exceed 30.0 MT/ Month.

ENDUSE OF PRODUCTS

Sr. No.

Name of the Product

CAS No. (Product)

Type/ Category of Product (API/ Intermediate)

In case of Intermediate stage of API Said API is used for/End Use of said API

Stage i.e. n-1, n-2, etc.

Name of API in which Intermediate Used/ End use of said Intermediate

CAS no. (API)

1. 1-4-Chloro Benzhydryl Piperazine

303-26-4 Intermediate

(n-1) Cetirizine 83881-51-0

An antihistamine used to relieve allergy symptoms such as watery eyes, runny nose, itching eyes/nose, sneezing, hives, and itching. It

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works by blocking a certain natural substance (histamine)

2. 1-[2,3 Di Chloro Phenyl] Piperazine Hydrochloride

119532-26-2

Intermediate

(n-1) Aripiprazole

HCl

129722-12-9

An antipsychotic- used in the treatment of schizophrenia and bipolar disorder and other uses include as an add-on treatment in major depressive disorder

3. Dibenzo[b,f][1,4]Thiazepin-11[10H]-One

3159-07-7

Intermediate

(n-1) Quetiapine Fumarate

111974-69-7

Anti-psychotic -used to treat certain mental/mood conditions.

4. 4 Methyl Acetophenone


(n-1) celecoxib 169590-42-5

Anti-inflammatory-t is used to treat the pain and inflammation in osteoarthritis.

5. Bis (2-Chloroethyl) Amine Hydrochloride


(n-1) Cyclophosphamide

50-18-0 an antifungal- used to treat certain infections caused by fungus

6. 8-Chloro-11-(4-methyl-1-piperazinyl)-5H-dibenzo[b,e][1,4] diazepine

5786-21-0

Intermediate

(n-1) clozapine 5786-21-0

An antipsychotic medicine. It works by changing the actions of chemicals in the brain. Used to treat schizophrenia after other treatments have failed. Reduce the risk of suicidal behavior in people with schizophrenia or similar disorders.

7. 2-[2-3(S)-3-[2-(7-chloro-2-quinolinyl) -ethyl] phenyl]-3-hydroxypropyl] phenyl-2-propanol

142569-70-8

Intermediate

(n-1) Montelukast

158966-92-8

Used in the treatment of asthma

8. 3,4-dimethoxybenzoyl chloride

3535-37-3

Intermediate

(n-1) Itopride 122898-67-3

It is used for the treatment of Gastroesophageal Reflux Disease, Functional

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Dyspepsia, and other associated motility disorders.

9. 5-amino-2,4,6-triiodobenzene-1,3-dicarbonyl chloride

35453-19-1

Intermediate

(n-1) Lopamidol

60166-93-0


10. Methyl-5-bromo-2-hydroxy-3-propanoylbenzoate

91983-31-2

Intermediate

(n-1) Flovaxate 15301-69-6

It is used to treat certain bladder/urinary tract symptoms. it is a smooth-muscle relaxant. it helps to reduce leaking of urine, feelings of needing to urinate right away, frequent trips to the bathroom, and bladder pain.

11 5-Amino-2,4,6-triiodoisophthalic acid

37441-29-5

Intermediate

(n-1) Lopamidol 60166-93-0


12. 1-Acetyl-4-(4-hydroxyphenyl)Piperazine

67914-60-7

Intermediate

(n-1) Ketoconazole

65277-42-1

It is used to treat skin infections such as athlete's foot, jock itch, ringworm, fungal infection that

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causes a lightening or darkening of the skin of the neck, chest, arms, or legs.

13. 3-(3-chloropropyl)-7,8-dimethoxy-1,3-dihydro-2H-3-benzazepin-2-one

85175-59-3

Intermediate

(n-1) Ivabradine 155974-00-8

It is used to treat heart failure.

14. 2-Butyl-4-Chloro-1H-imidazole-5-carbaldehyde

83857-96-9

Intermediate

(n-1) Losartan 114798-26-4

It is used to treat high blood pressure (hypertension) and to help protect the kidneys from damage due to diabetes. It is also used to lower the risk of strokes in patients with high blood pressure and an enlarged heart. Lowering high blood pressure and kidney problems.

15. 4-(4-aminophenyl)morpholin-3-one

438056-69-0

Intermediate

(n-1) Rivaroxaban

366789-02-8

It is used to prevent or treat a type of blood clot called deep vein thrombosis (DVT), which can lead to blood clots in the lungs (pulmonary embolism

16. 6-Hydroxy-3,4-dihydroquinolin-2(1H)-one

54197-66-9

Intermediate

(n-1) Cilostazol 73963-72-1

It is used to improve the symptoms of a certain blood flow problem in the legs (intermittent claudication). Cilostazol can decrease the muscle pain/cramps that occur during exercise/walking.

17. 1-(3-Chlorophenyl)-4-(3-Chloropropyl) Piperazine Hydrochloride

52605-52-4

Intermediate

(n-1) Trazodone 19794-93-5

It is used an antidepressant that increases serotonin activity in the brain. It is usedforDepression,

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anxiety, sleep and pain.

18. 1-(4-Fluorophenyl) Piperazine

2252-63-3

Intermediate

(n-1) Monatepil 103379-03-9

It is used to treat life-threatening low blood pressure (hypotension) that can occur with certain medical conditions or surgical procedures. Norepinephrine is often used during.

19. 2,6-Dimethylphenyl chloroacetamide

1131-01-7

Intermediate

(n-1) Lidocaine 137-58-6 used to prevent and relieve pain - used to reduce pain or discomfort caused by skin irritations such as sunburn, insect bites, poison ivy, poison oak, poison sumac, and minor cuts, scratches, or burns

20. 4,4'[2-Pyridinylmethylene] Bisphenol


(n-1) Sodium Picosulfate

10040-45-6

used as a treatment for constipation or to prepare the large bowel before colonoscopy or surgery

21. Trans 4-Amino Cyclohexanol

27489-62-9

Intermediate

(n-1) Ambroxol 23828-92-4

used in the treatment of respiratory diseases associated with viscid or excessive mucus

22. 3-[Aminomethyl]-5-Methyl Hexanoic Acid

128013-69-4

Intermediate

(n-1) Pregabalin 148553-50-8

Used to treat epilepsy, neuropathic pain, fibromyalgia, restless leg syndrome, and generalized anxiety disorder.

23 6 chloro-4- hydroxy- 2- methyl- 2H thieno [2,3-e] [1,2] thiazine- 3-

70415-50-8

Intermediate

(n-1) Lornoxicam 70374-39-9

Used for the treatment of various types of pain, especially resulting from

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carboxylate- 1,1- dioxide

inflammatory diseases of the joints, osteoarthritis, surgery, sciatica, and other inflammations.

24. 2-Amino 5-Methyl Thiazole

7305-71-7

Intermediate

(n-1) Meloxicam 71125-38-7

Anti-inflammatory- used to treat pain and inflammation in rheumatic diseases and osteoarthritis.

25 1-(3-Chlorophenyl) Piperazine

6640-24-0

Intermediate

(n-1) Trazodone 19794-93-5

It is an antidepressant that increases serotonin activity in the brain. it is used for depression, anxiety, sleep and pain.

26. 2-[2-(piperazin-1-yl)ethoxy]ethanol

13349-82-1

Intermediate

(n-1) Quetiapine 111974-69-7

It is used to treat certain mental/mood conditions (such as schizophrenia, bipolar disorder, sudden episodes of mania or depression associated with Bipolar disorder).

27. 4,4,4-trifluo-1-(4-methylphenyl) butane-1,3-dione


(n-1) Celecoxib 169590-42-5

It works by reducing hormones that cause inflammation and pain in the body. it is used to treat pain or inflammation caused by many conditions such as arthritis, ankylosing spondylitis, and menstrual pain

28. 1-(4-methoxyphenyl)piperazine hydrochloride

38869-47-5

Intermediate

(n-1) Itraconazole

84625-61-6

It is used in adults to treat infections caused by fungus. This includes infections in any part of the body including the lungs, mouth or throat, toenails, or

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fingernails. Some brands of itraconazole are not for use in treating fungal infections of the fingernails or toenails.

29. 3-(dimethylamino)-1(thiophen-2yl)propan-1-ol

132335-49-0

Intermediates

(n-1) Duloxetine 1165 39-59-4

Duloxetine is used to treat depression and anxiety. In addition, duloxetine is used to help relieve nerve pain (peripheral neuropathy) in people with diabetes or ongoing pain due to medical conditions such as arthritis,

30. 1-[2,4-d-Difluorophenyl]-2,3-epoxypropyl-1H-1,2,4-triazole methanesulfonate

86386-77-8

Intermediate

(n-1) Fluconazole

86386-73-4

An antifungal medication used for a number of fungal infections.





Sr. no. Particulars Details


(Rs. In Crores):

Total Project

5.0 Crores


Details Project Cost

(Rs. In Crores)

Land 0.7

Building 1.0

Machinery 1.5

EMP 1.8


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Sr. No

Unit Detail Capital Cost (Rs. In Crores)

Operating Cost (Rs. In Crores)

Maintenance Cost (Rs. In Crores)

Total Recurring Cost (Rs. In Crores)

1 Waste Water 20 KLD 0.4 0.088473 0.0528 0.1413

2 Air -- 0.25 --- 0.0046 0.0046

3 Hazardous Management

-- 0.24 0.012068 0.005 0.0171

4. Risk and Safety Audit and Safety Equipment (PPE, Safety Shower, Ventilation, etc.)

-- 0.45 0.00867 -- 0.0125

5. Cost of Fire Extinguisher, Fire hydrant line

-- 0.2 -- 0.0050 0.0083

5 Green Belt Development

-- 0.01 --- 0.0007 0.0007

6. AWH Monitoring

-- 0.2 0.004 0.00225 0.0063

7. Occupational Health

-- 0.05 --- 0.0042 0.0042

Total 1.8 0.1949

Summary

Cost of Project in Crores 5.0

EMP Capital Cost in Crores per Annum and

Percentage:

1.8 (36%)

EMP Recurring Cost in Crores per Annum

and Percentage:

2.34 (46.7%)

A-3 Details of CER as per OM dated 01/05/2018

As per OM no. 22-65/2017 on dated 01/05/2018 regarding ―Corporate Environment Responsibility‖ (CER), Greenfield projects have to contribute 2% of the Additional Capital Investment, the unit has planned to spend 4.0 % of the total cost of the proposed project (Rs.500 Lakhs) over a period of five years towards CER activity. So, as per the project cost Rs. 20 Lakhs used in the CER activities.

% as per the OM

Rs. in Crores

4% 0.2


BUDGETARY ALLOCATION FOR CER ACTIVITIES

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The unit has planned to spend 4.0 % of the total cost of the proposed project (Rs.500 Lakhs) over a period of five years towards CER activity. So, as per the project cost Rs. 20 Lakhs used in the CER activities. Budgetary allocation is given in below table.

Sr. No.

Activity

CER Activities Budget for 2

Years

1 Drinking Water Supply– Common Drinking Water Facility in Temple – Village

Bhadkodra

7.0

2 Electrification Including Solar Power– Motali Installation of Solar Street Light near Gam Panchayat Area

8.0

3 Development of Garden: We will develop a garden with facilities for young

children‘s and seating arrangement. (i.e., Sanjali)

5.0

TOTAL Rs. 20 Lakh


Details of Land/plot ownership are attached as Annexure-I.

B-1 Plot area

Total Plot area

1048.10 Sq. m.


Sr.No.

Area Ground Floor

First Floor

Second Floor

Sq. M.

%

1 Intermediate Production Area

100 100 100 300 10

2 R.M.Storage 40 40 40 120 4

3 F.G. Storage 15 0 0 15 1

4 Utility Area 30 0 0 30 3

5 ETP Area 50 0 0 50 5

6 Solid waste storage area 5 0 0 5 0

7 Haz waste storage area 10 0 0 10 1

8 Fresh Solvent Storage Area 10 0 0 10 1

9 Recovered Solvent Storage Area

25 0 0 25 2

10 Tank Farm storage area 30 0 0 30 3

11 Green Belt Area 262 0 0 262 25

12 Office Area/OH Centre 30 30 30 90 3

13 Open Area 441.075 0 0 441 42

TOTAL 1048.1 100

So, Adequate Area is available for Storage. As per above table we have

provided sufficient Finish product storage area. For raw material storage area,

we have provided separate storage area for chemicals to prevent Accident and

this area is sufficient to handle Safe products.

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B-3 Green belt area

Total (Sq. meter)

In side Plant Premises Outside Plant Premises (AIA)

Area in Sq. meter 419 320

% of total area 25% 30%


Total

15

D WATER

D-1

Source of Water Supply

GIDC Notified area Ankleshwar


Permission letter will provide you soon

D-2

Water consumption (KLD)

Category

Quantity

KLD

Remarks

(A) Domestic 2.0

(B) Gardening 1.0

(C) Industrial

Process 4.5

Washing 2.0

Boiler 4.8

Cooling 4.3

Others[Scrubber] 1.4


Total (A + B + C) 20.0

Summary of

water

requirement

Quantity

KLD

Remarks

Total water

requirement for

20.0

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the project (A)

Quantity to be

recycled (B)

4.0 2.0 KLD Steam Condensate + 2.0KLD Cooling Water will be re-use

Total fresh

water

requirement (C)

16.0

Ensure Total water requirement = Fresh

water + Recycled water

i.e. A = B + C

Reuse/Recycle details (KLD) with feasibility.

[Source of reuse & application area]

Source of

waste water

for reuse 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

Not Applicable


Category Waste water KLD

Remarks

(A) Domestic 1.5

(B) Industrial

Process 3.8

Washing 2.0

Boiler 1.0

Cooling 0.7

Others[Scrubber] 0.0

Total Industrial

waste water 7.5

Total [A + B] 9.0

Brief Note on worst case scenario for waste water generation (Qualitative and

Quantitative):

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We have calculated all the details based on stoichiometric calculation and based on that

considering worst case scenario Total Industrial Water consumption from production

quantity will be 4.5 KLD and waste water generation will be 3.8 KLD. Details of Product

wise water consumption and waste water generation is attached as Annexure II.

QUALITATIVE AND QUANTITATIVE ANALYSIS OF EACH WASTE STREAM

Sr. No.

Source of Waste Water Generation

Quantity [KLD]

Parameter

Quality Final load at ETP in Kg/day

1. Boiler blow down 1.0 pH 6.5-8.0 --

TSS 500-600 mg/L 0.6

COD 200-300 mg/L 0.3

TDS 2500-3000 mg/L 3.0

2. Cooling Tower blow down

0.7 pH 6.0-8.5 --

TSS 600-700 mg/L 0.49

COD 500-800 mg/L 0.56

TDS 3500-4000 mg/L 2.8

3. Washing 2.0 pH 5.0-6.5 --

TSS 1000-1500 mg/L 3.0

COD 1000-1200 mg/L 2.4

TDS 3000-4000 mg/L 8.0

4. Process 3.8 pH 3.0-6.5 --

TSS 800-1000 mg/L 5.7

COD 20000-25000 mg/L

95.0

TDS 35000-40000 mg/L

152

Total Industrial Effluent

7.5 - -

CHARACTERISTICS OF WASTEWATER BEFORE & AFTER TREATMENT:- [PRIMARY + SECONDARY + CMEE-BEIL]

Sr. No.

Parameters

Unit Before

Treatment After Primary

Treatment

After Secondary Treatment effluent

send to CMEE_BEIL

1. pH -- 3.5-5.5 6.5-8.5 6.5-8.5

2. T.S.S. mg/l 1000-1500 250-370 100-150

3. C.O.D. mg/l 20000-25000 17000-21500 5100-6400

4. T.D.S. mg/l 35000-40000 36500-41500 36500-41500

Brief justification in case of no process effluent generation or no industrial effluent

generation or no high concentration effluent generation from proposed project

(Whichever is applicable).

Not Applicable


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-

Domestic: Domestic waste water will be collected and will be treated into ETP. Domestic waste water will be used in aeration tank for adequate treatment.

Industrial: Effluent generated from Process, Utilities and Washing section will be mixed with effluent generated from Domestic and treated into ETP [Primary + Secondary] treatment plant and after adequate treatment effluent send to CMEE-BEIL for further disposal.

Scrubbing water will be goes along with by product which will be sell to authorized end users registered under rule-9.


For Domestic waste water:

Capacity of STP: Domestic waste water will be collected and will be treated into ETP.

Domestic waste water will be used in aeration tank for adequate treatment.

For Industrial waste water: Treatment facility within premises with capacity

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

Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In

case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.

Domestic: Domestic waste water will be collected and will be treated into ETP. Domestic waste water will be used in aeration tank for adequate treatment.

Industrial: Effluent generated from Process, Utilities and Washing section will be mixed with effluent generated from Domestic and treated into ETP [Primary + Secondary] treatment plant and after adequate treatment effluent send to CMEE-BEIL for further disposal.


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

Generated effluent will be treated into ETP and then send to CMEE_BEIL for further

treatment

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Not Applicable

Generated effluent will be treated into ETP and then send to CMEE_BEIL for further

treatment.

D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.

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

Not Applicable


occupied capacity and spare capacity and norms of acceptance of effluent from member

units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G

(5)/550706 dated 08/01/2020.

Membership Certificate is attached as Annexure-III.


E AIR

E-1 Brief Note on fuel based Heat energy requirement and worst case scenario

thereof: \

Considering the Calorific Value of the fuel and other parameters,

requirement of the heat, we have proposed consumption of fuel in m3/day.

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(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the

MOEFCC‘s OM vide dated 31.10.2019)

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 [Cap. 1TPH]

25

Natural Gas

860 Nm3/Day

Adequate Stack Height

PM SO2 NOx

2.

TFH [Cap. 2 Lakh K Cal/Hr.]

20

Natural Gas

300 Nm3/Day

3. DG Set [150 KVA]

15 Diesel 60

Lit/Day

Adequate Stack Height

E-3 Process gas 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/Vent

Height (meter)

Air Pollution Control Measures

(APCM)

1. Reaction Vessel-1 [Sr no. 1-4,6,7,810,11,12, 14,15,16,18]

HCl 18 Two Stage Water

Scrubber followed by Alkali Scrubber

2. Reaction Vessel-2 [SO2:-Sr no. 5,8,9,11] [HBr:-Sr no. 7,10,13,17]

SO2

HBr

18 Two Stage Alkali

Scrubber

Note:

Details of gaseous raw materials used in proposed project

Estimation of process gas emission (Product wise and Total)

Requirement of the scrubbing media (KL per Day) considering solubility (Product

wise and Total)

Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and


Details of scrubbing media are attached as Annexure-II.

E-4 Fugitive emission details with its mitigation measures.

Minimum Joints & flanges

Pumps with mechanical seals

Proper ventilation

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Adequate PPEs

F Hazardous waste

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

Note:

Priorities for HW Management: Pre-processing, Co-Processing,

Reuse/Recycle within premises, Sell out to actual users having Rule-9

permission, TSDF/CHWIH.

Quantification of hazardous waste shall be based on mass balance and

calculations shall be incorporated in EMP details separately.

Disposal to scrap vendors/vendors/traders is not allowed

Details of Product wise generation of Haz. Waste is attached as Annexure-II.


-

Sr. no.

Type/Name of Hazardous waste

Specific Source of generation (Name of the Activity, Product etc.)

Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Management of HW

1. Empty barrels/ containers/liners contaminated with hazardous chemicals /wastes

Raw Material

and Packaging

33.1 50 Collection, Storage, Transportation, reuse or send back to supplier or sell to authorize end users registered under rule-9.

2. Used or Spent Oil

From Machinery

5.1 1.0 Collection, Storage, Transportation and sold to authorized Recyclers.

3. ETP Sludge ETP 35.3 79 Collection, Storage, Transportation and sent to Common TSDF site (Ankleshwar/Dahej)

4. Distillation Residue

From Product No. 1,2,3,5-10,

12-28

20.3 72 Collection, Storage, transportation and sent for co-processing in cement industries disposal at CHWIF-Ankleshwar/Dahej. (Through GPS mounted vehicle)

5. Spent Carbon From Product No.

2,3,6,15

28.3 6

6. Spent Catalyst From Product No.

21

28.2 18

7. Acetic Acid From -- 315 Collection, Storage,

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[30-40%] Product No. 12,22

Transportation and sell to authorized end users registered under rule-9.

8. HCl Sol. [28-33%]

Scrubber & From

Product No. 1-

4,6,7,810,11,12,

14,15,16,18

-- 450 Collection, Storage, Transportation and sell to authorized end users registered under rule-9.

9. Sodium bisulfite Sol. [30-40%]

Scrubber & From

Product No. 5,8,9,11


10. Sodium Bromide [25-30%]

Scrubber & From

Product No. 7,10,13,17


11. Spent Solvent From Product No. 1,2,3,5-10,

12-28

28.6 730 Collection, Storage, Recovery and Recycle for manufacturing of product.

12. Sodium Hypo Chloride

Scrubber -- 10.0 Collection, Storage and reused in ETP as neutralizing agent.

13. Off-Specification Products

Process

28.4 5 Collection, Storage, transportation and sent for co-processing in cement industries disposal at CHWIF-Ankleshwar/Dahej. (Through GPS mounted vehicle)


(For HW management)


Membership certificate will provide you soon.


(MSW and others)

Not

Applicable

Sr. no.

Type/Name of Other wastes

Specific Source of generation (Name of the

Quantity (MT/Annum)

Management of Wastes

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Activity, Product etc.)

1 Not Applicable


G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of

recovered Solvents etc.

(Details in Table Format)

Sr. No.

Name of Product

Name of Solvent

Boiling Point

Fresh Qty of Solvent

(TPM)

Recovered Qty of

Solvent (TPM)

% Rec.

1 1-4-Chloro Benzhydryl Piperazine Toluene 110.6°C 30 28.8 96.00

2 1-[2,3 Di Chloro Phenyl] Piperazine Hydrochloride

Methanol 64.7 °C 60 58.2 97.00

3 Dibenzo[b,f][1,4]Thiazepin-11[10H]-One

Ethanol 78.37 °C 37.5 36.375 97.00

5 Bis (2-Chloroethyl) Amine Hydrochloride

EDC 83.47°C 51 48.96 96.00

Acetone 56°C 12 11.64 97.00

6 8-Chloro-11-(4-methyl-1-piperazinyl)-5H-dibenzo[b,e][1,4] diazepine

Toluene 110.6°C 27 26.055 96.50

MDC 39.6 °C 21 20.265 96.50

IPA 82.50C 15 14.475 96.50

7 2-[2-3(S)-3-[2-(7-chloro-2-quinolinyl) -ethyl]phenyl]-3-hydroxypropyl] phenyl-2-propanol

Tetra Hydro furan

66 °C 15 14.4 96.00

DMF 153°C 12 11.55 96.25

8 3,4-dimethoxybenzoyl chloride Toluene 110.6°C 13.5 12.96 96.00

10 Methyl-5-bromo-2-hydroxy-3-propanoylbenzoate

EDC 83.47°C 6 5.76 96.00

12 1-Acetyl-4-(4-hydroxyphenyl)Piperazine

Methanol 64.7 °C 9 8.7 96.67

13 3-(3-chloropropyl)-7,8-dimethoxy-1,3-dihydro-2H-3-benzazepin-2-one

Methanol 64.7 °C 6 5.76 96.00

14 2-Butyl-4-Chloro-1H-imidazole-5-carbaldehyde

Methanol 64.7 °C 6 5.76 96.00

15 4-(4-aminophenyl)morpholin-3-one Toluene 110.6°C 6 5.76 96.00

16 6-Hydroxy-3,4-dihydroquinolin-2(1H)-one

Methanol 64.7 °C 6 5.76 96.00

17 1-(3-Chlorophenyl)-4-(3-Chloropropyl) Piperazine Hydrochloride

Toluene 110.6°C 6 5.76 96.00

18 1-(4-Fluorophenyl) Piperazine IPA 82.50C 9 8.76 97.33

19 2,6-Dimethylphenyl chloroacetamide Toluene 110.6°C 9 8.7 96.67

20 4,4'[2-Pyridinylmethylene] Bisphenol Ethyl Acetate 77.1°C 15 14.7 98.00

Methanol 64.7 °C 6 5.76 96.00

21 Trans 4-Amino Cyclohexanol Toluene 110.6°C 15 14.4 96.00

22 3-[Aminomethyl]-5-Methyl Hexanoic Acid

Methanol 64.7 °C 15 14.625 97.50

23 6 chloro-4- hydroxy- 2- methyl- 2H thieno [2,3-e] [1,2] thiazine- 3- carboxylate- 1,1- dioxide

Methanol 64.7 °C 9 8.7 96.67

Toluene 110.6°C 15 14.4 96.00

24 2-Amino 5-Methyl Thiazole Toluene 110.6°C 15 14.4 96.00

25 1-(3-Chlorophenyl) Piperazine Toluene 110.6°C 6 5.76 96.00

26 2-[2-(piperazin-1-yl)ethoxy]ethanol Xylene 139 °C 12 11.7 97.50

27 4,4,4-trifluo-1-(4-methylphenyl) butane-1,3-dione

Ethanol 78.37 °C 6 5.76 96.00

Methanol 64.7 °C 4.2 4.05 96.43

28 1-(4-methoxyphenyl)piperazine hydrochloride

Toluene 110.6°C 9 8.7 96.67

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Sr.

No.

Source Probable

Pollutant

Emission

Control Measures/ APCM

1. Solvent storage tank Air pollutant (VOC)

i) Carry out work place area

monitoring to find out concentration

level in ambient air.

ii) Provision of breather valve

cum flame arrester.



H SAFETY details

H-1 Details regarding storage of Hazardous chemicals

(For tank storages only including spent acid and spent solvent tanks)

-

Sr. no Name of Chemical Capacity of Tank

Number of Tanks

Hazardous Characteristics of Chemical

1 Methanol 8.0 KL 1 Nos. Flammable

2 Toluene 5.0 KL 1 Nos. Flammable

3 H2SO4 3.0 KL 1 Nos. Corrosive

Brief note on storage of Hazardous chemicals in Tanks

Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels,

Carboys, Bags etc.

Other raw materials are store in Drums and Bags.


Type of Hazardous Chemicals

Safety measures

HYDROGEN

• CCE approved premises with door having locking arrangement provided.

• Protect cylinders against physical damage. • Store in cool, dry, well-ventilated area, away from sources of heat,

ignition and direct sunlight. • Do not allow area where cylinders are stored to exceed 52°C

(125°F). • Isolate from oxidizers such as oxygen, chlorine, or fluorine. • Use a check valve or trap in the discharge line to prevent hazardous

backflow. • Post ―No Smoking or Open Flame‖ signs in storage and use areas. • Cylinders should be stored upright and be firmly secured to prevent

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falling or being knocked over. • Cylinders can be stored in the open, but in such cases, should be

protected against extremes of weather and from the dampness of the ground to prevent rusting.

• Never tamper with pressure relief devices in valves and cylinders. Electrical equipment should be non-sparking or explosion proof.

• Flammable high-pressure gas. • Use only in a closed system. • Use piping and equipment adequately designed to withstand

pressures and temperatures to be encountered. • Gas can cause rapid suffocation due to oxygen deficiency. • Never work on a pressurized system. • If there is a leak, close the cylinder valve. Blow the system down in

a safe and environmentally sound manner in compliance with all federal, state, and local laws; then repair the leak.

• Never place a compressed gas cylinder where it may become part of an electrical circuit.

• Apron, Hand gloves, gumboot, goggles & helmet provided • ISI Portable fire extinguisher & Hydrant line is provided as per TAC

norms. • Flame proof fitting provided. • Sufficient Nos. of SBA sets & 2 No. of Air line mask.

Hydrogen cylinders

Hydrogen cylinders will be stored in cylinder storage area. Cylinder storage license will be obtained from PESO as per Gas cylinder rules.

Hydrogen cylinder storage area will be made well ventilated and safe distance will be maintained as per gas cylinder rule.

Sprinkler system provision will be made in cylinder storage area.

Gas detectors will be provided in Hydrogen cylinder storage area.

Copper tube will be used for Hydrogen cylinder connection with header. PRV station will be provided for Hydrogen and nitrogen cylinder header.

Non sparking tools will be used for cylinder connection with header.

FLP type area will be provided.

Total enclosed process system.

Instrument & Plant Air System. DCS operational plant.

Nitrogen blanketing in Hydrogenation reactor.

Safety valve and Rupture disc provided on reactor.

Cooling Chilling and power alternative arrangement have been made on reactor.

Hydrogen and Nitrogen Cylinder bank away from the autoclave reactor.

PRV station with shut off valve, safety valve provision will be made for hydrogenation reaction safety.

Before Hydrogen Gas charging into reactor and after completion of reaction Nitrogen flushing will be done.

Flame arrestor will be provided on vent line of reactor and it will be extended up to roof level.

Open well ventilated and fragile roof will be provided to on reactor.

Safe Catalyst charging method will be adopted.

SOP will be prepared and operators will be trained for the same.

Static earthing and electric earthing (Double) provided.

Rector vent extended out side the process area and flame arrestor

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provided on vent line.

Dumping vessel arrangement will be made.

Jumpers for static earthing on pipeline flanges of flammable chemical will be provided.

Ethyl Acetate

Apron, Hand gloves, gumboot, goggles and helmet will be provided.

ISI Portable fire extinguisher & Hydrant line is provided as per TAC norms.

Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.

Level indicator provided. SBA set, Canister mask and airline mask is provided. Vent line dipped in dilute caustic will be provided. RCC foundation will be provided. Transfer material to another empty Vessel.

HCl Valve, pipeline are checked and maintain, in good condition. Apron, Hand gloves, gumboot, goggles and helmet will be provided. ISI Portable fire extinguisher & Hydrant line is provided as per TAC

norms. Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.

Level indicator provided. Vent line dipped in water will be provided. RCC foundation will be provided. Transfer material to another empty Vessel.

DMF/ EDC

All Gaskets are checked periodically & if new one replaces found

defective.

Joints are checked regularly to found any Leakage. Apron, Hand gloves, gumboot, goggles and helmet provided. ISI Portable fire extinguisher & Hydrant line is provided as per

TAC norms. Sufficient amount of sand/soil are kept to control any spillage. Flame proof fitting provided. Eye washer cum shower is provided near storage area.

Level indicator provided. Spark arrester are installed on all vehicles inside the premises. Vent line provided at sufficient height above roof building. Level indicator provided.

Methanol / Toluene/ Acetone/ Butanol

Tank, valve, pipeline are checked and maintain, in good condition through preventive maintenance.

Joints are checked regularly to detect any Leakage. ISI Portable fire extinguisher & Fire Hydrant line is provided as per

TAC norms. Flame proof electrical fittings / installation provided. Proper Earthing, Bonding & flange-to-flange jump ring is provided. Flame arrester provided on vent line. CCE approved Separate Storage area with door having locking

arrangement. Auto & manual sprinkler provided. Spark arrester are installed on all vehicles inside the premises. Apron, Hand gloves, gumboot, goggles and helmet provided. Train operator employed. Eye washer & shower provided. Tank‘s thickness measured on regular interval.

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Good ventilation in the area. Flame arrester with breather valve. Perforated dip pipe in dyke wall will be provided to monitor & detect

any leakage from tank. Sump will be made under dyke to recover leakage material from

dyke. Tanks will be kept under RCC dyke. Tanks will be kept under shed. All tanks will be connected to ETP.

Iso Propyl Alcohol

Valve, pipeline are checked and maintain, in good condition. Apron, Hand gloves, gumboot, goggles and helmet will be provided. ISI Portable fire extinguisher & Hydrant line is provided as per TAC

norms. Flameproof electrical connection will be provided. Separate storage area will be provided. Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.

Level indicator provided. RCC foundation will be provided.

Caustic Soda Lye

Dyke wall with sufficient size is provided. Tank, valve, pipeline are checked and maintain, in good condition. Apron, Hand gloves, gumboot, goggles and helmet provided. ISI Portable fire extinguisher & Hydrant line is provided as per TAC

norms. Sufficient amount of sand/soil are kept to control any spillage. Eye washer cum shower is provided near storage area.

Level indicator provided.

AMMONIA (NH3)

• All Gaskets are checked periodically & if new one replaces found defective.

• Joints are checked regularly to found any Leakage. • ADEQUATE PPE is kept to handle the Hazard. • ISI Portable fire extinguisher & Hydrant line is provided as per TAC

norms. • Sufficient amount of sand/soil are kept to control any spillage. • Flame proof fitting provided. • Eye washer cum shower is provided near storage area. • Level indicator provided. • Spark arrester are installed on all vehicles inside the premises. • SBA set, Canister mask and airline mask is provided. • Earthing& bonding on tanks is provided. • Vent line dipped in water will be provided. • RCC foundation will be provided. • Transfer material to another empty Vessel.

Applicability of PESO : Applicable

H-2 Types of hazardous Processes involved and its safety measures:

(Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)

-

Type of Process

Safety measures including Automation

Hydrogenation process:-A

For hydrogenation process, hydrogen gas will be used. Unit will allot separate storage area for hydrogen gas cylinder. Hydrogen is a colorless, odorless, tasteless, flammable nontoxic gas which is flammable over a wide range of concentrations.

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Standard Operating procedure shall be made for before Hydrogen Gas charging into reactor and after completion of reaction Nitrogen flushing will be done.

SOP will be prepared and operators will be trained for the same. Nitrogen blanketing will be done in Hydrogenation reactor. Safety

valve and Rupture disc will be provided on reactor. Safe Catalyst charging method will be adopted. Flame arrestor will be provided on vent line of reactor and it will be

extended above the roof level. Static earthing and electric earthing (Double) will be provided. Hydrogen gas detector will be installed for early detection of gas

leak. One RCC wall having thickness 20 cm will be provided on all side of

hydrogenation reactor to protect surrounding and other infrastructure during worst case scenario.

Nitration process

Not applicable

Chlorination process

Not applicable

Exothermic Reaction

Not applicable


-

Total Plot Area: 1048.8.00 M2

Area utilized for plant activity: 363.0.00 M2

Area utilized for Hazardous Chemicals Storage:

238.00 M2

Number of Floors: G+2

Water requirement for firefighting in KLD :

0.0

Water storage tank provided for firefighting in KLD:

150 KL

Details of Hydrant Pumps: 5

Nearest Fire Station : 1-2 km

Applicability of Off Site Emergency Plan: Yes

-


After Getting EC/NOC we will apply for fire NOC.


-


Number of Contractual person/Labour : 10

Area provided for OHC: 30 sq. meter.

Number of First Aid Boxes : 3

Nearest General Hospital : 2 km

Name of Antidotes to be store in plant :


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Project proponent (PP) and Technical expert of PP, M/s. Ecopreneur Incorporate remains present during


Committee noted that the proposal is for Greenfield project in GIDC Ankleshwar. PP submitted details


depth. Looking to layout plan, Committee insisted for submit revised layout plan with mentioning

adequate separate entry and exit which is later on submitted by PP.

Committee noted that PP has submitted waste water management and total industrial effluent will be

treated in ETP and treated effluent will be sent to CMEE of M/s BEIL for evaporation. Domestic sewage

will be treated in ETP.

PP submitted that they have proposed boiler and DG set. Fuel used will be Natural gas for boiler and

thermo pack. Committee insisted for adequate stack height for thermo pack and PP later on submitted

revised flue gas emission details. Two stage scrubbers will be provided as APCM with each process

reactor stack. PP submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.



exit separately, proposed fire extinguishers details adequate fire water reservoir and fire load calculation.

Committee insisted for adequate fire water tank of 150 KL and PP later on submitted revised details.

Committee noted that PP has addressed fire evacuation plan, worker‘s safety and occupational Health

centre (OHC) and process hazard and its safety control measures. Committee insisted for auto control

system cost in EMP and PP later on submitted revised EMP.


CER, LDAR and solvent recovery etc. Looking to green belt area and plot size, Committee insisted for

more area of green belt outside premises and PP later on submitted Ankleshwar Industries Association

letter regarding it. Committee insisted for revised CER activity for infrastructure development instead of

general activity looking to cost of CER fund and PP later on submitted revised CER activity.







& 14/11/2019.





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Page 59 of 232


amendments.



5. PP shall manufacture any two products from product list as per layout submitted by PP.

6. Wastewater shall be fed to CMEE only after providing adequate treatment in such a way that no


7. The PP shall develop green belt [419 m2 inside plant premises + 320 m2 ouside the premises =

Total: 739 Sq. m.) i.e. 55 % of total plot area ] as per the undertaking submitted / committed before

SEAC. Green belt shall be developed with native plant species that are significant and used for the

pollution abatement as per the CPCB guidelines. It shall be implemented within 3 years of operation

phase in consultation with GPCB.















applicable)





2016.





accident.



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Page 60 of 232








j) Unit shall provide water sprinkler in Ammonia storage area.

k) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.

l) Unit shall store Bromine Bottle in cool dry separate area, out of direct sunlight.

m) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam


3. SIA/GJ/IND2/173420/2020 M/s. Will Care Pharma

Plot No. 8/7, GIDC- Panoli, Ta-Ankleshwar,

Dist. Bharuch

Appraisal


Project status: New






This is a new unit proposes manufacturing of synthetic organic chemicals [API and API Intermediates] as

tabulated below,

Sr. No.

Name of Product CAS NO. Quantity (MT/Month) End Use Remarks

GROUP-A

1 Oxcarbazepine & it‘s intermediate 28721-07-5

60.0

Anticonvulsants Unit is proposed to mfg either individual or total production of (Product No.- 1 to 23) shall not exceed 60 MT/Month.

10-Methoxy Carbezapine 28721-09-7 Intermediate of Oxcarbazepine

2 Fluconazole & it‘s intermediate 86386-73-4 Anti allergies

DFTA(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl)Acetophenone)

86404-63-9

Intermediates of Fluconazole (1-[2-(2,4- difluorophenyl)-2,3-

epoxypropyl]-1H-1,2,4-Trizole) 86386-76-7

3 Gapapentin & it‘s intermediate Anticonvulsant

2-Azaspiro[4.5]decan-3-one 64744-50-9 Intermediate of Gabapentin

1,1-Cyclohexanediacetic acid monoamide

99189-60-3

4 Quetiapine Fumarate 111974-69-7 anti-psychotic

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5 Fenofibrate 49562-28-9 Antihyperlipidemic

6 Telmisartan & it‘s intermediate 144701-48-4 Antihypertensive

4-Methyl -6-(1-methyl-1H-benzoimidozol-2-yl)-2-propyl-1H-benzo imidazole

152628-02-9

4-Bromomethyl)biphenyl-2-carboxylic acid methyl ester

114772-38-2

Mehtyl -4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]methyl]biphenyl carboxylate

528560-93-2

7 Losartan Potassium & it‘s intermediate

114798-26-4 Antihypertensive

4‘-Bromomethyl-biphenyl-2-carbonitrile

114772-54-2

Intermediate of Losratan

2-butyl-4-chloro-5-formylimidazole 83857-96-9

4‘-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile

11477-55-3

2-Butyl-5-chloro-3-[2‘(2H-tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde

114798-36-6

8 Teneligliptin & it‘s intermediate 760937-92-6 Anti Diabetic

tert-butyl 4-oxo-2-(1,3-thiazolidin-3-ylcarbonyl)pyrrolidine-1-carboxylate OR (2S)-4-Oxo-2-(3-thiazolidinylcarbonyl)-1-pyrrolidinecarboxylic acid tert-butyl ester

401564-36-1 Intermediates of Teneligliptin

9 Aceclofenac Sodium & it‘s intermediate

89796-99-6 Anti Flammatory

Tert Buyl Chloroacetate 107-59-5 Intermediate of Aceclofenac

10 Hyscin Butylbromide & it‘s intermediate

149-64-4 Antimuscarinic

11 Rabeprazole Sodium & it‘s intermediate

117976-89-3 Antiulcer

2-[[[4-(3-methoxypropoxy)-3-methyl-2-pyridinyl] methyl] thio]-1H-benzimidazole

117977-21-6 Intermediates of Rabeprazole Sodium 2-[[4-(3-methoxypropoxy)-3-methyl-

pyridin-2-yl]methylsulfinyl]-1H-benzoimidazole

N/A

12 Etoricoxib & it‘s intermediate 202409-33-4 anti-inflammatory

2-Chloro -3-(dimethylamino)propene-1-iminium

N/A Intermediate of Etoricoxib

13 Tranexamic Acid & it‘s intermediate 1197-18-8 Used to treat heavy bleeding during your menstrual period

4(Aminomethyl)benzoic acid 56-91-7 Intermediate of Tranexamic Acid

4(Aminomethyl)cyclohexanecar boxilic acid

1197-18-8

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14 Pantoprazole & it‘s intermediate 102625-70-7 Used for heartburn, acid reflux and gastro-oesophageal reflux disease

2-Chloromethyl-3,4-dimethoxypyridini hydrochloride 72830-09-2 Intermediates of

Pantoprazole

5-Difluoromethoxy-2-{[(3,4-dimethoxy-2-pyridinyl)methyl]thio}-1H-benzimidazole 102625-64-9

15 Clopidogrel Bisulphate 120202-66-6 Antiplatelet

Methyl (+)-alpha-(2-thienylethylamino)(2-chlorophenyl)acetate

141109-19-5

Intermediate of Clopidogrel Bisulphate

16 2-n-Butyl-3(4-Hydroxy Benzoyl) Benzofuran (n-3)

52490-15-0 Intermediate of Amiodarone HCL

17 4-(2-Methoxy ethyl) Phenol 56718-71-9 Intermediate of Metoprolol succinate

18 P-chloro benzophenone 134-85-0 Intermediate of Cetirizine Dihydrochloride

19 P- chloro Benzhydryl chloride 134-83-8 Intermediate of Cetirizine Dihydrochloride

20 P-chloro benzhydryl piperazine 303-26-4 Intermediate of Cetirizine Dihydrochloride

21 Ketosulfone 221615-75-4 Intermediate of Etoricoxib

22 Thiophene-2-ethanol 5402-55-1 Intermediate of Nebivolol HCI

23 Bis-(2-chloroethyl amine)hydrochloride

821-48-7 Intermediate of Apiprazole

GROUP-B

24 Pregabalin & it‘s intermediate

148553-50-8

20.0

Anti -nervousness

Unit is proposed to mfg either individual or total production of (Product No.- 24 to 32) shall not exceed 20 MT/Month.

R-(-)-3-(Carbomethyl)-5-mehtyl hexonic acid R(+)-Alpha Phenylamine salt

3886-69-9 Intermediate of Pregabalin

25 Rosuvastatin Calcium 147098-20-2 Cardiovascular Disease

N-[4-4-Fluoro-phenyl)5-formyl-6-isopropyl-pyrimidine -2-yl]-N-methyl-methanesulfonamide

147118-37-4

3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid ethyl ester

147118-35-2

7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy-5-oxo-hept-

851443-04-4

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6-enoic acid ethyl ester

26 Atorvastatin Calcium & it‘s intermediate

134523-00-5 Antihypertensive

[6-(2-Aminol-ethyal)-2,2 dimethyl-[1,3]dioxin-4-y]-acetic acid tert-buytl ester

125995-13-3

Intermediate of Atorvastatin

6-[2,[2(-4-fluoro-phenyl)5-isopropyl-3-phenyl-4-phenylcarbomoyl-pyrrol-1-yl-]ethyl}-2,2-lyhtemid-[1,3]dioxin-4-yl)-tret dicaciteca -retse lytub

125971-95-1

7-[2-(4-flouro-phenyl)-5-isopropyl-3-phenyl-4-phentlcarbomyl-pyrrol-1-yl]-3,5 hydroxy-heptanoic acid-tert butyl(

134395-00-9

27 Carvedilol 72956-09-3 Antihypertansive

3-(Phenylhydrazino)cyclohexanone 27385-45-1 Intermediate of Carvedilol 4-Oxo-1,2,3,4-tetrahydrocarbezole 15128-52-6

4-(2,3-Epoxypropoxy)carbazole 51997-51-4

28 Glimipride & it‘s intermediate 93479-97-1 To treat type 2 diabetes

(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1(N—2-phenyl ethyl)-carboxamido]

N/A

Intermediate of Glimipride

4-[2-[(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1-yl) carboxamido] ethyl]benzene sulfonamide

119018-29-0

29 Thiocolchicoside 602-41-5 used as a muscle relaxan

30 Nimesulide & it‘s intermediate 51803-78-2 anti-inflammatory drug

O- Phenoxy Nitrobenzene 2216-12-8 Intermediate of Nimesulide

O- Phenoxy Aniline 2688-84-8

O- Phenoxy Methane N/A

31 Diclofenac Sodium & it‘s intermediate 15307-79-6 Anti Flammatory

(2,6-DICHLORO PHENYLAMINE) 15307-93-4

Intermediate of Diclofenac Sodium

(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)

15308-01-7

(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)

15362-40-0

32 Albendazole 54965-21-8 Anthelmintic

4-Thiocyno-2-Nitro- anilnemol 54029-45-7 Intermediate of Albendazole

2-Nitro-4-propyl thio aniline 54393-89-4

1,2,diamine-5-propyl thio benznene 66608-52-4

33 R&D -- 0.3

Total 80.3

# Brief Note of Product Profile: 3. No of Manufacturing Plants: 15 Reaction Vessel 4. Brief Note regarding number of Products to be manufactured considering plant capacity:

They have applied for (32 + R&D) nos. of product in either & or condition, They will not manufacturing above 80.3 MT/Month. And as per the list of machinery, they will be manufacturing 2 to 3 products at a time as orders received from market.

ENDUSE OF PRODUCTS

Sr. No.

Name of the Product CAS No. (Product)

Type/ Category of

Stage of Intermediat

Name of API in which

CAS No.

Said API is used for/End

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Page 64 of 232

Product (API/

Intermediate)

e n-1, n-2, etc

Intermediate Used/ End use

of said Intermediate

(API) Use of said API

GROUP-A (Unit is proposed to mfg either individual or total production of Group - A (Product No.- 1 to 23) shall not exceed 60 MT/Month.)

1 Oxcarbazepine & it‘s intermediate

28721-07-5 API -- -- -- Anticonvulsants

10-Methoxy Carbezapine


(n-2) Intermediate of Oxcarbazepine

28721-

07-5

Anticonvulsants

2 Fluconazole & it‘s intermediate

86386-73-4 API -- -- -- Anti allergies

DFTA(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl)Acetophenone)


(n-2) Intermediates of Fluconazole

86386-

73-4

Anti allergies

(1-[2-(2,4- difluorophenyl)-2,3-epoxypropyl]-1H-1,2,4-Trizole)


(n-3) Intermediates of Fluconazole

86386-

73-4

Anti allergies

3 Gapapentin & it‘s intermediate

60142-96-3 API -- -- -- Anticonvulsan

t

2-Azaspiro[4.5]decan-3-one


(n-3) Intermediate of

Gabapentin

60142-

96-3

Anticonvulsan

t

1,1-Cyclohexanediacetic acid monoamide


(n-2) Intermediate of Gabapentin

60142-

96-3

Anticonvulsan

t

4 Quetiapine Fumarate

111974-69-7

API -- -- -- anti-psychotic

5 Fenofibrate 49562-28-9 API -- -- -- Antihyperlipidemic

6 Telmisartan & it‘s intermediate

144701-48-4

API -- -- -- Antihypertensive

4-Methyl -6-(1-methyl-1H-benzoimidozol-2-yl)-2-propyl-1H-benzo imidazole

152628-02-9

Intermediate

(n-4) Intermediate of Telmisartan

144701-48-4

Antihypertensive

4-Bromomethyl) biphenyl-2-carboxylic acid methyl ester

114772-38-2

Intermediate


144701-48-4

Antihypertensive

Mehtyl -4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]methyl]biphenyl carboxylate

528560-93-2

Intermediate


144701-48-4

Antihypertensive

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7 Losartan Potassium & it‘s intermediate

114798-26-4


4‘-Bromomethyl-biphenyl-2-carbonitrile

114772-54-2

Intermediate


Losratan

11479

8-26-4

Antihypertensi

ve

2-butyl-4-chloro-5-formylimidazole



Losratan

11479

8-26-4

Antihypertensi

ve

4‘-(2-Butyl-4-chloro-5-formyl-imidazol-1-ylmethyl)-biphenyl-2-carbonitrile


(n-3) Intermediate of Losratan

11479

8-26-4

Antihypertensive

2-Butyl-5-chloro-3-[2‘(2H-tetrazol-5-yl)-biphenyl-4-ylmethy]-3H-imidazole-4-carbaldehyde

114798-36-6

Intermediate

(n-2) Intermediate of Losratan

11479

8-26-4

Antihypertensive

8 Teneligliptin & it‘s intermediate

760937-92-6

API -- -- -- Anti Diabetic

tert-butyl 4-oxo-2-(1,3-thiazolidin-3-ylcarbonyl)pyrrolidine-1-carboxylate OR (2S)-4-Oxo-2-(3-thiazolidinylcarbonyl)-1-pyrrolidinecarboxylic acid tert-butyl ester

401564-36-1

Intermediate

(n-1) Intermediates

of

Teneligliptin

76093

7-92-6

Anti Diabetic

9 Aceclofenac Sodium & it‘s intermediate

89796-99-6 API -- -- -- Anti Flammatory

Tert Buyl Chloroacetate


(n-1) Intermediate of Aceclofenac

89796-99-6

Anti Flammatory

10 Hyscin Butylbromide & it‘s intermediate

149-64-4 API -- -- -- Antimuscarinic

11 Rabeprazole Sodium & it‘s intermediate

117976-89-3

API -- -- -- Antiulcer

2-[[[4-(3-methoxypropoxy)-3-methyl-2-pyridinyl] methyl] thio]-1H-benzimidazole

117977-21-6

Intermediate

(n-2) Intermediates of Rabeprazole Sodium

11797

6-89-3

Antiulcer

2-[[4-(3-methoxypropoxy)-3-methyl-pyridin-2-yl]methylsulfinyl]-1H-benzoimidazole

N/A Intermediate

(n-1) Intermediates

of

Rabeprazole

Sodium

11797

6-89-3

Antiulcer

12 Etoricoxib & it‘s intermediate

202409-33-4

API -- -- -- anti-inflammatory

2-Chloro -3-(dimethylamino)

N/A Intermediate

(n-1) Intermediate of Etoricoxib

202409-33-4

anti-inflammatory

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propene-1-iminium

13 Tranexamic Acid & it‘s intermediate

1197-18-8 API -- -- -- Used to treat heavy bleeding during your menstrual period

4(Aminomethyl)benzoic acid



Tranexamic

Acid

1197-

18-8

Used to treat

heavy

bleeding

during your

menstrual

period

4(Aminomethyl)cyclohexanecar boxilic acid


(n-1) Intermediate of Tranexamic Acid

1197-

18-8

Used to treat heavy bleeding during your menstrual period

14 Pantoprazole & it‘s intermediate

102625-70-7

API -- -- -- Used for heartburn, acid reflux and gastro-oesophageal reflux disease

2-Chloromethyl-3,4-dimethoxypyridini hydrochloride


(n-3) Intermediates of Pantoprazole

10262

5-70-7

Used for heartburn, acid reflux and gastro-oesophageal reflux disease

5-Difluoromethoxy-2-{[(3,4-dimethoxy-2-pyridinyl)methyl]thio}-1H-benzimidazole

102625-64-9

Intermediate

(n-1) Intermediates of Pantoprazole

10262

5-70-7

Used

for heartburn,

acid

reflux and

gastro-

oesophageal

reflux disease

15 Clopidogrel Bisulphate

120202-66-6

API -- -- -- Antiplatelet

Methyl (+)-alpha-(2-thienylethylamino)(2-chlorophenyl)acetate

141109-19-5

Intermediate

(n-1) Intermediate of Clopidogrel Bisulphate

12020

2-66-6

Antiplatelet

16 2-n-Butyl-3(4-Hydroxy Benzoyl) Benzofuran


(n-3) Intermediate of Amiodarone HCL

19774-

82-4

Anti-

arrhythmic

17 4-(2-Methoxy ethyl) Phenol


(n-3) Intermediate of Metoprolol succinate

98418-

47-4

Antihypertansi

ve

18 P-chloro 134-85-0 Intermediat (n-4) Intermediate of 83881- Antihistamine

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benzophenone e Cetirizine Dihydrochloride

52-1

19 P- chloro Benzhydryl chloride


(n-3) Intermediate of Cetirizine Dihydrochloride

83881-

52-1

Antihistamine

20 P-chloro benzhydryl piperazine



Cetirizine

Dihydrochlorid

e

83881-

52-1

Antihistamine

21 Ketosulfone 221615-75-4

Intermediate

(n-3) Intermediate of Etoricoxib

20240

9-33-4

NSAID

22 Thiophene-2-ethanol 5402-55-1 Intermediate

(n-3) Intermediate of Nebivolol HCI

12020

2-66-6

Antiplatelet

23 Bis-(2-chloroethyl amine)hydrochloride


(n-3) Intermediate of Aripiprazole

12972

2-12-9

Antidepressant

GROUP-B(Unit is proposed to mfg either individual or total production of Group - B (Product No.- 24 to 32) shall not exceed 20 MT/Month.)

24 Pregabalin & it‘s intermediate

148553-50-8

API -- -- -- Anti -nervousness

R-(-)-3-(Carbomethyl)-5-mehtyl hexonic acid R(+)-Alpha Phenylamine salt

3886-69-9

Intermediate

(n-2) Intermediate

of Pregabalin

148553-

50-8

Anti -nervousness

25 Rosuvastatin Calcium

147098-20-2

API -- -- -- Cardiovascular

Disease

N-[4-4-Fluoro-phenyl)5-formyl-6-isopropyl-pyrimidine -2-yl]-N-methyl-methanesulfonamide

147118-37-4

Intermediate

(n-4) Intermediate of Rosuvastatin Calcium

147098-

20-2

Cardiovascular Disease

3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid ethyl ester

147118-35-2

Intermediate


147098-

20-2


7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methansulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy-5-oxo-hept-6-enoic acid ethyl ester

851443-04-4

Intermediate


147098-

20-2


26 Atorvastatin Calcium & it‘s intermediate

134523-00-5


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[6-(2-Aminol-ethyal)-2,2 dimethyl-[1,3]dioxin-4-y]-acetic acid tert-buytl ester

125995-13-3

Intermediate

(n-3) Intermediate of Atorvastatin

134523-

00-5

Antihypertensive

6-[2,[2(-4-fluoro-phenyl)5-isopropyl-3-phenyl-4-phenylcarbomoyl-pyrrol-1-yl-]ethyl}-2,2-lyhtemid-[1,3]dioxin-4-yl)- tret dicaciteca- lytubretse

125971-95-1

Intermediate


134523-

00-5

Antihypertensive

7-[2-(4-flouro-phenyl)-5-isopropyl-3-phenyl-4-phentlcarbomyl-pyrrol-1-yl]-3,5 hydroxy-heptanoic acid-tert butyl

134395-00-9

Intermediate


134523-

00-5

Antihypertensive

27 Carvedilol 72956-09-3

API -- -- -- Antihypertansive

3-(Phenylhydrazino) cyclohexanone

27385-45-1

Intermediate

(n-3) Intermediate of Carvedilol

72956-

09-3

Antihypertansive

4-Oxo-1,2,3,4-tetrahydrocarbezole

15128-52-6

Intermediate


72956-

09-3

Antihypertansive

4-(2,3-Epoxypropoxy) carbazole

51997-51-4

Intermediate


72956-

09-3

Antihypertansive

28 Glimipride & it‘s intermediate

93479-97-1

API -- -- -- To treat type 2 diabetes

(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1(N—2-phenyl ethyl)-carboxamido]

N/A Intermediate

(n-2) Intermediate of Glimipride

93479-

97-1

To treat type 2 diabetes

4-[2-[(3-Ethyl-4-methyl-2-oxo-3-pyrrolin-1-yl) carboxamido] ethyl]benzene sulfonamide

119018-29-0

Intermediate

(n-1) Intermediate of Glimipride

93479-

97-1

To treat type 2 diabetes

29 Thiocolchicoside 602-41-5 API -- -- -- used as a muscle relaxan

30 Nimesulide & it‘s intermediate

51803-78-2

API -- -- -- anti-inflammatory drug

O- Phenoxy Nitrobenzene

2216-12-8

Intermediate

(n-3) Intermediate of Nimesulide

51803-78-2

anti-inflammatory drug

O- Phenoxy Aniline 2688-84-8

Intermediate


51803-78-2


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Page 69 of 232

O- Phenoxy Methane

N/A Intermediate


51803-78-2


31 Diclofenac Sodium & it‘s intermediate

15307-79-6

API -- -- -- Anti Flammatory

(2,6-DICHLORO PHENYLAMINE)

15307-93-4

Intermediate

(n-4) Intermediate of Diclofenac Sodium

15307-

79-6

Anti Flammatory

(N-CHLOROACETYL, 2,6-DICHLORO PHENYLAMINE)

15308-01-7

Intermediate


15307-

79-6

Anti Flammatory

(1-(2,6 -DICHLOROPHENYL) 2-INDOLINONE)

15362-40-0

Intermediate


15307-

79-6

Anti Flammatory

32 Albendazole 54965-21-8

API -- -- -- Anthelmintic

4-Thiocyno-2-Nitro- anilnemol

54029-45-7

Intermediate

(n-3) Intermediate of Albendazole

54965-

21-8

Anthelmintic

2-Nitro-4-propyl thio aniline

54393-89-4

Intermediate


54965-

21-8

Anthelmintic

1,2,diamine-5-propyl thio benznene

66608-52-4

Intermediate


54965-

21-8

Anthelmintic





Sr. no.

Particulars Details

A

A-1 Total cost of Proposed Project (Rs. in Crores):

3.90 crores

Break-Up of Project Cost

Particulars Proposed Amount

(Rs. in Crore)

Land Cost & It‘s Development 0.00

Civil Structure & Building 0.75

Plant & Machinery Cost 2.19

Environment protection measures (includes cost of ETP, Tree Plantation, etc.)

0.96

Total Project Cost 3.90

-

A-2 Details of Environmental Management Plan (EMP) As Below

Bifurcation of EMP Cost

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Page 70 of 232

Sr. No

Unit Installed Capacity

(KLD)

Capital Cost (Rs. In Lakhs )

Operating Cost

(Lacs/Year)

Maintenance Cost

(Lacs/Year)

Total Recurring

Cost (Lacs/Year)

1 Waste Water 30 KLD 11.0 291.60 -- 291.60

2 Air -- 27.50 -- 3.40 3.40


-- 9.0 108.91 -- 108.91

4 Fire & Safety -- 25.0 -- 3.00 3.00

5 AWH Monitoring

-- 1.0 -- 1.00 1.00


-- 3.46 -- 1.80 1.80

7 Occupational Health

-- 4.0 -- 2.35 2.35

8 Corporate Environment Responsibility

For Year 2021-2024 15.6 -- -- --

Total 96.56 400.51 11.55 412.06

Summary

Cost of Project in Crores per Annum: 3.90 Cr.

EMP Capital Cost in Crores per Annum and Percentage: 0.96 Cr. (24.61%)

EMP Recurring Cost in Crores per Annum and Percentage: 4.12 Cr

--

A-3 Details of CER (As per MoEF&CC OM dated 01/05/2018) As Below

As per OM no. 22-65/2017 on dated 01/05/2018 regarding ―Corporate Environment Responsibility‖ (CER), Greenfield projects have to contribute 2% (Rs. 7.80 Lack) of the Capital Investment (3.90 Cr). But as per New Mechanism of CPCB vide letter no CPCB/IPC-VII/CEPI/NGT/2019 on dated 25/10/2019, we shall commit to do 4% (Rs. 15.60 Lack) of Project Cost as a CER. Our CER activity are as below table…

Component As per Norms Allocation

CER Rs. 7.80 Lakhs (2 %) Rs. 15.6 Lakhs (4 %)

Activities to be carried out under CER:

CER Activities Fund (Rs.)

2021-2022

Provided Solar street light set with battery backup (18W -15 Nos.) in Kharod Village

4,50,000/-

2022-2023

To provide Sports Equipment and stationary in the primary schools of Bakrol Village.

1,60,000/-

Company provide R.O. Plant (2000 Liter) and drinking water storage tank in Bakrol village

4,00,000/-

2023-2024

Company will purchased instrument and renovation of Primary Health center in Bhadkodra Village

5,50,000/-

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Page 71 of 232

TOTAL 15,60,000 /-

-


B-1 Total Plot area ( sq. meter) 2883 Sq. m.


Sr. No.

Description Gr. Floor

Area Sq. Meter

First Floor B/U Area Sq. Meter

Second Floor B/U Area Sq. Meter

1 Production Building 100 100 100

2 Raw Material Storage Area 200 -- --

3 Finish Product Storage Area 50 -- --

4 Haz. Waste Storage Area 150 -- --

5 Boiler Area 80 -- --

6 ETP 50 -- --

7 Hydrogen Storage Area 20 -- --

8 Gas storage Area 20 -- --

9 Admin & OHC Room 50 50 50

10 Green Belt Area (40%) 1153 -- --

11 Road & Open Area 1000 -- --

12 Security Cabin 10 -- --

TOTAL 2883

Company have store 1056 MT material as per calculations, we require 405 MT storage of material. Hence company has adequate area for storage of the Raw Material / Haz. Chemicals, Hazardous waste and Product. --

B-3 Green belt area ( sq. meter)

1153 Sq. m. (40%)

C Employment generation Direct - 15 Employees Indirect - 10 Employees Total - 25 Employees

D Water

D-1 Source of Water Supply (GIDC Bore well, Surface water, Tanker supply etc...)

GIDC Water Supply

Status of permission from the concern authority. GIDC Water Supply vide letter no NAO/PNK/742 dated 16/09/2020


Category

Quantity KLD

Remarks

(D) Domestic 3.0

(E) Gardening 6.0

(F) Industrial

Process 12.4

Washing 5.0

Boiler 45.0

Cooling 30.0

Scrubber 2.4

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Other (R&D) 0.2


Total (A + B + C) 104.0

--

As per our proposed product profile manufacturing process and mass balance, worst case scenario for water consumption is (Product no- 20) (P-chloro benzhydryl piperazine ) (4.80) and (Product no- 27) (Carvedilol) (7.57).

Summary of water requirement Quantity

KLD Remarks

Total water requirement for the project (A) 104.0

Quantity to be recycled (B) 62.5

Total fresh water requirement (C) 41.5

Ensure Total water requirement = Fresh water + Recycled water (104.0 = 41.5 + 62.5)

Reuse/Recycle details (KLD) with feasibility. [Source of reuse & application area]

Source of waste water for reuse 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

2.5 KLD Domestic effluent

Gardening Purposed

BOD-30 --

In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. --


Category

Waste water KLD

Remarks

(A) Domestic 2.5

(B) Industrial

Process 14.3

Washing 5.0

Boiler 4.5

Cooling 3.0

Scrubber 3.2

Other (R&D) 0.2


Total (A + B) 32.7

-

Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative): As per our proposed product profile manufacturing process and mass balance, worst case scenario for waste water generation is (Product no- 22) (Thiophene-2-ethanol) (5.4) and(Product no- 27) (Carvedilol) (8.99)

Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (If any applicable to proposal).

Not Applicable


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Domestic: 2.5 KLD domestic effluent will be treated into STP and reused for gardening purposed

Industrial: 27.0 KLD Effluent from process and utility will be treated into primary ETP and primary treated effluent send to common MEE for the final treatment and disposal. 3.2 KLD Scrubbing media reuse in plant premises & Sell to end user who is having Rule-9 Permission.

-

D-5 Treatment facility within premises with capacity

For Domestic waste water: Capacity of STP – 3.0 KLD.

For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.

[In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. In-house ETP @ 30 KLD

Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.)

CHARACTERISTICS BEFORE & AFTER TREATEMENT OF EFFLUENT

Sr. No.

Parameter

Characteristics(mg/L)

Primary treated Process

Boiler blow down

Cooling Tower blow down

Washing Composite

1 pH 3-9 8 - 8.5 8 - 8.5 5.5 - 8.5 3-9 6.5-7.5

2 TDS 28000 350 250 1000 28000 28700

3 TSS 500 250 350 200 500 75

4 COD 20000 30 100 600 20000 13000

5 BOD3 700 10 30 200 700 490

--

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): Total proposed waste water generation from the industry will be 32.7 KLD (Ind. – 30.2 KLD + Dom. –2.5) Industrial:- 27.0 KLD Effluent from process and utility will be treated into primary ETP and primary

treated effluent send to common MEE for the final treatment and disposal. 3.2 KLD Scrubbing media reuse in plant premises & Sell to end user who is having

Rule-9 Permission. Domestic:- 2.5 KLD domestic effluent will be treated into STP and reused for gardening purposed.

D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc. Name of Common facility (CF) (For waste water treatment)

Common MEE Ms/ BEIL, Ankleshwer

Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line

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with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.

M/s. BEIL, Ankleshwar for Common MEE vide letter no BEIL/ANK/2020 dated 16/09/2020


E Air

E-1 Brief Note on fuel based heat energy requirement and worst case scenario thereof:

SR. NO.

NAME OF FUEL QUANTITY

1. Briquette of Bio Coal 13 MT/Day

2. HSD 50 Lit/hr

Power Requirements: Proposed: Power required from DGVCL is 1000 KVA. Standby power supply from D.G. set (500 KVA) in emergency case. --

E-2 Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)

-

SR. NO.

SOURCE OF EMISSION

WITH

STACK HEIGHT (METER)

TYPE OF FUEL

QUANTITY OF FUEL

TYPE OF EMISSIONS

I.E. AIR

AIR POLLUTION CONTROL

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CAPACITY POLLUTANTS MEASURES (APCM)

1

Boiler

(Cap. - 1.5

MT/hr & 4.0

MT/hr) 30 M

Briquette of Bio Coal

10 MT/Day

PM

SO2 NOx

Multicyclone Separator With

Bag Filter

2

Thermic Fluid Heater (Cap. - 1 Lakh Kcal/ Hr)

Briquette of Bio Coal

3 MT/Day

Multicyclone

Separator With

Bag Filter

3

D.G. Sets

(Stand by)

(Cap. – 500 KVA)

18 M HSD 50

Liter/hr

Adequate

Stack Height

-

E-3 Process gas emission details i.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)

-

Sr. No.

Stack Attached To Stack Height

Air Pollution Control System

Parameter

1 Process Vent -1 (Chlorination/Sulphonation) Product No. 23

11 M

Two stage Scrubber (Water +

Alkali)

HCl SO2

2 Process Vent -2 (Nitrification) Product No. 30

11 M Two stage Alkali

Scrubber NOx

3 Process Vent -3 Product No. 5,32

11 M Two stage Alkali

Scrubber HBr

4 Process Vent -4 (Ammonification) Product No. 27

11 M Two stage

water Scrubber

NH3

5 Process Vent -5 (Chlorination) Product No. 32

11 M Two stage

water Scrubber

Cl2

Note:

Details of gaseous raw materials used in proposed project – Hydrogen gas, Ammonia

gas and Chlorine gas are used

Estimation of process gas emission (Product wise and Total) – process gas emission

for chlorination & Sulphonation – Product No.- 23, process gas emission for

Nitrification – Product No.- 30, process gas emission for Bromination– Product No.-

5,32 process gas emission for Ammonification – Product No.- 27, process gas

emission for Chlorination– Product No.- 32.

Requirement of the scrubbing media (KL per Day) considering solubility (Product wise

and Total).

Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its

sound management in HW matrix. Complied

E-4 Fugitive emission details with its mitigation measures:

Following measures will be adopted to prevent and control fugitive emissions… Solid raw material charging will be done through closed system to avoid fugitive emissions. Airborne dust at all transfers operations/ points will be controlled either by spraying water or

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providing enclosures. Adequate ventilation will be provided. Periodic monitoring of work area will be carried out to check the fugitive emission. Minimum number of flanges, joints and valves in pipelines. Regular inspection of floating roof seals and proper preventive maintenance of roofs and

seals for tanks. 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 / bad filter.

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 waste management matrix (as per the Hazardous and Other Wastes (Management and Transboundary Movement) Rules 2016. Note:

Priorities for HW Management: Pre-processing, Co-Processing, Reuse/Recycle within premises, Sell out to actual users having Rule-9 permission, TSDF/CHWIH.

Quantification of hazardous waste shall be based on mass balance and calculations shall be incorporated in EMP details separately.



Sr. no.


Source of generation

Category and

Schedule as per HW

Rules.

Quantity (MT/Annum)

Disposal Method

1 ETP Sludge ETP SCH-I/35.3 90 Collection, Storage, Transportation and Disposal at common TSDF site.

2 Discarded Drums/Bags/ Liners

Raw Materials/ Products

SCH-I/33.1 35 Collection, Storage, Transportation, Decontamination & Sale to GPCB approved vendors/ reuse /send back to supplier.

3 Used/ Spent Oil Machineries/Utility

SCH-I/5.1 1.4 Collection, Storage, Disposal by reuse in plant machinery as lubricant or transportation & Sale to GPCB registered re-processor.

4 Distillation Residue

Distillation SCH-I/20.3 184 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.

5 Spent Solvent Process SCH-I/28.6 7311 Collections, Storage, distillation and reuse in

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plant premises.

6 Spent Carbon Process SCH-I/28.3 76 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.

7 Organic Residue Process SCH-I/28.1 159 Collection, Storage, Transportation and sent for co-processing in cement industries or (in case of non-operation of co-processing site) Disposal at common incineration site.

8 Inorganic residue Process SCH-I/28.1 58 Collection, Storage, Transportation and sent for co-processing in cement industries or Disposal at common TSDF Site .

9 Spent Catalyst Process SCH-I/28.1 25 Collection, Storage, reuse in the plant premises or Transportation and send to regenerator under Rule-9.

10 Iron Sludge Process (Product No. 30)

SCH-I/28.1 277 Collection, Storage, Transportation and sent for co-processing in cement industries (in case of non-operation of co-processing site) Disposal at common incineration site.

11 Aluminum chloride

Process (Product

No. 18,31)

SCH-I/28.1 1193 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.

14 Dilute HCl (28%) Process (Product No.- 25)

+ Scrubber (Product

No.- 23, 32)

SCH- II / B 15

10.70 +

468.3 = 479

Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 19 – 849 MT/Year)

15 Sodium bi sulphite (30%)

Scrubber SCH- II / B 15

82 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.

16 Sodium Nitrate Scrubber SCH-I/28.1 22 Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission

17 Sodium Bromide (25%)

Process (Product No.- 22)

+

SCH- II / B 15

492.12 +

516= 1009

Collection, Storage, Transportation and Sell to end user who is having Rule-9 Permission.

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-

Scrubber (Product

No.- 5,32)

18 Liq. Ammonia (25%)

Scrubber SCH- II / B 15

159 Collection, Storage and reuse in plant premises. (Requirement of HCL in Product No. 13 – 593.16 MT/Year)

19 Off Specification Products

From mfg. Process (Batch failure)

SCH-I/28.4 10 Collection, Storage, Transportation and sent for co-processing in cement industries (in case of non-operation of co-processing site) Disposal at common incineration site.

R&D

20 ETP Sludge ETP 35.3 3.0 Collection, Storage, Transportation & disposal in TSDF.

21 Residue from Distillation/ Organic Process Waste

R&D 28.1 4.0 Collection, Storage, Transportation & send to cement industries for co-processing or incineration in CHWIF.

22 Discarded Drum Raw Materials/Pr

oducts

33.1 20 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.

23 Discarded Bags / Liner

Raw Materials/Pr

oducts

33.1 0.2 Collection, Storage, Transportation & Sell to GPCB authorized Vendor.

24 Off Specification Products

R&D 28.4 1.0 Collection, Storage, Transportation & send for co-processing or incineration in CHWIF.

F-2 Membership details of TSDF, CHWIF etc. (For HW management)

Company is obtain the provisional membership of TSDF & CHWIF

Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Ankleshwar for Common TSDF & CHWIF vide letter no BEIL/ANK/2020 dated 16/09/2020

F-3 Details of Non-Hazardous waste & its disposal (MSW and others)

Not Applicable


G-1 Types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc. (Details in Table Format)

SOLVENT RECOVERY AFTER LDAR

Sr. No.

Type of Solvent

% Recovery

% Losses

Air Water Haz

1 Methanol 96.4 0.86 1.84 0.90

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2 Cyclohexane 96.0 0.93 2.07 1.00

3 Methylne Dichloride 96.3 0.89 1.96 0.95

4 Ethyl Acetate 96.4 0.91 1.79 0.90

5 Dimethyl Formamide 96.5 0.76 1.87 0.87

6 Ethylene Dichloride 96.3 0.97 1.81 0.92

7 Acetone 96.4 0.88 1.82 0.90

8 Toluene 96.3 0.94 1.84 0.92

Justification of Reuse of solvent

Name of Solvent Total requirement

MT/Month

Total quantity of solvent recovered MT/Month

Methanol 95.06 91.63

Cyclohexane 37.40 35.89

Methylne Dichloride 64.00 61.6

Ethyl Acetate 44.00 42.41

Dimethyl Formamide 24.00 23.15

Ethylene Dichloride 210.00 202.26

Acetone 30.00 28.92

Toluene 260.00 250.32

--


Company will be installed double mechanical seal and MSW Gaskets in solvent pipelines to prevent leakage from flanges

Company will be reduced the joints and valves in pipelines. All the rotating equipment like pumps will be installed with double Mechanical Seals to arrest

any sort of emissions. Flanges will be sealed so less losses will be there. Down the Temperature of Cooling tower to 5 0C Chilled Brine at -10 0C will be used to trap any traces of Solvent which is slipped from

Secondary condenser. Closed loop system. For continue vapor travelling 100mm of Hg (slight vacuum) will be applied on secondary

condenser. --

G-3 VOC emission sources and its mitigation measures (Brief note on LDAR)

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

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

To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at all solvent pumps.

Stand by pumps will be provided on all scrubbers. Besides, scrubbers will be equipped with on-line pH meter with hotter system for better operational control.

Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers.

All the raw materials will be pneumatically transfer to the reactor. Emphasis will be given to solvent management/solvent loss prevention. Control by having proper scrubbing system. Condenser to trap VOC. Proper gland packing will be maintained for pumps and valves and to the extent possible

pumps with mechanical seal.

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H Safety Detail

H-1 Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)

Details regarding storage of Hazardous chemicals

Storage details Name of major Hazardous chemicals Remarks

Storage tanks -- --

Drum/Barrel storage

All Other Raw material storage into Drum & Bags only like Methylene Dichloride, Acetic acid, Hydrochloric acid, Sulphuric acid.

Bottles --

Cylinder Ammonia gas, Hydrogen gas & Chlorine gas

Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.

FLP type light fittings will be provided. Proper ventilation will be provided in Godown. Proper label and identification board /stickers will be provided in the storage area. Conductive drum pallets will be provided. Drum handling trolley / stackers/fork lift will be used for drum handling. Separate dispensing room with local exhaust and static earthing provision will be made. Materials will be stored as per its compatibility study and separate area will be made for

flammable, corrosive and toxic chemical drums storage. Smoking and other spark, flame generating item will be banned from the Gate.



Safety measures

Sulfuric Acid Milk of magnesia

Hydrochloric Acid Milk of Magnesia, Drink Large Quantity of Water

Acetic Acid Milk of magnesia

Methanol In case of acidosis give Sodium Bicarbonate. In case of delirium give Diazepam 10 mg. by intravenous injection.

Acetonitrile Hydroxocobalamin or the cynide antidote kit

Applicability of PESO : Company will apply for PESO after getting EC if applicable

H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)

Type of Process Safety measures including Automation

Hydrogenation Installed DCS Systeam FLP type area will be provided. Total enclosed process system. Instrument & Plant Air System. Nitrogen blanketing in Hydrogenation reactor. Safety valve and Rupture disc provided on reactor. Cooling Chilling and power alternative arrangement have been

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made on reactor. Hydrogen and Nitrogen Cylinder bank away from the auto clave

reactor. PRV station with shut off valve, safety valve provision will be

made for hydrogenation reaction safety. Before Hydrogen Gas charging in to reactor and after completion

of reaction Nitrogen flushing will be done. Flame arrestor will be provided on vent line of reactor and it will

be extended up to roof level. Open well ventilated and fragile roofs will be provided to on

reactor. Safe Catalyst charging method will be adopted. SOP will be prepared and operators will be trained for the same. Static earthing and electric earthing (Double) provided. Reactor vent extended outside the process area and flame

arrestor provided on vent line. Dumping vessel arrangement will be made. Dumpers for static earthing on pipeline flanges of flammable

chemical will be provided.

Ammonia Valve, pipeline will be checked and maintain, in good condition. All Gaskets will be checked periodically & if new one replaces

found defective. Joints will be checked regularly to found any Leakage. ADEQUATE PPE will be kept to handle the Hazard. ISI Portable fire extinguisher & Hydrant line will be provided as

per TAC norms. Sufficient amount of sand/soil are kept to control any spillage. Flame proof fitting provided. Eye washer cum shower will be provided near tank-farm area. Spark arrester will be installed on all vehicles inside the premises. SBA set, Canister mask and airline mask will be provided. Earthing& bonding on tanks will be provided. Vent line dipped in water will be provided.

Chlorination Chlorine Hood with blower will be provided with scrubbing arrangement.

Chlorine absorption system will be provided. In case of chlorine leakage in chlorine shed it will be suck through blower and it will be scrubbed in Caustic scrubber.

Safety Shower and eye wash will be provided in Chlorine shed area.

Emergency siren will be provided. First Aid Boxes and Occupational health centre will be made at

site. Chlorine cylinders will be stored in cylinder storage area. Safety Valve and pressure gauge will be provided on reactor. All emergency valves and switches and emergency handling

facilities will be easily assessable. All the vessels and equipments will be earthed appropriately and

protected against Static Electricity. Materials will be transferred by pumping through pipeline or by

vacuum Flame proof light fittings will be installed in the plant. All the Plant Personnel will be provided with PPE All employees will be given and updated in Safety aspects

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through periodic training in safety

Nitration The Reactor will have Temperature control system cascaded with cooling water system consisting of Cooling tower, pumps and circulating system. In case of high temperature the steam will get cut off and cooling water will start circulating through the reactor coils. Alternately Chilled water system is also provided for extreme emergencies.

The Reactor will have rupture disc and safety valves which will take care of excess pressure and the outlet of which is connected to the scrubbers.

The Reactor will also have a separate high local vent with pressure relief valve which is connected to a catch pot with water. The catch pot contents will be separated for recycle purpose. This will be additional safety, if 1 & 2 fail at the same time, which is unlikely.

In case of contact with eyes, immediately flush eyes with plenty of water for at least 15 minutes. Cold water may be used. Get medical attention immediately.

In case of contact with skin, immediately flush skin with plenty of water for at least 15 minutes while removing contaminated clothing and shoes. Cover the irritated skin with an emollient. Cold water may be used. Wash clothing before reuse. Thoroughly clean shoes before reuse. Get medical attention immediately.

Wash with a disinfectant soap and cover the contaminated skin with an anti-bacterial cream. Get medical attention.

If inhaled, remove to fresh air. If not breathing, give artificial respiration. If breathing is difficult, give oxygen. Get medical attention immediately.

Evacuate the victim to a safe area as soon as possible.

--


Total Plot Area: 2883

Area utilized for plant activity: 300

Area utilized for Hazardous Chemicals Storage: 440

Number of Floors: G+2

Water requirement for firefighting in KL/hr: 3.51

Water storage tank provided for firefighting in KL 200

Details of Hydrant Pumps: One Fire pump, One diesel driven pump and one Jockey pump are being implemented.

Nearest Fire Station : Panoli GIDC – 2.25 Km

Applicability of Off Site Emergency Plan: N.A

-

H-4 Details of Fire NOC/Certificate: Company will apply for Fire NOC/Certificate after getting EC if applicable


-



Area provided for OHC: 15 Sq. Meter provided in Ground Floor at Admin Building

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Nearest General Hospital : Welcare hospital – 0.8 KM

Name of Antidotes to be store in plant :

--



Project proponent (PP) and Technical expert of PP, M/s. Ozone Enviro tech remains present during


This is new proposal of API and Its Intermediates plant at GIDC, Panoli. Source of water supply is GIDC.

Committee noted that proposed plot is taken over by PP on rental basis from plot owner namely, M/s

Baid Export Pvt. Ltd., which is textile unit. Upon asking, PP informed that original plot holder has done

sub-plotting and sub-plot was taken over as rent basis. PP could not furnish documents regarding the

NOC of GIDC for sub plotting of original plot and plot allotment letter mentioning purpose of the original

Plot.

After detailed discussion, Committee unanimously decided to defer the project and consider the

project only after submission of following documents,

1. Documents regarding the NOC of GIDC for sub plotting of original plot.

2. Plot allotment letter mentioning purpose of the original Plot.

4. SIA/GJ/IND2/164606/2020 M/s. Aalidhra Pharmachem Pvt. Ltd.

Plot No: C-289,289/1, GIDC Saykha, Ta-

Vagra, Dist: Bharuch

Appraisal


Project status: New






This is a new unit proposes for manufacturing of synthetic organic chemicals [API and API

Intermediates] as tabulated below,

Sr. No.

Product Name CAS No. MT/ Month End Use

1 Fenofibrate 49562-28-9 22.0 to help Lower "bad" cholesterol and fats

2 Fexofenadine 83799-24-0 an antihistamine

3 Deferasirox 201530-41-8 to treat iron overload

4 Montelukast sodium 151767-02-1 to prevent and manage asthma symptoms

5 Nebivolol 99200-09-6 to treat high blood pressure

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6 Pregabalin 148553-50-8 20.0 an antidepressant

7 Derifenacin 133099-04-4 to treat an overactive bladder

8 Febuxostat 144060-53-7 to treat hyperuricemia

9 Linezolid 165800-03-3 antibiotic

10 Dabigatran 211915-06-9 anticoagulant

11 Metoprolol succinate 98418-47-4 18.0 to treat angina and hypertension

12 Metoprolol Tartrate 37350-58-6 to treat high blood pressure

13 Rivarixaroban 366789-02-8 to treat or prevent blood clots

14 Etoricoxib 202409-33-4 To treat eases pain and swelling

15 Olmesartan 144689-63-4 15.0 to treat high blood pressure

16 Telmisartan 144701-48-4 to treat high blood pressure

17 Brexpiprazole 913611-97-9 an antipsychotic medication

18 Macitentan 441798-33-0 to treat high blood pressure

19 Teneligliptin 760937-92-6 12.0 to treatment of type 2 diabetes mellitus

20 Vildagliptin 274901-16 to treatment of type 2 diabetes

21 Alogliptin 850649-62-6 to treatment of type 2 diabetes

22 Sitagliptin 486460-32-6 to treatment of type 2 diabetes

23 Duloxetine Hydrochloride 136434-34-9 10.0 to treat depression and anxiety

24 Selexipag 475086-01-2 to treat high blood pressure

25 Apixaban 503612-47-3 to prevent serious blood clots from forming due to a certain irregular heartbeat

26 Ticagrelor 274693-27-5 to treat angina and hypertension

27 Atorvastatin calcium 134523-00-5 9.0 to help Lower "bad" cholesterol and fats

28 Rosuvastatin calcium 147098-20-2 to help Lower "bad" cholesterol and fats

29 Bosentan 147536-97-8 to treat pulmonary arterial hypertension

30 Lurasidone Hydrochloride 367514-88-3 to treat certain mental/mood disorders

31 Nintedanib 656247-17-5 5.0 To treatment of idiopathic pulmonary fibrosis

32 Imatinib 152459-95-5 to treat certain types of cancer

33 Gefitinib 184475-35-2 to treat lung cancer

34 Ibrutinib 936563-96-1 to treat certain cancers

35 Apremilast 608141-41-9 3.0 to treat a certain type of skin condition

36 Vilazodone 163521-08-2 to treat depression

37 Brivaracetam 357336-20-0 anti-epileptic drug anticonvulsant

38 Erlotinib 183321-74-6 Cancer medicine

39 Lacosamide 175481-36-4 anti-epileptic drug

R & D -- 0.5 --

TOTAL 114.5 MT/Month

ENDUSE OF PRODUCTS

Sr. No.


CAS no. Type/ Category of Product (API/


Name of API in which Intermedia

CAS no. (API)

Said API is used for/End Use of said API

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Intermediate)

te Used/ End use of said Intermediate

1 Fenofibrate 49562-28-9 API -- -- -- to help Lower "bad" cholesterol and fats

2 Fexofenadine 83799-24-0 API -- -- -- an antihistamine

3 Deferasirox 201530-41-8

API -- -- -- to treat iron overload

4 Montelukast sodium

151767-02-1

API -- -- -- to prevent and manage asthma symptoms

5 Nebivolol 99200-09-6 API -- -- -- to treat high blood pressure

6 Pregabalin

148553-50-8

API -- -- -- an antidepressant

7

Derifenacin

133099-04-4

API -- -- -- to treat an overactive bladder

8 Febuxostat 144060-53-7

API -- -- -- to treat hyperuricemia

9 Linezolid 165800-03-3

API -- -- -- antibiotic

10 Dabigatran 211915-06-9

API -- -- -- anticoagulant

11 Metoprolol succinate

98418-47-4 API -- -- -- to treat angina and hypertension

12 Metoprolol Tartrate

37350-58-6 API -- -- -- to treat high blood pressure

13 Rivarixaroban 366789-02-8

API -- -- -- to treat or prevent blood clots

14 Etoricoxib 202409-33-4

API -- -- -- To treat eases pain and swelling

15 Olmesartan 144689-63-4

API -- -- -- to treat high blood pressure

16 Telmisartan 144701-48-4


17 Brexpiprazole 913611-97-9

API -- -- -- an antipsychotic medication

18 Macitentan 441798-33-0


19 Teneligliptin 760937-92-6

API -- -- -- to treatment of type 2 diabetes mellitus

20 Vildagliptin 274901-16 API -- -- -- to treatment of type

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2 diabetes

21 Alogliptin 850649-62-6

API -- -- -- to treatment of type 2 diabetes

22 Sitagliptin 486460-32-6

API -- -- -- to treatment of type 2 diabetes

23 Duloxetine Hydrochloride

136434-34-9

API -- -- -- to treat depression and anxiety

24 Selexipag 475086-01-2


25 Apixaban 503612-47-3

API -- -- -- to prevent serious blood clots from forming due to a certain irregular heartbeat

26 Ticagrelor 274693-27-5

API -- -- -- to treat angina and hypertension

27 Atorvastatin calcium

134523-00-5

API -- -- -- to help Lower "bad" cholesterol and fats

28 Rosuvastatin calcium

147098-20-2

API -- -- -- to help Lower "bad" cholesterol and fats

29 Bosentan 147536-97-8

API -- -- -- to treat pulmonary arterial hypertension

30 Lurasidone Hydrochloride

367514-88-3

API -- -- -- to treat certain mental/mood disorders

31 Nintedanib 656247-17-5

API -- -- -- To treatment of idiopathic pulmonary fibrosis

32 Imatinib 152459-95-5

API -- -- -- to treat certain types of cancer

33 Gefitinib 184475-35-2

API -- -- -- to treat lung cancer

34 Ibrutinib 936563-96-1

API -- -- -- to treat certain cancers

35 Apremilast 608141-41-9

API -- -- -- to treat a certain type of skin condition

36 Vilazodone 163521-08-2

API -- -- -- to treat depression

37 Brivaracetam 357336-20-0

API -- -- -- anti-epileptic drug anticonvulsant

38 Erlotinib 183321-74-6

API -- -- -- Cancer medicine

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39 Lacosamide 175481-36-4

API -- -- -- anti-epileptic drug







Total Project

10.0 Crores


Details Project Cost (Rs. In Crores)

Land 1.0

Building 2.0

Machinery 3.0


Environment Issue/ Component

Remedial Measures

Component Capital Cost of EMP

Recurring Cost of EMP /Year

Hazardous waste generation & disposal

Proper collection, Safe Handling, Storage within premises and disposal of waste at approved TSDF, incineration facility, re-cyclers, re-processors.

Cost of TSDF/CHWIF site membership letter

Rs. 2,00,000/- --

Construction of Hazardous waste storage yard

Rs. 10,00,000/- --

Cost for TSDF disposal

-- Rs. 1,88,24,000/-

Cost for incineration disposal

-- Rs. 12,65,40,000/-

Effluent generation and treatment

ETP Construction Construction cost of ETP, STP

Rs. 1,50,00,000/- Rs. 2,00,000/-

--

Treatment cost of effluent/ year

-- Rs. 3,24,00,000/-

Rs. 10,51,20,000/-

Common MEE Membership

Rs. 1,00,000 --

STP Plant Rs. 3,50,000/- Rs. 25,000/-

Details of Air Adequate Cost of stack Rs. 10,00,000 --

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Emission pollution control system will be provided for control of gaseous emission. Adequate stack height for better dispersion of pollutants

installation of Stack

Cost of scrubber Rs. 4,50,000 --

Cost of MCS with bag filter

Rs. 7,00,000 --

Cost of LDAR With DSC in

Solvent Distillation

Rs.10,00,000 Rs. 25,000/- per year

Cost of

maintenance of APCM System

-- Rs. 1,50,000/- per year

Plantation 40 % of the plant area will be developed as greenbelt.

Cost of tree plantation

Rs. 40,95,000/- --

Cost of

maintenance -- Rs. 60,000/-

Monitoring of Environmental parameters

Regular monitoring of various environmental parameters will be carried out to check the effectiveness of the control system.

Cost of monitoring of various environmental parameters In-house COD, BOD, NH3-N, Instruments lab Set up. Third Party Monitoring

Rs. 15,00,000/- Rs. 1,50,000/-

Occupational Health and safety precaution

First aid box, Fire Fighting system, Periodical medical Check-up of employees, doctor‘s visit to the unit, insurance policy of the employees

Cost of PPE & Antidote 5 Beds, Oxygen Cylinder, Antidote, etc. (OHC)

Rs. 3,00,000/- Rs.30,000/-

Imparting safety training to employees every 6 months

-- Rs. 40,000/-

Medical examination of employees

-- Rs. 80,000/-

Cost of firefighting equipment's

Rs. 15,00,000/- Rs. 1,00,000/-

Cost of Fire Hydrant

Rs. 51,80,565 Rs. 5,00,000/-

Safety measures for Hazardous Operation- like Nitration, Ammoniation, i.e. Rupture disc, safety valve, alternate cooling

Rs. 18,00,000/- Rs. 1,00,000/-

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arrangement with DCS System

Safety measures for hydrogenation, & bromination i.e. DCS, O2 detector, auto damping system,

Rs. 10,00,000/- Rs. 1,00,000 per

year

Safety measures for Ammonia i.e. HCL torch detector, auto damping system with DCS System

Rs. 9 Lakhs Rs. 1,00,000 per

year

Trees Plantation and Provide Tree Protection Cage at Nearest Village Sayakaha & Vahiyal 260.0 Nos. of Trees

Rs.4,00,000/- --

To Provide Solar Lamps And Lights to Nearest School, Kothia, Pipaliya Village, Total No. 50

Rs.5,00,000/- --

Water Purifier System in Village (RO), Village: Bhersam, Chilad

Rs.5,00,000/- --

Setting up solar system in Sayakha village.

Rs.6,00,000/- --

Total Rs.

4,04,25,30565/- Rs.

28,43,44,000/-

Summary

Cost of Project in Crores 10.0 Crore

EMP Capital Cost in Crores per Annum and Percentage:

4.0 Crore

EMP Recurring Cost in Crores per Annum and Percentage:

28.43 Crore

A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide 31.10.2019.)

% as per the OM

Rs. in Crores

2 % 20.0 Lakh

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Brief note on proposed activities: As per OM no. 22-65/2017 on dated 01/05/2018 regarding ―Corporate Environment Responsibility‖ (CER), Expansion projects have to contribute 2% of the Additional Capital Investment, the company will contribute Rs 10.0 Lakhs as funds for CER activities Activities to be carried out under CER: Education,

Health, Environment Agriculture

B Land / Plot ownership details: Plot Allotment letter

B-1 Plot area

Total Plot area 33,168.00

10925.77 Sq. m. Green Belt


B-3 Green belt area

Total (Sq. meter)

Area in Sq. meter

10945.44 Sq. m.

% of total area

(33%)


Total

Direct:25 Indirect:25

D WATER

D-1

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

Status of permission from the concern authority. Permission Granted

D-2


Category

Quantity KLD

Remarks

(G) Domestic 15.0

(H) Gardening

12.0

(I) Industrial

Process 130.0

Washing 12.0

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Boiler 50.0

Cooling 50.0

Scrubber/Others 3.5


Grand Total (A+B+C)

272.5


Group:1 Product No: 01: Fenofibrate: 17.7 KLD Group:2 Product No: 06: Pregabalin: 28.37 KLD Group:3 Product No: 11: Metoprolol succinate: 13.29 KLD Group:4 Product No: 17: Brexpiprazole: 24.8 KLD Group:5 Product No: 19: Teneligliptin: 7.0 KLD Group:6 Product No: 23: Duloxetine Hydrochloride: 18.38

KLD Group:7 Product No: 29: Bosentan: 9.0 KLD Group:8 Product No: 34: Ibrutinib: 4.8 KLD Group:9 Product No: 36: Vilazodone: 7.29 KLD

-

Summary of water requirement

Quantity KLD

Remarks

Total water requirement for the project (A)

272.5

Quantity to be recycled (B)

59.0 KLD

Total fresh water requirement (C)

213.5

Ensure Total water requirement = Fresh water + Recycled water i.e. A = B + C






STP Water Gardening pH: 7.0 COD: <50.0 BOD: <30.0

--

Boiler Condensate Cooling pH: 7.0 COD: <50.0 BOD: <30.0

--

In case of no reuse/recycle of waste water, Give brief

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note on justification as why no reuse/recycle.


Category Waste water

KLD Remarks

(C) Domestic 12.0

STP Plant

(D) Industrial

Process 160.0

Washing 12.0

Boiler 1.5

Cooling 1.5

Scrubber/Others 4.58

Total Industrial

waste water

179.58

Total [A + B] 191.58

Brief Note on worst case scenario for waste water generation (Qualitative and Quantitative):

Group:1 Product No: 02: Fexofenadine: 18.2 KLD Group:2 Product No: 06: Pregabalin: 21.59 KLD Group:3 Product No: 14: Etoricoxib: 18.46 KLD Group:4 Product No: 15: Olmesartan: 21.5 KLD Group:5 Product No: 19: Teneligliptin: 27.41 KLD Group:6 Product No: 23: Duloxetine Hydrochloride: 17.13 KLD Group:7 Product No: 28: Rosuvastatin calcium:11.95 KLD Group:8 Product No: 32: Imatinib: 6.70 KLD Group:9 Product No: 38: Erlotinib: 17.4 KLD

Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (Whichever is applicable).


-

Domestic: Domestic waste water (12.0 m3/day) will be Treated In STP Plant and Reuse in Gardening

Industrial: Total water requirement will be 272.5 m3/day which will be met through GIDC water supply. The wastewater generation will be 191.58 m3/day. (Industrial: 179.58 KLD + Domestic: 12.0 KLD) 145.0 KLD Low COD/TDS Stream will be in Stream: 1 ETP:1 with Primary, Secondary Treatment and send to CETP of Saykha For final treatment and disposal. 30.0 KLD High COD/TDS Stream:2 will be treated in ETP:2 With Primary

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Treatment and send to Common MEE. Scrubbing media will be reuse in plant premises or send to end users having rule-9 permission.

- Clearly mention about final disposal


For Domestic waste water: Capacity of STP: 12.0 KLD

For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed. DETAILS OF EFFLUENT TREATMENT PLANT Stream I (Low COD & TDS Stream) First all non-toxic and biodegradable streams (low & medium COD & TDS) 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 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. 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

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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) 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. EXPECTED CHARACTERISTICS OF WASTEWATER BEFORE & AFTER TREATMENT EXPECTED CHARACTERISTICS OF WASTEWATER: LOW COD STREAM

Sr. No.

Category of Wastewater

Untreated Primary Treated

Secondary Treated

Tertiary Treatment

CETP Norms

1 pH 4.5-8.5 6.5-7.5 6.5-7.5 6.5-7.5 6.5-7.5

2 COD (mg/L) 5000 3600 1600 1450 3000

3 BOD3 (mg/L) 1600 1100 500 400 1000

4 TDS (mg/L) 4000 4500 4500 4100 8000

5 NH3-N (mg/L)

30 30 30 30 50

High COD & TDS stream

Sr. No. Category of Wastewater Before Treatment After Treatment

1 pH 3.5 - 8.5 6.5 - 7.5

2 COD (mg/L) 28000 22000

3 BOD3 (mg/L) 9000 7000

4 TDS (mg/L) 33000 36000


CETP of Sayakha.

Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Total water requirement will be 272.5 m3/day which will be met through GIDC water supply. The wastewater generation will be 191.58 m3/day. (Industrial: 179.58 KLD + Domestic: 12.0 KLD) 145.0 KLD Low COD/TDS Stream will be in Stream: 1 ETP:1 with Primary, Secondary

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Treatment and send to CETP of Saykha For final treatment and disposal. 30.0 KLD High COD/TDS Stream:2 will be treated in ETP:2 With Primary Treatment and send to Common MEE. Scrubbing media will be reuse in plant premises or send to end users having rule-9 permission.


Common MEE of M/s. BEIL

Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member unitsin-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.

CETP of Sayakha


E AIR

E-1 Brief Note on fuel based Heat energy requirement and worst case scenario thereof:


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DETAILS OF FLUE GAS

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 (5.0TPH)

30 m Briquettes of Bio-Coal

12.5 MT/Day

PM<150 mg/Nm3 SO2< 100 ppm NOx< 50 ppm

Multi-Cyclone Separator with bag filter With water scrubber

2 TFH (8 lakh kcal/hr.)

30 m Briquettes of Bio-Coal

14.0 MT/Day

Multi-Cyclone Separator with bag filter With water scrubber

3 D.G. Set (500 KVA)

11 m HSD 2500 lit/Day

Adequate height Provided

E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOx etc.)

-

DETAILS OF PROCESS GAS EMISSION

Sr. no.

Specific Source of emission (Name of the Product & Process)

Type of emission

Stack/Vent Height (meter)


1 Process Vent*-1 product no.06,21

HCl < 20 mg/Nm3 SO2<40.0 mg/Nm3

11m Two Stage Water + Alkali Scrubber

2 Process Vent*-2 Product No.18,29

NH3 < 175.0 mg/Nm3

11m Two Stage Water Scrubber

3 process vent-3 Product No.7,13,

HBr < 30.0 mg/Nm3

11 m Two Stage Water Scrubber

Note: Details of gaseous raw materials used in proposed project Estimation of process gas emission (Product wise and Total) Requirement of the scrubbing media (KL per Day) considering solubility (Product wise

and Total) Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its

sound management in HW matrix.

Sr. No.

Emissions

Assumed Quantity of Gaseous

Emissions (MT/Day)

Water required to

scrub pollutants (KL/Day)

% of solution Quantity of bleed

liquors (KL/Day)

1 HCl SO2

0.48 0.24

1.14 NaOH: 0.72

Dil. HCL (30 %) Sodium Sulphite

soln.

1.62 0.96

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(25 %)

2 NH3 0.20 0.89 Ammonia soln. (15-20 %)

1.09

3 HBR 0.25 0.75 Hbr Solution (25 %)

1.0

Total 3.5 KL/Day 4.58 KL/Day


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





-

Sr. no.




Quantity (MT/Annum)

Management of HW

1 ETP Sludge

ETP Sch-I /35.3 502.0 MT/Annum

Collection, Storage, Transportation and dispose to TSDF site.

2 Discarded Drums /Containers

Raw material Sch-I/33.1 100.00 MT/Annum

Collection, Storage, Transportation, Decontamination & Disposal by selling to

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3 Discarded Liner/Bag

Raw material Sch-I/33.1 12.00 MT/Annum

registered recycler

4 Used Oil

Plant Machinery Sch-I/5.1 6.00 MT/Annum

Collection, Storage, Transportation, Disposal by selling to registered recycler or re-use as lubricant

5 Spent Sulphuric Acid

From Mfg. Of Sch-I/28.1 (II-B-B15)

1962.0 MT/Annum

Collection, Storage, Transportation and sell to end user

6 Spent Carbon

From mfg. process

Sch-I/28.3 194.0 MT/Annum

Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site.

7 Spent Catalyst

From mfg. process


Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site.

8 Spent Solvents

From mfg. Process

Sch-I/28.6 16800.00 MT/Annum

Collection, Storage, recovered through in house distillation or sent for distillation job work to authorized recycler then reuse in process


From Solvent recovery plan


Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site

10 Organic Waste

From process of Sch-I/28.1 7718.0 MT/Annum

Collection, Storage, Transportation and dispose to co-processing in cement industries or common incineration Site

11 Inorganic waste

From process Sch-I/28.1 8910.0 MT/Annum

Collection, Storage, Transportation and dispose to TSDF site.

12 Sodium Sulphate

From mfg. process


Collection, Storage, Transportation And send to end user having rule-9 permission.

13 HCl (30%) From Scrubber Sch-I/28.1 535.0 MT/Year

Collection, Storage, Transportation And send to end user having rule-9 permission.

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14 Sodium Sulfite

Solution (25%)

From Scrubber Sch-I/28.1 317.0 MT/Year

Collection, Storage, Transportation & sell to end user having Rule-9 Permission.

15 Liq. Ammonia (15-20%)



16 HBr Solution (25%)






Sr. no.



Quantity (MT/Annum)


1

2 Fly Ash

From APCM

440 MT/Annum Collection, Storage, Transportation & send to brick manufacturer

3


G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.

All the solvents shall be directly distilled from product mixes and; if required shall be purified in packed column with the help of reflux and therefore there is no generation of any distillation residue from the solvent distillation.

The solvent distillation system shall be designed so as to achieve minimum 96.0 % recovery of solvent.

Pure solvent, crude solvent and distilled (recovered) solvent shall be stored only in storage tanks and we shall not be using drums at any stage in the Solvent Management System.

Wherever required, the solvents shall be directly pumped into day tanks from the storage tanks and shall be charged into the reactors without involving any manual handling.

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

All necessary fire fighting systems shall be provided with alarm system. Flame proof wiring and flame proof electrical accessories shall be provided to avoid any mishap.

All the storage tank and day tank shall be connected to a vent system through cooling water and chilled brine condensers to prevent loss of solvents in the atmosphere.

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

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condensers for maximum possible recovery of the solvents.

All the vents will be connected to a common carbon Adsorber for removing traces of solvent from vent gases.

Residue generated from the distillation will be incinerated in-house or sent to BEIL incinerator site.

Coolant to be used Primary Condensers Cooling Water Secondary Condensers Chilled Brine up to -5

0C


LEAK DETECTION AND REPAIR (LDAR) To prevent losses of these solvents in atmosphere, following infrastructure shall be used in

addition to LDAR program: Leak Free Pumps for transfer of solvents MSW Gaskets in solvent pipelines to prevent leakage from flanges Minimum number of flanges, joints and valves in pipelines. Down the Temperature of Cooling tower to -5

0C.

Chilled Brine at -15 0C will be used to trap any traces of Solvent which is slipped from

Secondary condenser. For continue vapor travelling 100mm of Hg (slight vacuum) will be applied on secondary

condenser. To eliminate chances of leakages from glands of pumps, mechanical seal will be provided at

all solvent pumps. All the rotating equipments like pumps will be installed with Mechanical Seals to arrest any

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

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

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

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

Flanges will be sealed so less losses will be there.

IMMEDIATE REPAIR OF DEVICES IN CASE OF LEAKAGES A regular preventive maintenance schedule will be in place to replace or rectify all gaskets

and joints etc to ensure no fugitive emissions shall take place. Plant shall also maintain adequate number of spares and consumables required to repair the

leaking device Plant shall also have competent contractor team to handle Leakages and can repair the same

immediately Standby equipments like Pumps, valves etc shall be kept basis the criticality and usage Plant shall also have access equipments like Boom lift to handle leakages at height

immediately

MONITORING OF SOLVENT LOSSES In warding, storage and consumption of solvents in various products shall be measured

through Level Transmitters and Load cells weighing systems resp. The quantity at each stage shall be reconciled periodically to arrive at Losses.

Periodic monitoring of work area will be carried out to check the fugitive emission. VOC detectors will be installed at various places to detect leak.

PREVENTIVE MAINTENANCE TO PREVENT LEAKAGES In order to prevent leakage from Pump, Seals, Valves etc, preventive maintenance shall be

carried out periodically as per plan. Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to prevent leakages and thus minimizing the fugitive emissions of VOCs.

Sr. No. Component Preventive Maintenance schedule

1 Pump seals with visible liquid dripping

Daily

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2 Valves/flanges Quarterly

3 Compressor seals Quarterly

4 Pressure relief devices Yearly

5 Pipeline Thickness Testing Yearly


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

Solid raw material charging will be done through closed system.

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

Close feeding system will be provided for centrifuges. Centrifuge and filtrate tank vents will be connected to vent chillers.

Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area, will be collected through hoods and ducts by induced draft and controlled by scrubber/dust collector.

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

Control by having proper scrubbing system.

Condenser to trap VOC.

Enclosures to chemical storage area, collection of emission from loading of raw materials in particular solvents through hoods and ducts by induced draft, and control by scrubber/dust collector to be ensured.

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 spraying water or providing enclosures.

Breather valves will be provided on solvent tanks.

H SAFETY details


- Brief note on storage of Hazardous chemicals in Tanks

All chemical store in Drums


All chemical store in Drums


Sr. No. Name Of Hazardous Substance

Control Measures Provided

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1 Sulphuric Acid 1. Store in a cool, dry, ventilated storage area with acid resistant floors and good drainage. Protect from physical damage. Keep out of direct sunlight and away from heat, water, and incompatible materials. Do not wash out container and use it for other purposes.

2 Caustic Lye 1. Store at ambient temperatures with venting open. Protect containers against physical damage and water.

2. Handling should occur in a chemical fume hood.

3 35 % Hydrochloric Acid

1. Safeguard containers against mechanical injury. 2. Emergency eyewash fountains and safety showers

should be available in the immediate vicinity of potential exposure. Do not puncture or incinerate containers.

3. Wear appropriate chemical protective clothing.

4 Thionyl Chloride 1. Store in a cool, dry, area away from incompatible substances. Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment., No manual handling

5 Phenol 1. Store in a cool, dry, underground storage area away from incompatible substances. Flammables-area. Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment.

6 Toluene 1. Store in a, dry well-ventilated location, away from any area where the fire hazard may be acute. If the exposure limit is exceeded and engineering controls are not feasible, a full face piece respirator with organic vapor cartridge may be worn up to 50 times the exposure limit or the maximum use concentration specified by the appropriate regulatory agency or respirator supplier, whichever is lowest above flash point, vapor-air mixtures are explosive within flammable limits noted above.

7 EDC 1. Keep away from heat, sparks, and flame. Keep away from sources of ignition. Store in a tightly closed container, Wear appropriate protective eyeglasses or chemical safety goggles., Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment., No manual handling

8 IPA 1. Store in a cool, dry place. Store in a tightly closed container, Respiratory Protection equipment Fire Fighting Equipment, Flame proof electrical equipment., No manual handling

9 HBR HBR will be stored in Iso-container in separate storage area and transported in Iso-container.

10 Methanol Flame proof plant, pumping transfer, close process, etc. Double Static earthing, Dyke wall , Tanker unloading procedure. SCBA sets available. Flame proof plant, pumping transfer, close process, etc. Jumper clips on flanges, Fire extinguishers, Fencing and No, Smoking and prohibited area., Tanker unloading procedure., Flame arrestor provided on vent line of the tank, Hydrant system

11 Dimethyl Formamide

12 Hydrogen

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13 Nitric Acid Safety Showers provided

Caution note provided

Dyke wall provided

Level gauge provided.

Double drain valve provided

Scrubber provided, Required PPEs provided to all employees

Applicability of PESO : Not Applicable All Raw material will be store as PESO Standards

H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)

- Hydrogenation Plant: • FLP type area will be provided. • Total enclosed process system. • Instrument & Plant Air System. • Nitrogen blanketing in Hydrogenation reactor. • Safety valve and Rupture disc provided on reactor. • Cooling Chilling and power alternative arrangement have been made on reactor. • Hydrogen and Nitrogen Cylinder bank away from the auto clave reactor. • PRV station with shut off valve, safety valve provision will be made for hydrogenation

reaction safety. • Before Hydrogen Gas charging in to reactor and after completion of reaction Nitrogen

flushing will be done. • Flame arrestor will be provided on vent line of reactor and it will be extended up to

roof level. • Open well ventilated and fragile roofs will be provided to on reactor. • Safe Catalyst charging method will be adopted. • SOP will be prepared and operators will be trained for the same. • Static earthing and electric earthing (Double) provided. • Reactor vent extended outside the process area and flame arrestor provided on vent

line. • Dumping vessel arrangement will be made. • Jumpers for static earthing on pipeline flanges of flammable chemical will be

provided. Nitration process

• Total enclosed process system. • Instrument & Plant Air System. • Safety valve and Rupture disc provided on reactor. • Cooling and power alternative arrangement have been made on reactor. • Emergency cooling alternative arrangement have been made on reactor. • Nitric acid storage away from the auto clave reactor. • Open well ventilated and fragile roofs will be provided to on reactor. • Scrubbing system will be installed to scrub nitrous gases generated during reaction. • SOP will be prepared and operators will be trained for the same. • Employees will be trained to handle nitric acid and continuous training schedule will be made. • Dumping vessel arrangement will be made.


FIRE LOAD CALCULATION

1 Name & Address of factory : M/s. Aalidhra Pharmachem Pvt. Ltd. Plot no. C-289,289/1, GIDC Saykha, Ta-Vagra, Dist-Bharuch, Gujarat, India.

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2 Phone Number : +91 99798 62155

3 Name of Occupier : Mr. Manish Gondalia

4 Total Floor of the factory : G + 1

5 Detail of Combustible Area (In sq. Meter)

a) Total Floor Area : 19650.0 M2

b) Open Space Area in which Combustible Material stored

: 100 M2

c) Area having more than 15 meter Height

: 0 M2

d) Area having Wooden material

: 500 M2

Total (a + b + c + d) : 20250 M2

6 a + b + c + d . 20

: 20250/20= 1012.5 L/Min

7 Total Requirement of Water (based on area in sr. no-6)

: 60750 Ltrs

8 Current Water storage Capacity for fire hydrant (Proposed)

: 750000 Ltrs

Under ground Tank + over head tank + On ground Tank

: UG Water Tank:

375,000 UG Water

Tank: 375,000

Ltrs

9 In case of Fire, Arrangement for water to be used in fire fighting

a) Is Hydrant Line available? If Yes give dimension of Pipe.

: Fire Hydrant Line with 6‖ pipe diameter is being implemented

b) Which type of arrangement are available for Supply water on ground or upper floor i.e. Pipe line and it's Diameter (c.m.); Give detail

: 1700 meter length of 6‖ pipe diameter will be provided for fire hydrant system.

c) Are Fire Water Pump Available or Not? Give detail

: Kirloskar main pump*2 (30000 Lit/Hr, 110-meter head) and one jockey pump (15 m3/hr, 75-meter head) will be provided

10

If the Value of Sr. 6 is more than 550, then requirement of trailer Pump is applicable. If it applicable then what is the arrangement for the Same. Give detail

: Trailer pump will be available having capacity of 1800 LPM at 7 kg/cm2

11

How many water buckets required?

: 90 nos

12

How Many 9 Litres water type Extinguisher required?(Water Bucket/6)

Fire Extinguisher

required =

90 / 6 = 15

Bucket may be dispensed with provided supply of extinguisher

is double than indicate above =

15 + 15

= 30

1 Requirement of 5 Kg CO2 : 0 nos

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3 Type Fire Extinguisher for Class - E fire. Floor wise (1 for every 15 m length)

Total requirement of Fire extinguishers (5 Kg ABC).

: 35 + 0 35 Nos.

14

Details of installed Fire Extinguishers.

Type nos

ABC (5 kg) : 35

CO2_ : 15

SAND BUCKET : 25

FOAM () : 30

FOAM TROLLY 45 Lit : 05

DCP : 20

TOTAL : 130

15

Additional Fire Extinguisher Required

: 20

16

Emergency Fire Exit provided to Each Floor? Ladder Provided to Each floor?

: YES

17

Arrangement for Fire warning. i.e. Hooter / Ele. Bell / Other

: YES

18

Water Sprinkler Provided? : YES

-


Unit will apply for fire NOC before getting CCA/NOC.


Occupational health impacts on the workers and mitigation measures proposed to avoid the human health hazards along with the personal protective equipment to be provided. Provision of industrial hygienist and monitoring of the occupational injury to workers as well as impact on the workers. Plan for periodic medical checkup of the workers exposed. Details of work place ambient air quality monitoring plan as per Gujarat Factories Rules. Expected Occupational Health Hazards & Safety

Physical Hazards: Noise, Heat, Dust Chemical Hazards: Corrosive (like Sulfuric acid), Toxic Substances (like Methanol &

Liquid Ammonia.). Psychological hazards resulting from stress and strain Hazards associated with the non-application of ergonomic principles, for

example badly designed machinery, mechanical devices and tools used by workers, improper seating and workstation design, or poorly designed work practices

Occupational Health effects of Chemicals primarily in the: Respiratory System: Lungs and Respiratory Track Brain – memory loss, confusion, difficulty concentrating, fatigue, headache Reproductive system – miscarriages, fetal alcohol syndrome Kidneys - Glomerulonephritis Skin – Irritant dermatitis, defatting Liver – Fatty liver, chemical hepatitis And Cardiovascular system – Increased sensitivity to epinephrine, exacerbation of coronary artery disease by CO due to methylene chloride, carbon disulfide.

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Mitigation Measures will be taken : - Proper PPE and sanitation facility will be provided - Washing Facility provided with adequate Lockers - Good Hygiene Measures will be adopted - Training will be imparted - Medical Surveillance program will be started.



Project proponent (PP) and Technical expert of PP, M/s. Aqua Air Environmental Engineers Pvt. Ltd

remains present during video conference meeting.

Committee noted that the proposal is for new project in GIDC Saykha. PP submitted details regarding

area adequacy. Source of water is GIDC. Product profile along with end use discussed in depth. Looking

to layout plan, Committee insisted for submit revised layout plan with mentioning water sprinkler in raw

material storage area which is later on submitted by PP.

Committee noted that PP has submitted waste water management and industrial effluent will be

segregated. High COD stream will be treated in primary ETP-1 and treated effluent will be sent to CMEE

of M/s BEIL for evaporation. Low COD stream will be treated in ETP-2 consist of primary, secondary and

tertiary ETP units and treated effluent will be sent to CETP of GIDC Saykha for further treatment and

disposal. Domestic sewage will be treated in STP. Committee discussed regarding stage wise reduction

of BOD, COD and TDS in ETP. Committee insisted for submit revised water balance diagram with

mentioning reuse of waste water and PP later on submitted revised water balance diagram with

mentioning reuse of boiler condensate for cooling tower in water balance diagram.

PP submitted that they have proposed boiler and thermo pack. Fuel used will be briquettes of bio coal for

boiler and thermo pack. Two stage scrubbers will be provided as APCM with each process reactor stack.

PP submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.





centre (OHC) and process hazard and its safety control measures. Committee insisted for fire hydrant

cost, Cost of LDAR with DSC in Solvent Distillation and PP later on submitted revised EMP with

mentioning its cost. Committee noted that PP presented details of auto control system for critical hazard

process. PP presented Hazardous chemical storage area with its risk assessment.


CER, etc.


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amendments.



4. Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB directions to all

SPCB vide letter no. B-29016/04/06PCI-1/5401 dated 05/02/2014 for effluent discharge and air

emission as per pollutants discharge/emission from respective project and an arrangement shall also

be done for reflecting the online monitoring results on the company's server, which can be

assessable by the GPCB/CPCB on real time basis. [For Small/Large/Medium (Red Category) &

Whichever (Air emission & Effluent discharge) is applicable].

5. Wastewater shall be fed to MEE only after providing adequate treatment in such a way that no


6. Treated waste water shall be sent to CETP only after complying with the inlet norms of common

facilities prescribed by GPCB to ensure no adverse impact on Human Health and Environment.

7. The PP shall develop green belt within premises (10925.77 Sq. m i.e. 33 % of the total plot area) as

per the undertaking submitted before SEAC. Green belt shall be developed with native plant species

that are significant and used for the pollution abatement as per the CPCB guidelines. It shall be



treated in STP. Treated sewage shall be utilized for gardening and plantation purpose within

premises after achieving on-land discharge norms prescribed by the GPCB.

9. During monsoon season when treated sewage may not be required for the plantation / Gardening /

Green belt purpose, it shall be stored within premises. There shall be no discharge of waste water

outside the premises in any case.

10. (a) R & D products shall be of similar chemistry in line with the EIA Notification vide S.O. 1223 (E)

dated 27/03/2020 and the pollution load shall remain the same as committed. (b) Project proponent

shall not take continuous/commercial production of the R & D materials. Necessary approvals shall

be obtained from the concern authorities prior to commercial production of R & D materials. (c) Unit

shall submit relevant details of R & D products like raw materials, its safety measures to the

regulatory authority well before R & D activity. (d) Unit shall submit relevant details of R & D products

like different wastes generated (Quantity & Quality) and its management to the regulatory authority

within a month of R & D activity.


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applicable)





2016.





accident.











k) Unit shall provide safety valve & rupture disc to the Hydrogenation vessel.

l) Unit shall store Bromine Bottle in cool dry separate area, out of direct sunlight.

m) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam


n) Unit shall provide safety valve and rapture disc, as well as auto dump or auto quenches/,

suppresses system for nitration reaction vessel safety.

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5. SIA/GJ/IND2/166174/2020 M/s. Ambition Pharma

Survey No. 202/10, Golana Road, Village:

Sokhada, Ta: Khambhat, Dist: Anand

Appraisal


Project status: New







tabulated below,

Sr. No

Company Products

API Or Intermediate

CAs No Quantity

(MT/Month) End Use

1. Sucralfate API 54182-58-

0 25

Sucralfate is an anti-ulcer medication. Sucralfate is not greatly absorbed into the body through the digestive tract. It works mainly in the lining of the stomach by adhering to ulcer sites and protecting them from acids, enzymes, and bile salts. Sucralfate is used to treat an active duodenal ulcer.

2. Riboflavin Sodium

Phosphate API 130-40-5 10.50

Riboflavin sodiumphosphate is converted to flavin mononucleotide (FMN) and flavin adenine dinucleotide (FAD), which are required for red blood cell formation and respiration, antibody production

3. Ferrous

Ascorbate API

24808-52-4

16 Ferrous Acrobat is used in the treatment of anaemia. Anaemia cause to chronic kidney disease

Total 51.50

ENDUSE OF PRODUCTS

Sr. No.

Name of the

Product

CAS No. (Product)

Type/ Category of

Product (API/

Intermediate)

In case of Intermediate stage of API

Said API is used for/End Use of said API Stage of

Intermediate n-1, n-2, etc


Intermediate Used/ End use of said

Intermediate

CAS No.

(API)

1. Sucralfate 54182-58-

0 API - - -

Sucralfate is an anti-ulcer medication. Sucralfate is

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not greatly absorbed into the body through the digestive tract. It works mainly in the lining of the stomach by adhering to ulcer sites and protecting them from acids, enzymes, and bile salts. Sucralfate is used to treat an active duodenal ulcer.

2.

Riboflavin Sodium

Phosphate 130-40-5 API - - -

Riboflavin phosphate sodium is converted to flavin mononucleotide (FMN) and flavin adenine dinucleotide (FAD), which are required for red blood cell formation and respiration, antibody production.

3. Ferrous

Ascorbate 24808-52-

4 API - - -

Ferrous Acrobat is used in the treatment of anaemia. Anaemia cause to chronic kidney disease





Sr. no.

Particulars Details

A

A-1

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

Total Project

2.0 Crores



Land 0.7

Building

Machinery 1.3

A-2

Details of Environmental Management Plan (EMP) As below:

Sr. No

Unit Installed Capacity (KLD)

Capital Cost (Rs.in Lacs )

Operating Cost (Lacs/ Month)

Maintenance Cost (Lacs/ Month)

Total Recurring Cost (Lacs/ Month)

1 Effluent Treatment

Installation of ETP and evaporator

10 0.7 0.1 0.8

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Plant

2. APCM

Provision of odour control system Provision of gas detectors

5 0.3 0.1 0.4

3. AWH Monitoring

To conduct EMS efficacy & environment monitoring

- 1.0 - 1.0

4. Green belt development

Development of Greenbelt Area

- 3.5 - 3.5

5. Fire

Provision of Safety Measures including Fire Detectors, Sensors, Alarm, Fire Hydrant, Fire Extinguishers, Lightening arrestors etc

12 2.0 0.50 2.50

6. Health & Safety

Provision of Occupational Health Centre with Antidotes

5 1.0 0.5 1.50

7. Other CER 4.0 - - -

PLC, SCADA 10 2.0 0.5 2.5

Total 46 10.5 1.7 12.2

Summary

Cost of Project in Crores per Annum: 2.0

EMP Capital Cost in Crores per Annum and Percentage:

0.44 (13 %)

EMP Recurring Cost in Crores per Annum and Percentage:

0.12

A-3

Details of CER as per OM dated 01/05/2018 (In case of project falls under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide 31.10.2019.)

% as per the OM Rs. in Lakh

2.0 4.0

Brief note on proposed activities

No. CER-Proposed Planned Activities Identified Villages

Year wise Budget (Lakhs)

1st Year

1

Contribution towards Installation of RO System (100 LPH) and other required materials to Primary School, and primary health center at Sokhda Village.

Sokhda Village 4.0

Total (Year Wise) 4.0

Grand Total 4.0 lac

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B-1

Total Plot area ( sq. meter)

Total Plot area

5722 Sq. m.

B-2

Brief note on Area adequacy in line to proposed project activities:

Sr No.

Description of Area Area (sq. m)

1 Production 1200

2 Raw material Storage 150

3 Product Storage 150

4 Storage tank Area 150

5 Occupational Health Center 25

6 Utility 270

7 Effluent Treatment plant 60

8 Sewage Treatment Plant 30

9 Water Storage tank 30

10 Green Belt 1890

11 Road & Open 1767

TOTAL 5722

B-3

Green belt area

Total (Sq. meter)

Area in Sq. meter 1890

% of total area 33.0


Total

40

D Water

D-1

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

Status of permission from the concern authority. The unit obtained CGWA NOC

D-2


Sr No

Category Water Consumption KLD

Remark

1. Domestic Purpose 2.0

2. Other use(Gardening) 1.5 Reuse from STP

3.

INDUSTRIAL

DM plant 13.0 For Process DM Water plant Inside

Boiler 6.0

Washing 1.0 Reuse

Cooling 3.0 Reuse

Total water Consumption (Domestic)

2.0

Total water Consumption 23.0

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(Industrial )

Grand total(1+2+3) 26.50

Total Fresh 21.00

Total Reuse 5.50

D-3

Waste water generation (KLD)

Sr No

Category Waste Water

Generation KLD Remark

1. Domestic Purpose 1.5 Send to STP

2.

INDUSTRIAL

Process 7.0 In house Evaporate

DM Reject 3.4 Treated in separate ETP followed by RO. RO Permeate will be

utilized in Cooling and washing

Boiler 0.6

Washing 1.0

Cooling 0.3

Total wastewater Generation (Domestic)

1.50

Total wastewater generation (Industrial )

12.3

-

Brief Note on worst case scenario for waste water generation(Qualitative and Quantitative):

Sr. No

Name of Product

KL per MT of Product KL Per Day

Waste Water Generation

Waste Water Generation

1. Sucralfate 3.5 3.5

2. Riboflavin Sodium Phosphate 5.0 2.1

3. Ferrous Ascorbate 2.2 1.4

TOTAL KLD 7.0

Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (If any applicable to proposal).

D-4

Mode of Disposal & Final meeting point

Domestic: Domestic sewage 1.50 KLD generated will be reuse in Gardening After Treatment in STP Plant

Industrial: Total industrial 12.3 KLD Waste water generation from manufacturing Process and other ancillary Operation

The Wastewater from process 7.00 KLD will be treated in ETP -1 and evaporated along with RO Reject water from ETP 2

The stream other than process will be treated in ETP 2 followed RO and RO Permeate will be reuse in washing and cooling

- Clearly mention about final disposal In house Evaporation System

D-5

Treatment facilities


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Capacity of STP: 1.5 KLD

For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed. ETP 1

ETP 2

ETP – 1

Sr. No. Name of Unit Capacity (KL)

1. Stripping tank 10.0

2. Effluent collection tank 10.0

3. Primary Settling tank 5.0

4. Holding tank-1 5.0

5. Pressure Sand Filter 1.0 m dia


7 Evaporator 1 KLPH

8. Sludge Drying Bed 1.5 m x 1.5 m, 4 Nos.

ETP – 2

Sr. No. Name of Unit Capacity (KL)

1. Effluent collection tank 6.00

2. Primary Settling tank 5.0


4. RO System 500 LPH


Sr No

Parameter

Unit Process Washing Boiler Cooling Combine

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1. pH pH Scale 4-5 7-8 7-8 7-8 4-5

2. T.D.S. mg/l 4000-5000 1500-2000 500-800 500-800 4000-5000

3. C.O.D mg/l 2000-4500 1200-1500 250-300 250-300 2000-4500

Sr No Parameter Unit ETP inlet After primary treatment

Evaporate

1. pH pH Scale 4-5 7-8 7-8

2. T.D.S. mg/l 4000-5000 5000-6000 5000-6000

3. C.O.D mg/l 2000-4500 1800-2000 1800-2000


Total industrial 12.3 KLD Waste water generation from manufacturing Process and other ancillary Operation



Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Total industrial 12.3 KLD Waste water generation from manufacturing Process and other

ancillary Operation



.

D-6

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

Not Applicable

Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.

Not Applicable

D-7

Simplified water balance diagram with reuse / recycle of waste water

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E Air

E-1

Brief Note on fuel based heat energy requirement and worst case scenario thereof:

E-2

Flue gas emission details No. of Boilers/TFH/Furnaces/DG sets etc. with capacities viz. TPH, Kcal/hr, MT/hr, KVA etc. (In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)

-

Sr. no

Stack attached to

Stack height and dia

Fuel Quantity of

Fuel MT/Day

APCM Types of Emission

1 Steam boiler (1.5 TPH)

20.0 m

Briquettes or Agro waste

1 Cyclone Separator

PM SOx NOX

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2 HAG 5 lac Kcal/hr

20.0 m

Briquettes or Agro waste

4 Cyclone Separator

3 D.G Set (200 KVA)

5.0 m HSD 0.6 adequate stack Height

E-3

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

-

Sr. No.

Stack Attached to Stack

Height (m) APCM

Parameter & Permissible

Limit

1 Spray Dryer for Product 500 LPH

15.0 Cyclone Separator+ Two

stage Water Scrubber PM

Note:

Details of gaseous raw materials used in proposed project Estimation of process gas emission (Product wise and Total) Requirement of the scrubbing media (KL per Day) considering solubility (Product wise and

Total) Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its sound

management in HW matrix.

E-4

Fugitive emission details with its mitigation measures: As below:

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

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

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

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

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

chemical storage area

A regular preventive maintenance will be planned to replace or rectify all gaskets, joints etc.

The unit will also develop green belt within the factory premises to control the fugitive emission from spreading into surrounding environment.

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




F-1

Hazardous waste management matrix

Sr Types of Specific Category Propose Management of HW

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. No

Hazardous Waste

Source of generation (Name of the Activity, Product etc.)

and Schedule as per HW Rules.

MT/Year

1. ETP Sludge

ETP area 35.3 60

Collection, Storage, transportation and disposal at any registered TSDF site

2.

Process Wastes, sludge

Riboflavin Sodium Phosphate, Ferrous Ascorbate

21.1 250

Collection, Storage, Transportation, Disposal at Registered TSDF or Disposal by co-processing or Incineration

3. Used Oil Plant Machinery

5.1 0.050

Collection, Storage, Transportation, sell to MoEFCC approved recyclers OR Reused as Lubricant within premises

4.

Discarded Container/ Liner

Material Storage and Handling

33.3 1.0

Collection, storage, Transportation and Dispose to Registered Recycler

5. Solvent residue

Distillation Unit

26.3 36

Collection, Storage, Transportation and disposal by co processing or by disposal to CHWIF

6. Spent solvent

Riboflavin Sodium Phosphate, Ferrous Ascorbate

26.4 1200

Recovered, storage and reused in the next batch of same product after Distillation

7. Evaporation Residue

Evaporation

35.3 15.0

Collection, Storage, transportation and disposal at any registered TSDF site

-

F-2

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

Details of Membership letter no. & Date with spare capacity of the Common Facility. We will obtained after getting NOC from GPCB

F-3

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

Sr. no.



Quantity (MT/Annum)


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1 NIL NIL NIL NIL


G-1

Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.

Sr. No

Name of Product Solvent Total Solvent Quantity

Recover of Solvent

Loss of Solvent

% of recovery

% of Losses

1.

Riboflavin Sodium Phosphate,

Methanol 6250 6100 313 97.6 2.4

2. Ferrous Ascorbate

Methanol 2310 2217 93 96.0 4.0

G-2

Brief Note on LDAR proposed:

The industry is engaged in the manufacturing of bulk drugs and fine chemical, which require solvents during various unit processes. The unit uses solvent which is

The spent solvent generated during the manufacturing process will be recovered by way of distillation and will be reused in the process. The process of the solvent recovery system is described hereunder;

After completion of the reaction, the whole mass in the reactor will be pumped to SS reactor which is subjected to the distillation to separate finished product and recover solvent.

Firstly, the mass will be distilled at required temperature and pressure where pure solvent will be distilled out depending on their boiling points and it will be collected in the recovered solvent storage tank and reused in the process.

Vacuum will also be applied as per requirement during distillation.

The overall requirements and mass balance for the solvent based on mass balance of each product and summary has been worked out which is given in Table as above. The schematic diagram of the solvent recovery system is shown in the Figure Measures for achieving maximum solvent recovery:

The entire manufacturing activities & distillation process will be carried out in totally closed system.

Regular maintenance of the pipeline and valves & fittings will be carried out regularly to avoid any leakages.

Distillation column will be connected with condenser where cooling water will be used as media and also equipped with vacuum system.

The condenser will be provided with the sufficient HTA and residence time to achieve more than 98% recovery.

During the manufacturing activity as well as during distillation process 2% of the total solvent will be lost; approx. 98 % of solvent will be recovered during the process. The fresh solvent requirement will depend on solvent loss during distillation as well as manufacturing activity.

G-3

VOC emission sources and its mitigation measures

Sources of fugitive emissions include storage of chemicals, solvents storage, loading and unloading section, raw material handling and, hazardous waste storage area

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

handling. Hazardous chemicals will be stored as per standard criteria. Periodically monitoring will be carried out as per the post project monitoring plan. Proper ventilation in storage & production area shall be ensured All materials must be stored in suitable packing to prevent contamination of air

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Enclosed system & efficient procedures for materials charging shall be ensured. Procedures for start-up shut down, operation & maintenance procedures shall be established &

maintained. The coverage of greenbelt around the plant also acts as natural barrier to stop carrying of dust

along with the wind current.

H Safety Detail

H-1

Details regarding storage of Hazardous chemicals (For tank storages only including spent acid and spent solvent tanks)

Sr No

Name of Raw Material

State

Storage Capacity in KL

Number of Tank

Storage at time (KL)

IDLH ppm

Boiling Point °C

Flash Point °C

Dyke Wall height

Capacity of Dyke (KL)

Hazard characteristic

Fire extinguisher Type

1 Methanol

Liquid

15 1 15

6000

64.7

9 1.3 16.5 Flammable

CO2, Dry Chemical or Foam

2

Distilled Methanol

Liquid

5 1 5

6000

64.7

9 1.3 5.5 Flammable


3

Spent Methanol

Liquid

10 1 10

6000

64.7

9 1.3 11 Flammable


4 Suphuric Acid

Liquid

10 1 10 15

193 - 1.3 11 Corrosive

Sand Bucket

5 HCl Liquid

5 1 5 50

83 - 1.3 5.5 Corrosive

Sand Bucket


Methanol

• Tank, valve, pipeline are checked and maintain, in good condition through preventive maintenance

• Joints are checked regularly to detect any Leakage. • ISI Portable fire extinguisher & Fire Hydrant line is provided as per TAC norms. • Flame proof electrical fittings / installation provided. • Proper Earthing, Bonding & flange-to-flange jump ring is provided. • Flame arrester provided on vent line. • CCE approved Separate Storage area with door having locking arrangement. • Auto & manual sprinkler provided. • Spark arrester are installed on all vehicles inside the premises. • Apron, Hand gloves, gumboot, goggles and helmet provided. • Train operator employed. • Eye washer & shower provided. • Tank‘s thickness measured on regular interval. • Good ventilation in the area. • Flame arrester with breather valve. • Perforated dip pipe in dyke wall will be provided to monitor & detect any leakage from

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tank. • Sump will be made under dyke to recover leakage material from dyke. • Tanks will be kept under RCC dyke. • Tanks will be kept under shed.


Ferrous Sulphate PhosphrousOxi chloride Riboflavin Gluconic Acid Soda ash



Safety measures

Methanol • The charging of material will be carried out by PLC based SCADA System semi automization

• Tank, valve, pipeline are checked and maintain, in good condition through preventive maintenance

• Joints are checked regularly to detect any Leakage. • ISI Portable fire extinguisher & Fire Hydrant line is provided as per

TAC norms. • Flame proof electrical fittings / installation provided. • Proper Earthing, Bonding & flange-to-flange jump ring is provided. • Flame arrester provided on vent line. • CCE approved Separate Storage area with door having locking

arrangement. • Auto & manual sprinkler provided. • Spark arrester are installed on all vehicles inside the premises. • Apron, Hand gloves, gumboot, goggles and helmet provided. • Train operator employed. • Eye washer & shower provided. • Tank‘s thickness measured on regular interval. • Good ventilation in the area. • Flame arrester with breather valve. • Perforated dip pipe in dyke wall will be provided to monitor & detect

any leakage from tank. • Sump will be made under dyke to recover leakage material from

dyke. • Tanks will be kept under RCC dyke. • Tanks will be kept under shed.

Sulphuric Acid

• The Entire plant will be operated by PLC based SCADA System and semi atomization

• Store in cool, dry and well ventilated area in compliance with compatible chart

• Dyke wall with sufficient size is provided. • Tank, valve, pipeline are checked and maintain, in good condition. • Apron, Hand gloves, gumboot, goggles and helmet will be provided. • ISI Portable fire extinguisher & Hydrant line is provided as per TAC

norms. • Sufficient amount of sand/soil are kept to control any spillage. • Eye washer cum shower is provided near tank-farm area. • Level indicator provided.

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• Vent line dipped in dilute caustic will be provided. • RCC foundation will be provided. • The material transfer is only from pump and fixed line in receiver

tank with return valve to main tank

HCL • The charging of material will be carried out by PLC based SCADA System and semi automization.

• Dyke wall provided. • Dyke wall with sufficient size is provided. • Tank, valve, pipeline are checked and maintain, in good condition. • Apron, Hand gloves, gumboot, goggles and helmet will be provided. • ISI Portable fire extinguisher & Hydrant line is provided as per TAC

norms. • Sufficient amount of sand/soil are kept to control any spillage. • Eye washer cum shower is provided near tank-farm area. • Level indicator provided. • Vent line dipped in water will be provided. • RCC foundation will be provided. • Transfer material to another empty tank/ Vessel.

Applicability of PESO :

H-2

Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)

Type of Process


NIL There is no nay hazardous Process involved

H-3

Details of Fire Load Calculation

Total Plot Area: 5722

Area utilized for plant activity: 1650

Area utilized for Hazardous Chemicals Storage: 150

Number of Floors: GF

Water requirement for firefighting in KL : 11.100 KL

Water storage tank provided for firefighting in KL: 200 KL

Details of Hydrant Pumps: 6.0 Inch Diameter fire hydrant line will be provided connected to Jockey Pump having 07 bar pressure with sprinkler system. The jockey pump is placed with the fire water tank having capacity of 200 KL.

Nearest Fire Station : Khambhat @5.12 KM

Applicability of Off Site Emergency Plan: Not Applicable

H-4

Details of Fire NOC/Certificate:

We will obtained after getting NOC from GPCB

H-5

Details of Occupational Health Centre (OHC):

Number of permanent Employee: 15


Area provided for OHC: 25 Sq. m

Number of First Aid Boxes : At least one box containing such items and placed and maintained in accordance with the requirements of Sec. 45 is separately provided.

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Nearest General Hospital : The Cambay General Hospital Khambhat@ 4.0 Km

Name of Antidotes to be store in plant : Injection -morphia, pethidins, atropins, adrenaline, coramine, novocan Fomepizole, Cobalt EDTA, Diazem, Epinephina, Efidrine, Ethanol, Milk of Magnesia epicake syrup, Sodium Hydro-Carbonate (4% Conc.), Milk, Lime Juice, Soda Water, Soframycine



Project proponent (PP) and Technical expert of PP, M/s. Satva Environ Consultancy remains present

during video conference meeting.

This is a new proposal of API and Its Intermediates plant at Survey No. 202/10, Golana Road, Village:

Sokhada, Ta: Khambhat, Dist: Anand, located outside notified area. Source of water supply is Bore well.

Committee asked for status of CGWA permission for ground water source, PP informed that they have

apply for CGWA permission. Also PP has presented NA permission for proposed plot is for industrial

purpose. PP submitted Google map showing that there is no any water bodies, villages, School,

monuments etc. within 500 m radius of the project site. PP also submitted that there are no Eco sensitive

zones, wild life sanctuaries within the 10 km area from the boundary of the project site.

Product profile along with End Use discussed in depth. Committee noted that PP has addressed area

adequacy for proposed project with layout plan.

Committee noted that effluent stream segregation will be carried out. High COD effluent from Process

will be treated in primary treatment plant, ETP-1 and treated effluent will be evaporated in in-house

evaporator. Low COD stream will be treated in ETP-2 followed by RO plant. RO reject will be evaporated

in evaporator. Committee insisted for clarification regarding high COD and TDS stream evaporated in

evaporator is technically feasible with treatability report for ETP and evaporator and justification

regarding totally evaporation of effluent in evaporator with heat balance, technical expert of PP could not

addressed properly during meeting.

Committee noted that agro waste or briquette will be used as fuel for boiler and hot air generator.

Cyclone separator as APCM will be attached with boilers and thermo pack. Committee insisted for

technical clarification regarding proposal of cyclone separator as APCM for 1.5 TPH boiler and Hot air

generator and 1 TPD agro waste or briquette consumption as fuel for 1.5 TPH boiler. Cyclone separator

and water scrubber will be provided as APCM with spray dryer. Technical expert addressed hazardous

waste management including scrubber bleed liquor and spent solvent disposal.

Committee noted that PP has addressed LDAR and solvent recovery, green belt development, EMP and

CER for proposed project. PP explained regarding safety control measures for process hazard and

Hazardous chemical storage and its management. Committee discussed in length regarding fire hydrant

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system, evacuation plan, storage and safety measures of hazardous chemicals.

Since, the unit falls in B2 category as per the MoEF&CC‘s amended EIA Notification vide S.O. 1223(E)

dated 27.03.2020, the public consultation is not applicable as per paragraph 7(i) III (i) (e) of the

Environment Impact Assessment Notification-2006.

After detailed discussion, Committee unanimously decided to consider the project only after

submission of following documents,

1. Submit clarification regarding high COD and TDS stream evaporated in evaporator is technically

feasible with treatability report for ETP and evaporator and also justification regarding totally

evaporation of effluent in evaporator with heat balance.

2. Submit technical clarification regarding proposal of cyclone separator as APCM for 1.5 TPH boiler

and Hot air generator and 1 TPD agro waste or briquette consumption as fuel for 1.5 TPH Boiler.

6. SIA/GJ/IND2/166235/2020 M/s. Global Medicines Limited

Plot No. 5068, GIDC- Ankleshwar, Dist -

Bharuch

Appraisal

During SEAC VC meeting on dated 17.12.2020, Project Proponent and their technical expert remain

absent. PP has submitted letter via Email stating that they would remain absent during meeting. PP

also requested to schedule the project in any upcoming SEAC meeting.

Hence, Committee decided to defer this proposal and consider this in one of the upcoming SEAC

meeting.

7. SIA/GJ/IND2/173473/2020 M/s. Skanttr Life science LLP

Survey no.: 340 & 345, Amipura,

Ta. Bavla, Dist: Ahmedabad

Appraisal


Project status: Expansion






This is an existing unit and now proposes expansion in manufacturing of synthetic organic chemicals

[API and API Intermediates] as tabulated below,

Sr. no.


API OR

INTERMEDIA

TE

CAS no.

Quantity MT/Month

End-use of the products * Exi

sting

Proposed

Total

of 232


Page 125 of 232

1 Itraconazole API 84625-

61-6

-

12.5

MT/M

20

MT/M

(Either/

or)

Anti-Fungal

2

Ketoconazol

e

API

65277-42-1

-

Anti-Fungal

3

Vardenatil API 224785-

90-4 -

Phosphodiesterase inhibitors

4

Miconazole

API

22916-47-8

- Anti-Fungal

5

Ticonazole

API

65899-73-2

- Anti-Fungal

6

Atorvastatin calcium

API 134523-

00-5 6

Cardiovascular

diseases

7

Candesartan API 139481-

59-7

Anti-Hypertensive

8

Carbidopa API 28860-95-9

1.5

used to treat symptoms of Parkinson's

disease, such as muscle stiffness, tremors, spasms

9

Losartan

Potassium

API 124750-

99-8 -

Anti-hypertensive/T

ablet

10 Hydroxychlor

oquine API

118-42-

3 4

-6.5

MT/M

20

MT/M

(Either/

or)

rheumatoid

arthritis

11 Rosuvastatin

e Calcium API

287714-41-4

1.5

To reduce your LDL (bad) cholesterol levels and

increase your HDL (good) cholesterol

levels

12 Montelukast

sodium API

158966-92-8

5

It is used to control and

prevent symptoms

caused by asthma (suc

h as wheezing and shortness of

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Page 126 of 232

breath)

13 Luliconazole API 187164-

19-8 - Anti Fungal

14 Clotrimazole API 25593-75-1

- Anti Fungal

15 Sodium

valproate API

1069-66-5

-

Sodium valproate is used to treat epilepsy and

bipolar disorder.

16 Pantoprazole

Sodium API

138786-67-1

16

It is used to treat damage

from gastroesophag

eal reflux disease

17 Azilasartanm

edoxoil API

147403-03-0

- Anti-

Hypertensive

18 Telmisartan API 144701-

48-4 -

13.2

MT/M

20

MT/M

(Either/

or)

Anti

Hypertensive

19 Valsartan API 137862-

53-4 -

Anti Hypertensive

20 Ranolazine API 142387-

99-3 - Anti Anginal

21 Amlodipine Besylate

API 88150-42-9

6.8

used to treat high blood pressure (hype

rtension).

22 Valproic acid API 99-66-1 - Used to treat

migraine headache

23 Olmesartan API 144689-

63-4 -

Angiotensin receptor blockers

24 Abiraterone

Acetate API

154229-

19-3 -

-2.2

MT/M

10

MT/M

(Either/

or)

Anti-Cancer

25 Linezolid API 165800-

03-3 - Anti bacterials

26 Quetiapine Fumarate

API 111974-

69-7 -

anti-psychotic drug

27 Rivaroxaban API 366789-

02-8 - Anti coagulant

28 Glimepiride API 93479-97-1

10

Controlling high blood sugar

helps prevent kidney

damage, blindness,

nerve problems

29 Escitalopram

Oxalate API

219861-08-2

- Anti-

Depressant

30 Fexofenadin API 153439- 2.2 Fexofenadine i

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Page 127 of 232

e hydrochlorid

e

40-8 s an antihistamin

e used to relieve allergy

symptoms such as

watery eyes, runny

nose, itching eyes/nose, sneezi

ng, hives,

31 Atenolol API 29122-

68-7 9.6

-7.9

MT/M

10

MT/M

(Either/

or)

Used to treat

high blood

pressure

32 Levosulporid

e API

23672-07-3

2.1

Levosulpiride is used in

the treatment of

Gastroesophageal reflux disease

33 Aripiprazole API 129722-

12-9 3.0

Used as an antipsychotic

drug

34 Olanzapine API 132539-

06-1 3.2

Used for the treatment of schizophrenia

35 Taurine API 107-35-

7 -

Use for high blood pressure,

high cholesterol

36 Levetiraceta

m API

102767-28-2

- Epilepsy

37 Bupivacaine API 38396-

39-3 -

4.8

MT/M

10

MT/M

(Either/

or)

Local-

Anesthetic

38 Lidocaine

HCl API

137-58-6

- Local-

Anesthetic

39 Febuxostat API 144060-

53-7 -

Xanthine Oxidase Inhibitors

40 Levamisole API 16595-80-5

- Anti fugal

41 Labetalol

hydrochloride

API 36894-69-6

3

Labetalol is used to treat hypertension (high blood pressure).

42 Lafutidine API 118288-

08-7 2.2

used to treat stomach acid-

related disorders such

as gastroduodenal

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ulcers

43 Clopidogrelbi

sulphate API

120202-

66-6 -

3.4

MT/M

5

MT/M

(Either/

or)

Anti-Platelet

44 Oseltamivir Phosphate

API 204255-

11-8 - Anti Viral

used for the treatment of

osteoarthritis, rheumatoid

arthritis, acute pain in adults, and primary

dysmenorrhea

45 Rofecoxib API 162011-

90-7 -

46 Ticagrelor API 274693-

27-5 - Anti Platelet

47 Methylcobala

min API

288315-09-3

0.1 used to treat

anemia, diabetes

48 Albuterol API 18559-94-9

1.5

Albuterol is used to prevent

and treat difficulty

breathing, wheezing,

shortness of breath, etc.

49 Etoricoxib API 202409-

33-4 -

Anti-Inflammation

50 Sertraline

hydrochloride

API 79617-96-2

- Anti-

Depressant

52 Favipiravir API 259793-

96-9 -

1.9

MT/M

5

MT/M

(Either/

or)

Anti-Viral

53 Silodosin API 160970-

54-7 - alpha blockers

54 Saxagliptin API 709031-

78-7 1 alpha blockers

55 Artemether API 71963-77-4

- Anti-Malerial

56 Artesunate API 88495-63-0

- Anti-Malerial

57 Abacavir Sulphate

API 216699-

07-9 2.1

This lower the chances of getting HIV

complications such as

infections, cancer

58 Dapagliflozin API 461432-

26-8 - -1.6

MT/M

5

MT/M

Anti-Diabetic

59 Empagliflozin API 864070- - Anti-Diabetic

of 232


Page 129 of 232

44-0 (Either/

or) 60 Paliperidone API 144598-

75-4 - Schizophrenia

61 Ursodeoxych

olic acid API

128-13-2

1.4 Used to treat a certain type of liver dieases

62 Folic acid API 59-30-3 3

Folic acid is used to treat deficiencies, which can

cause certain types

of anemia and other problems

63 Ciprofloxacin API 85721-33-1

-

used to treat serious infectio

ns, such as: chest infections

(including pneumonia)

skin and bone infections

.

64 Praziquantel API 55268-74-1

- anthelmintics

65 Ramipril API 87333-19-5

- Anti

Hypertensive

66 Lisinopril API 83915-83-7

- Anti

Hypertensive

67 Eszopiclone API 138729-

47-2 - Insomnia

68 Nebivolol API 99200-09-6

- Anti

Hypertensive

69 Ipratropium

Bromide API

7726-95-6

2.2

Ipratropium is used to control

and prevent symptoms

(wheezing and shortness of

breath) caused by

ongoing lung disease

70 Captopril API 62571-86-2

- Anti-

Hypertensive

R&D activity, pilot batches

0.5 0.5

Total

87.

4

MT/

M

18.1

MT/M

105.5

MT/M

ENDUSE OF PRODUCTS

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Page 130 of 232

Sr. no.


CAS no. Product

Type/Category

of Product (API/Intermedia

te)

In case of intermediate stage of API

End-use of the said API

Stage of

Intermediate n-1, n-2, etc


Intermediate Used/ End use of said

Intermediate

CAS No.

(API)

1. Itraconazole 84625-61-6

API -

Anti-Fungal

2.

Ketoconazole

65277-42-1

API -

Anti-Fungal

3. Vardenatil 224785-90-4

API - Phosphodiesteras

e inhibitors

4. Miconazole

22916-47-8

API - Anti-Fungal

5. Ticonazole

65899-73-2

API - Anti-Fungal

6. Atorvastatin

calcium 134523-

00-5 API

Cardiovascular diseases

7. Candesartan 139481-

59-7 API Anti-Hypertensive

8. Carbidopa 28860-95-9

API

used to treat symptoms of Parkinson's

disease, such as muscle stiffness, tremors, spasms

9.

Losartan Potassium

124750-99-8

API Anti-

hypertensive/Tablet

10. Hydroxychlor

oquine 118-42-

3 API

rheumatoid arthritis

11. Rosuvastatin

e Calcium 287714-

41-4 API

To reduce your LDL (bad)

cholesterol levels and increase your

HDL (good) cholesterol levels

12. Montelukast

sodium 158966-

92-8 API

It is used to control and prevent

symptoms caused by asthma (such as wheezing and

of 232


Page 131 of 232

shortness of breath)

13. Luliconazole 187164-

19-8 API Anti Fungal

14. Clotrimazole 25593-75-1

API Anti Fungal

15. Sodium

valproate 1069-66-5

API

Sodium valproate is used to treat epilepsy and

bipolar disorder.

16. Pantoprazole

Sodium 138786-

67-1 API

It is used to treat damage from

gastroesophageal reflux disease

17. Azilasartanm

edoxoil 147403-

03-0 API Anti-Hypertensive

18. Telmisartan 144701-

48-4 API

Anti Hypertensive

19. Valsartan 137862-

53-4 API Anti Hypertensive

20. Ranolazine 142387-

99-3 API Anti Anginal

21. Amlodipine Besylate

88150-42-9

API

used to treat high blood

pressure (hypertension).

22. Valproic acid 99-66-1 API Used to treat

migraine headache

23. Olmesartan 144689-

63-4 API

Angiotensin receptor blockers

24. Abiraterone

Acetate 154229-

19-3 API

Anti-Cancer

25. Linezolid 165800-

03-3 API Anti bacterials

26. Quetiapine Fumarate

111974-69-7

API anti-psychotic drug

27. Rivaroxaban 366789-

02-8 API Anti coagulant

28. Glimepiride 93479-97-1

API

Controlling high blood sugar helps

prevent kidney damage,

blindness, nerve problems

29. Escitalopram

Oxalate 219861-

08-2 API Anti-Depressant

30.

Fexofenadine

hydrochloride

153439-40-8

API

Fexofenadine is an antihistamine u

sed to relieve allergy

symptoms such as watery eyes, runny nose, itching eyes/

https://www.webmd.com/migraines-headaches/migraines-headaches-migraines



of 232


Page 132 of 232

nose, sneezing, hives, and itching.

31. Atenolol

29122-68-7

API

Used to treat high blood pressure

32. Levosulporid

e 23672-07-3

API

Levosulpiride is used in

the treatment of Gastroesophageal

reflux disease

33. Aripiprazole 129722-

12-9 API

Used as an antipsychotic drug

34. Olanzapine 132539-

06-1 API

Used for the treatment of schizophrenia

35. Taurine 107-35-

7 API

Use for high blood pressure, high

cholesterol

36. Levetiraceta

m 102767-

28-2 API Epilepsy

37. Bupivacaine 38396-39-3

API

Local-Anesthetic

38. Lidocaine

HCl 137-58-

6 API Local-Anesthetic

39. Febuxostat 144060-

53-7 API

Xanthine Oxidase Inhibitors

40. Levamisole 16595-80-5

API Anti fugal

41.

Labetalol hydrochlorid

e

36894-69-6

API

Labetalol is used to treat

hypertension (high blood pressure).

42. Lafutidine 118288-

08-7 API

used to treat stomach acid-

related disorders such as

gastroduodenal ulcers

43. Clopidogrelbi

sulphate 120202-

66-6 API

Anti-Platelet

44. Oseltamivir Phosphate

204255-11-8

API Anti Viral

45. Rofecoxib 162011-

90-7 API

used for the treatment of

osteoarthritis, rheumatoid

arthritis, acute pain in adults, and

primary dysmenorrhea

46. Ticagrelor 274693-

27-5 API Anti Platelet

47. Methylcobala 288315- API used to treat

of 232


Page 133 of 232

min 09-3 anemia, diabetes

48. Albuterol 18559-94-9

API

Albuterol is used to prevent and treat difficulty

breathing, wheezing,

shortness of breath, coughing

etc.

49. Etoricoxib 202409-

33-4 API Anti-Inflammation

50.

Sertraline hydrochlorid

e

79617-96-2

API Anti-Depressant

51. Solifenacin succinate

242478-38-2

API Anti muscarinics

52. Favipiravir 259793-

96-9 API

Anti-Viral

53. Silodosin 160970-

54-7 API alpha blockers

54. Saxagliptin 709031-

78-7 API alpha blockers

55. Artemether 71963-77-4

API Anti-Malerial

56. Artesunate 88495-63-0

API Anti-Malerial

57. Abacavir Sulphate

216699-07-9

API

This lower the chances of getting HIV complications such as infections,

58. Dapagliflozin 461432-

26-8 API

Anti-Diabetic

59. Empagliflozin 864070-

44-0 API Anti-Diabetic

60. Paliperidone 144598-

75-4 API Schizophrenia

61. Ursodeoxych

olic acid 128-13-

2 API

Used to treat a certain type of liver

dieases

62. Folic acid 59-30-3 API

Folic acid is used to treat

deficiencies, which can cause certain

types of anemia and other problems

63. Ciprofloxacin 85721-33-1

API

It is used to treat bacterial

infections, such as:

chest infections (including

pneumonia) skin

of 232


Page 134 of 232

and bone infections.

64. Praziquantel 55268-74-1

API anthelmintics

65. Ramipril 87333-19-5

API Anti Hypertensive

66. Lisinopril 83915-83-7


67. Eszopiclone 138729-

47-2 API Insomnia

68. Nebivolol 99200-09-6


69. Ipratropium

Bromide 7726-95-6

API

Ipratropium is used to control

and prevent symptoms

(wheezing and shortness of

breath) caused by ongoing lung

disease (chronic obstructive pulmonary disease-

COPD which includes bronchitis and emphysema).

70. Captopril 62571-86-2

API Anti-Hypertensive

R&D activity, pilot batches

- -

- - - -







(Rs. in Crores):

Existing

Proposed

Total

7.048 Crores 15 Crores 22.048 Crores


Details Existing

(Rs. In Crores)

Proposed

(Rs. In

Total

(Rs. In

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Page 135 of 232

Crores) Crores)

Land 0.25 0 0.25

Building 1.75 5 6.75

Machinery 3 7.124 10.124

EMP 2.018 0.936 2.954

Miscellaneo

us 0.03 1.94 1.97

Total 7.048 15 22.048


Pollution control equipment

Cost in Lac Recurring

Cost (Rs. In

Lac /Annum)

Remarks

Air Pollution

75 12

Capital cost would include air pollution

control devices and the recurring cost would

include operation and maintenance of

pollution control devices and stack

emission/AAQ monitoring & sample analysis

charges.

Water Pollution

134 30.4

Capital cost would include cost of ETP units

etc. and the recurring cost would include

maintenance charges, manpower salary,

sample analysis charges etc.

Noise pollution

0.15 0.36

Capital cost would include providing

adequate sound enclosures and recurring

cost would include monitoring of noise level.

Hazardous / solid waste

management

5.5 586.27

Capital cost would include expense for

providing storage area for hazardous waste

and for the membership of TSDF/CHWIF

site. Recurring cost would be for solid/

hazardous waste packing & its disposal &

analysis charges.

Green belt

5 1

Capital cost would include development of

green belt within and outside the project

premises and recurring cost would include

maintenance charges, manpower salary etc.

Occupational

Health & Safety

40.2 0.5

Capital cost would include cost of OHS

center, PPEs , SCADA and PLC and cost of

fire and safety equipment. Recurring cost

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Page 136 of 232

would include maintenance charges.

Fire and Safety cost

17 0.25

Capital cost include the cost of jockey pump,

fire hydrant system, and all the equipments

required to control fire and keep the safety in

the workplace

Miscellaneous

2.5 3

Miscellaneous activity such as development

of rain water harvesting system and

recurring cost would include maintenance

charges

CER 15 -- Drinking facility, Paver block, Medical camp,

solar street provision

Total 294.35 633.68

Summary

Cost of Project in Crores per Annum: 15/-


Percentage:

2.94/- and 19.6%


and Percentage:

633.68/-

A-3 Details of CER as per OM dated 01/05/2018 (In case of project falls

under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs

given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of

Environmental Clearance as per the mechanism published vide

MoEF&CC‘s OM vide 31.10.2019.)

% as per the OM

Rs. in Crores

1% 0.15


Sr. No. Activity

Year (Amount to be spent in Lakhs)

Total amount to be spent in Lakhs 1st 2nd 3rd

Safe Drinking Water Facilities

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1

Ro facility (200 liter per hour) including annual maintenance contract for drinking water in Amipura Primary Schhol (1st year) and Dahegamda Primary school (2nd year) and maintenance of the RO facility in the (3rd year).

1.2 1.2 1 3.4

Infrastructure development & Healthcare Facilities

2

Paver block facility in nearest school Amipura Primary school (1st year) & Up gradation of Toilets and Water Tank in School (2nd year)

2 2 0 4

3 Medical camp in Amipura village and distribution of medicines to needy people.

-- -- 1.6 1.6

Renewable energy

4 Solar street light (12 W) in Amipura (1st year, 25 Units), Dahegamda village (2nd year, 25 Units)

3 3 - 6

Total 6.2 6.2 2.6 15

B Land / Plot ownership details: The Land documents attached with

Fom-1

B-1 Plot area

Existing

Proposed

Total

14485 Sq. m. 0 Sq. m. 14485 Sq. m.

B-2 Brief note on Area adequacy in line to proposed project activities: The plat

area of the project is 14485 sq. m. with green belt of 4823.6 sq.m. and the

detailed plant layout with the feasibility of the capacity of production is

attached in Annexure-2

B-3 Green belt area

Existing

Proposed

(Sq. meter)

Total

(Sq. meter)

Area in

Sq. meter 4767 m2 56.6 4823.6 m2

% of total 33% --. 33.3%

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area


Existing

Proposed

Total

110 30 140

D WATER

D-1


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

Borewell


Unit has already applied for CGWA and obtained the NOC approval for

existing unit & The unit has also applied for CGWA for proposed unit.


Category

Existing KLD

Proposed (Additiona

l) KLD

Total after Expansion

KLD Remarks

( A) Domestic

5.5 2 7.5

(B) Gardening

16.5 0 16.5

(C) Industrial

RO

47 (35 KLD permeate + 12 KLD RO

reject.

RO permeate

will be used in boiler, DM plant

and cooling tower

30.5

72.5 (58 KLD permeate +

14.5 RO reject)

RO permeate will be used in

boiler and process

Boiler 2

24 26

Cooling

16.2 138.22 154.42

DM water 16.8 - -

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Process

13.7 18.3 32

Washing 2 2 4

Scrubber

1 5.6 6.6

Industrial Total

(C)

47 (out of

47 KLD, 35 KLD will be

recycled water so

fresh water requirement for industrial purpose will be 12 KLD

190.52

237.52 (Out 237.52 KLD,

59.67 KLD will be the recycled

water hence 177.85 KLD will

be the fresh water

requirement for industrial purpose.)

Total (A+B+C) 69 KLD 192.52 261.52 KLD

Recycled water 35 KLD 24.67 59.67 KLD

Fresh water requirement

34 KLD 167.85 201.85 KLD


-

Summary of water requirement

Existing KLD

Proposed (Additional)

KLD

Total after Expansion

KLD

Remarks

Total water

requirement for the project (A)

69 KLD

192.52 KLD

261.52 KLD

Quantity to be recycled (B) 35 KLD

24.67 KLD

59.67 KLD

Total fresh water requirement (C) 34 KLD

167.85 KLD

201.85 KLD

Ensure Total water requirement = Fresh water + Recycled water

i.e. A = B + C



Source of waste water for reuse 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.)


RO permeate Total 59.67 KLD from RO will be used in

industrial purpose such

Particular Ro Permeate

Quantity 59.67s

pH 6.5-7.5

RO permeate

will be used in industrial

activities

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as washing, process and

allied equipments

TDS <500

COD <250

TSS <10



D-3


Category

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(E) Domestic

4.5 1.85 6.35

(F) Industrial

RO rejected water 12 2.5 14.5

Process 18.3 3.83 22.13

Washing 2 2 4

Boiler 0.1 2.4 2.5

Cooling 1.6 13.82 15.42

Scrubber 1 3.78 4.78

Total Industrial

waste water

39.5

(Domest

ic:4.5KL

D &

Industria

l: 35

KLD)

30.18

(Domestic:

1.85 KLD &

Industrial:

28.33 KLD)

69.68

(Domestic :6.5

KLD and 63.1

KLD is

Indsutrial w/w.

Brief Note on worst case scenario for waste water generation (Qualitative and

Quantitative):

In worst case scenario maximum waste water from group A will be generated

during the production of the following

S.NO. Product Group Waste water generation (KL/day)

1 Ketoconazole A 5.1

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2 Pantoprazole Sodium B 1.6

3 Valproic Acid C 4

4 RIVAROXABAN D 3.9

5 Levetiracetam E 1.4

6 Levamisole F 0.9

7 Sertraline hcl G 3

8 Artesunate H 1.704

9 DAPAGLIFLOZIN I 0.5

Brief justification in case of no process effluent generation or no industrial

effluent generation or no high concentration effluent generation from proposed

project (Whichever is applicable).

Not applicable

D-4 Mode of Disposal & Final meeting point (Existing and Proposed)

Zero Liquid Discharge

Existing and Proposed

Domestic: Domestic waste water generated from existing and proposed unit will be

Treated in in-house ETP containing Primary, secondary and tertiary unit of

treatment

Industrial: Industrial waste water generated from existing and proposed unit will be

Treated in in-house ETP containing Primary, secondary and tertiary unit of

treatment

-

Clearly mention about final disposal: Zero Liquid Discahrge


Existing ETP units

Sr. No. Unit Size/

Capacity Quantity

1. Collection Tank -1 5.4 KL 2 Nos.

2. Ammonia Stripper 550 lit/hr 1 No.

3. Collection cum Neutralization tank-2

20 KL 2 Nos.

4. ETP 42 KLD 1 No.

5. RO 5000 lit/hr 1 No.

6. MEE/MVR 2000 lit/hr 1 No.

7. Centrifuge 1000 lit/hr 1 No.

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Details of Effluent treatment plant after expansion

Sr. No. Unit No. of units Size/ Capacity

1. Collection tank-1 2 5.4 KLD

2. Ammonia stripper 1 550 lit/hr

3. Collection cum

Neutralization tank - 1 2 20 KL

4. Solvent Stripper 1 3 m3/hr

5. Holding Tank 1 40 KLD

6. MEE 1 3 m3/hr

7. ATFD 1 1.5 m3/hr

8. Collection cum

Neutralization tank - 2 2 50 KLD

9. Primary Clarifloccutor 1 40 KLD

10. Aerobic Tank 1 40 KLD

11. Secondary Clariflocculator 1 40 KLD

12. PSF/ACF 1 4 m3/hr

13. RO-2 2 2 m3/hr

W/W generated from from industrial activities will be 68.82 KLD. The 22.13 KLD W/W stream containing Ammonical Nitrogen will be treated in ammonia

stripper and then it will be sent to ETP. 17.01 KLD high COD w/w from process, 2 KLD w/w from washings and 3.78 KLD w/w

from scrubber will be collected in collection cum neutralization tank then it will passed through solvent stripper and w/w coming from solvent stripper will be sent to MEE. Condensate water from MEE along with 11.75 KLD w/w rejected from RO, 2.4 KLD boiler blow-down and 13.82 KLD cooling tower blow down will be taken to ETP.

ETP will be consisting of collection cum neutralization tank, primary clariflocculator, aeration tank, secondary clariflocculator, PSF, ACF& RO.

Sludge generated from ETP and MEE salt will be sent to TSDF site Thus, unit will maintain Zero liquid discharged.


Capacity of STP/ Secondary treatment unit: 40 KLD



Treatment scheme including segregation at source. (Give Characteristics of each

stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP

(ETP-1, ETP-2….) for each stream shall be proposed.

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w/w

from

Scrub

ber

High

COD

strea

m

After

ammon

ia

stripper

Washi

ng

Composit

e

(Concentr

ated

Stream)

After

VOC

Stripp

er

RO

reject

Composi

te to

MEE

inlet

MEE

condensate

Quantity

(KLD) 4.78 17.01 5 4 30.79 30 15.5 45.5 36.4

pH 6.5-7.5 3.4-

4.5 4.5-5.5 6.5-7.5 4.46-5.51 6.5-7 6.5-7.5 6.5-7.17 6.5-7.5

TSS

(mg/l) 20-30

200-

250 200-250

200-

250

172.05-

215.84

120-

200 20-30 85-143 43-75

TDS

(mg/l)

1500-

2000

40000

-

45000

400000-

450000

200-

300

28852.54-

32517.37

25000

-

28000

5000-

5150

18200-

20220 900-1000

COD

(mg/l) 100-

200

50000

0-

60000

0

500000-

600000

400-

500

35800-

43000

29280

-

36510

10-20 19300-

24080 6700-8400

w/w from MEE

condensate

Dilute

stream

composi

te

Composite After

PST After SST

After

RO/perme

ate water

Quantity

(KLD) 36.4 38.7 75.1 12.6 12.6 8.8

pH 6.5-7.5 6.6-8.3 6.5-7.9 6.5-7.5 6.5-7.5 6.5-7.5

TSS

(mg/l) 43-75 100-190 70-130 30-40 10-20 <10

TDS

(mg/l) 900-1000

1920-

2390 1430-1720 1250-1440 450-470 <500

COD

(mg/l) 6700-8400 185-360 3370-4270 1000-1200 200-240 <250


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Page 144 of 232

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


W/W generated from from industrial activities will be 68.82 KLD. The 22.13 KLD W/W stream containing Ammonical Nitrogen will be treated in ammonia

stripper and then it will be sent to ETP. 17.01 KLD high COD w/w from process, 2 KLD w/w from washings and 3.78 KLD w/w

from scrubber will be collected in collection cum neutralization tank then it will passed through solvent stripper and w/w coming from solvent stripper will be sent to MEE. Condensate water from MEE along with 11.75 KLD w/w rejected from RO, 2.4 KLD boiler blow-down and 13.82 KLD cooling tower blow down will be taken to ETP.

ETP will be consisting of collection cum neutralization tank, primary clariflocculator, aeration tank, secondary clariflocculator, PSF, ACF& RO.

Sludge generated from ETP and MEE salt will be sent to TSDF site Thus, unit will maintain Zero liquid discharged.

D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer,

Common MEE, CHWIF etc.


Project proponent already have TSDF Provisional certificate from BEIL

Membership of Common facility (CF) mentioning total capacity, consented

quantity, occupied capacity and spare capacity and norms of acceptance of

effluent from member units in-line with the direction given by GPCB vide Letter No.

GPCB/P-1/8-G (5)/550706 dated 08/01/2020.


(Existing and Proposed)

Existing:

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After expansion

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Page 146 of 232

E AIR

E-1 Brief Note on fuel based Heat energy requirement and worst case

scenario there of:

Coal/Briquettes will be used for heat energy. The GCV of coal is 4500

kcal/hr.


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

MT/hr, KVA etc.

(In case of Project located within CPA/SPA , APCM shall be in line to the

mechanism published in the MOEFCC‘s OM vide dated 31.10.2019)

Existing & Proposed

Flue gas emission from existing unit

Sr.

No.

Stack

attached to

Stack

Height

(m)

Fuel

Requirement APC System

Expected

Pollutant

1 Steam Boiler

(1*1 TPH) 30

Coal/Briquette

s

(1 MT/day)

Cyclone

separator

followed by

Bag collector

SPM: <150 mg/Nm3

SO2: <100 ppm

NOx: <50 ppm

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2 D.G.Set

(1*125 kVA) 6.5

HSD

(21 Lit/hr.)

Adequate

stack height

Sr.

No. Stack attached to Status

Stack

Height

Fuel

Requireme

nt

APC System

Expecte

d

Pollutant

1 Steam Boiler

(1*1 TPH) Existing 30 m

Coal/Briquet

tes

(1 MT/day)

Cyclone

separator

followed by

Bag collector

SPM

150

mg/Nm3

SO2

100 ppm

NO2 50

ppm

2 Steam Boiler

(2*4 TPH) Proposed

Common

Stack of

30 m

Coal/Briquet

tes

(15 MT/day)

Multi-cyclone

separator

followed by

bag filter

followed by

water scrubber

3

Thermic fluid

Heater

(2 nos.)

(1*1000000 Kcal/hr.

& 1*600000

Kcal/hr.)

Proposed

Common

Stack of

30 m

Coal/Briquet

tes

(2 MT/day)

Multi-cyclone

separator

followed by

bag filter

followed by

water scrubber

4

D.G.Set

(1*125 kVA)

(1*250 kVA)

(1*500 kVA)

Existing

&

Proposed

6.5 m

H.S.D.

(21 Lit/hr.)

(50 Lit/hr.)

(100 Lit/hr.)

Adequate stack

height


Existing

Sr. No.

Stack attached to

Height of the stack

APC System Expected Pollutant

1 Glimepiride 12 m Common duct to Caustic

scrubber Adequate

HCL

2 Carbidopa 12 m SO2

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3 Folic acid 12m stack height

H2S

After expansion

Sr.

No.

Stack

attached to

Height

of the

stack

APC System Expected

Pollutant

1

Reactor

vessel

(30 nos.)

12 m

Dual Condenser System on each

Reactor (water + Brine) followed by

dual stage Scrubber (Primary water

+ secondary alkali media) followed

by activated carbon column

HCL, VOCs

2

Reactor

vessel

(8 nos.)

12 m



dual stage Scrubber (Primary water

+ secondary acidic media) followed

by activated carbon column

NH3, VOCs

3

Reactor

vessel

(15 nos.) &

suction hood

to Bromine

handling area

12m



dual stage Scrubber (Primary

water + secondary alkali media)

followed by activated carbon

column

SO2,

Cl2, HBr, H2S,

VOCs

4

Reactor

vessel

(57 nos.)

12 m

Dual stage condenser system

(primary cooling water circulation

and second Brine chilled media

circulation) followed by the

Activated carbon column

VOCs

5 Dryer 12 m Activated carbon column VOCs

Note:

Details of gaseous raw materials used in proposed project : Yes, Bromine, chlorine,

hydrogen gas are going to be used as raw material

Estimation of process gas emission (Product wise and Total): There will be the

chances of emission of HCL, NH3, SO2, Br2, H2S, CL2

Requirement of the scrubbing media (KL per Day) considering solubility (Product

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Page 149 of 232

wise and total): For Ammonia, media used in scrubber will be 670.4 l/day for HCl it will

be 1037 l/day, Cl2 it will be 2166.4, for SO2 it will be 514.4 l/day, H2S it will be 7.2 l/day,

Br2 it will be 1099.5 l/day. So total will be = 5.6 kl/day scrubbing media is required.

Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and



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.

Note:




Quantification of hazardous waste shall be based on mass balance

and calculations shall be incorporated in EMP details separately.



Existing & Proposed

Sr. No.

Description Category

Existing

Proposed

Total Quantity (MT/Annum)

Mode of Disposal

1 ETP Sludge 35.3 252 42.17 294.17 Collection, storage, transport and disposal at approved TSDF site.

2 Process Residue / Process Sludge

28.1 - 829.7 829.7

Collection, Storage, Transportation (Through GPS mounted vehicles) and Disposal by sending to registered recycler for regeneration /for co-processing/ Incinerated

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Page 150 of 232

at CHWIF.

3 Spent Carbon(process)

28.3 79.6 3400.2 3479.8

Collection, Storage, Transportation and Incinerated at CHWIF/ for co-processing


20.3 641.5 7269.54

7911.04

Collection, Storage, Transportation (Through GPS mounted vehicles) and Disposal by sending to registered recycler for regeneration /for co-processing/Incinerated at CHWIF.

5 Off Specification Drugs

28.4 5 1 6 Collection, Storage, Transportation and Incinerated at CHWIF.

6 Date Expired Product

28.5 48 1 49 Collection, Storage, Transportation and Incinerated at CHWIF.

7

Spent Solvent 28.6 22.6 27.4 50

Collection, Storage, Transportation and Incinerated at CHWIF/ for co-processing

Spent Solvent 28.6 - 67729.64

67729.64 Collected, Treated and Recover& Reuse in the next batch.

8 Spent Catalyst 28.2 215.3 215.3 Collection, Storage, Transportation and Incinerated at CHWIF.

9 Bleed liquor 35.1 - 302.13 302.13 Collection, Storage, Transportation and Incinerated at CHWIF.

10 Used Oil 5.1 0.1 3 3.1

Collection, storage and used within premises as a lubricant / sold to registered recycler.

11 Discarded Plastic Bags / Barrels / Liners

33.3 28.6 50 78.6 Collection, storage & sold to registered recycler.

12 Bleed Liquor 35.1 - 832.22 832.22 Collection and sent to ETP for further Treatment

-


(For HW management)

Unit will apply for TSDF site membership

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Page 151 of 232


The unit will send the w/w to common facility at the time of maintenance of ETP and

MEE and unit will apply for the same after getting EC.


(MSW and others)

Sr. no.



Quantity (MT/Annum)


Existing Proposed Total

1 Municipal solid waste

18 7.2 25.2 Treated in in-house ETP


G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery,

reuse of recovered Solvents etc.

Sr. No.

Raw Materials Comsumpt

ion Mt/M Recovered

Mt/M % Recovery

1. Acetone 903 777 86.05

2. Acetonitrile 654.5 620.4 94.79

3. Benzene 9.4 8.4 89.36

4. Butanol 10 9.7 97.00

5. Chloroform 213.76 195.75 91.57

6. Cyclohexane 678.6 644.6 94.99

7. Dimehtyl Sulfoxide (DMSO)

217 201.8 93.00

8. Dimethyl

formamide (DMF)

116.1 112.1 96.55

9. Ethanol 246.5 222.2 90.14

10. Ethyl Acetate 3156.4 2861.1 90.64

11. Ethylene diamine

27 26 96.30

12. Heptane 15.2 14.89 97.96

13. Hexane 99.16 92.9 93.69

14. Isopropyl alcohal

735.8 690.46 93.84

15. Methyl Ethyl

ketone (MEK) 70.29 67.76 96.40

16. Methanol 2541.1 2416.11 95.08

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Page 152 of 232

17. Methyl Isobutyl Ketone (MIBK)

150 142.51 95.01

18. Methylene dichloride

(MDC) 2489.21 2320.98 93.24

19. O-xylene 41.32 39.88 96.52

20. Pyridine 100.27 96.25 95.99

21. Tetra Hydro Furan (THF)

585.17 556.08 95.03

22. Toluene 1650.2 1502.5 91.05

23. Triethylamine 100 96 96.00

24. 1-4 dioxane 105 98.7 94.00

25. Acetic acid 93.9 86.1 91.69

26. Diethyl ether 80 76 95.00

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.


Components Average quantity

Average Uncontrolled

VOC Emissions (ton/year)

Percentage of total emission

Preventive Measures

Pumps 8 1.52 7.36

-Use Sealless design -Use Dual mechanical seal with barrier fluid maintained at a higher pressure than the pumped fluid -Provide Closed-vent system -Use Spare pumps at the time of repair. Tightening the packing glands. The pump will be flushed of VOC as much as possible before opening for seal replacement.

Valves 90 4.96 24.03

-Use Sealless design. -Plug type valves can be lubricated with grease to reduce emissions. Many valves have no means of in-service repair and must be isolated from the process.

Connectors 150 2.51 12.17

-Weld together -In some cases, leaks from flanges can be reduced by replacing the flange gaskets.

Open ended lines

90 1.45 7.00 -It can be controlled by using Blind, cap, plug, or second

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Page 153 of 232

valve and flanges.

Sampling Connections

50 6.88 33.29 -Provide Closed-loop sampling

Pressure relief valves

60 3.33 16.14

-Provide Closed-vent system. -Installation of a rupture disk in the line prior to relief valve Connection of the discharge port of the relief valve to a closed vent system use of Soft seat technology such as elastomer "0-rings.


Unit has provided the dryer attached to reactors for controlling the VOC emission

H SAFETY details



Details of raw material storage and hazardous chemicals are included in risk

assessment report, which is attached with form-1.

Sr. no Name of Chemical Capacity of

Tank

Number of

Tanks

Hazardous

Characteristi

cs of

Chemical

1 - - - -

2 - - - -

3 - - - -


Not applicable

Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum,

Barrels, Carboys, Bags etc.

Details of raw material storage and hazardous chemicals are included in risk

assessment report which is attached with form-1

Safety details of Hazardous Chemicals: Detailed of hazardous chemicals and its

safety measures are included in risk assessment report which is attached with Fomr-1

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Page 154 of 232

Type of

Hazardous

Chemicals

Safety measures

- -

- -

Applicability of PESO : Unit will obtain permission from PESO department After

getting EC


(Hydrogenation process, Nitration process, Chlorination process,

Exothermic Reaction etc.)

-

Type of

Process


Nitration Fire / explosion occurred during the nitration process.

Control measures:

Nitration is exothermic reaction leads to runaway reaction. So, entire process of nitration is to be followed as per standard operating procedure established by industry.

All engineering controls w.r.t nitration process i.e. temperature and pressure controller, jacket surrounding to reactor etc. will be provided.

Chilled water to control exothermic reaction during nitration. NOx fumes will be scrubbed in ventury Scrubber from the Nitration

reactor. Only trained person will be allocated for handling nitration process. Programmable Logic Controller (PLC) based control plan will be

provided for Nitration. Direct Contact with skin and eyes will be avoided. Appropriate personal protective equipment‘s like Safety Gloves,

Goggles, shoes etc., will be provided to workers. Periodically inspection of scrubber system will be carried out

Bromination Toxic flames/ explosion occurred during the bromination process.

Control Measures:

Bromination is exothermic reaction leads to runaway reaction. So, entire

process of bromination is to be followed as per standard operating

procedure established by industry.

All engineering controls w.r.t bromination process i.e. temperature and

pressure controller, jacket surrounding to reactor etc. will be provided.

Chilled water to control exothermic reaction during bromination

Exothermic

reaction

Fire/Explosion

Control Measures:

Exothermic reaction leads to runaway reaction. So, entire process is to

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be followed as per standard operating procedure established by industry.

All engineering controls w.r.t exothermic reaction i.e. temperature and pressure controller, jacket surrounding to reactor etc. will be provided.

Chilled water circulation to control exothermic reaction. Only trained person will be allocated to operate. Programmable Logic Controller (PLC) based control plan will be

provided. Appropriate personal protective equipment‘s like Safety Gloves,

Goggles, shoes etc., will be provided to workers.

Hydrogenati

on

Improper handling of cylinders Control Measures: Separate hydrogenation plant will be provided to carryout hydrogenation

reaction.

Hydrogen gas will be transferred from cylinder to reactor through closed transfer system.

Hydrogenation process is exothermic reaction process so temperature and pressure will be maintained to control the rate of reaction.

All the precautions will be followed as per statutory guideline. SOP will be made available to handle hydrogenation process Adequate scrubbing system will be for Hydrogen gas Only trained person will be allow to access in hydrogenation plant. Appropriate PPEs will be provided for person working in hydrogenation

plant


-

Total Plot Area: 14485 sq.m.

Area utilized for plant activity: 17958.00 sq.m.

Area utilized for Hazardous Chemicals

Storage:

1797.00 sq.m.

Number of Floors: There will be ground floor and 1st,2nd floor and terrace will be provided.

Water requirement for firefighting in KLD :

49.5125 KLD

Water storage tank provided for firefighting

in KLD:

170 KL

Details of Hydrant Pumps: Yes, 2 electrical pump (180 lit/min) and 1 diseal pump (2280 lit/min) at 7 kg /cm2 pressure. Yes , one trailer Pump

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of 1600 lit/Min at 7 Kg/cm2 pressure.

Nearest Fire Station : Bavla & Prahladnagar Fire Station disctance from project site is 13 Km & 38 km respectively

Applicability of Off Site Emergency Plan: Shown in Risk Hazards report.

-

H-4 Details of Fire NOC/Certificate: Unit will apply after getting EC


-



Area provided for OHC: 15 m2


Nearest General Hospital : Parekh hospital

bavla is 13 Km

away from project

site

Name of Antidotes to be store in plant : 10



Project proponent (PP) and Technical expert of PP, M/s. T.R. Associates remains present during video

conference meeting.

This is an existing unit and now proposes expansion for API and Its Intermediates plant at Vill- Amipura,

Ta- Bavla, Dist- Ahmedabad, located outside notified area. Source of water supply is Bore well.

Committee asked for status of CGWA permission for ground water source, PP informed that they will

apply for CGWA permission. PP submitted Google map showing that there is no any water bodies,

villages, School, monuments etc. within 500 m radius of the project site. There are no Eco sensitive

zones, wild life sanctuaries within the 10 km area from the boundary of the project site.

Product profile along with End Use discussed in depth. Committee noted that PP has addressed area

adequacy for proposed project with layout plan. PP has submitted EC and its self compliance report and

informed that they have still not started plant and not converted existing EC in CTO order.

Committee noted that effluent stream segregation will be carried out. High COD effluent from Process

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will be treated in primary treatment plant, ETP-1 followed by solvent stripper and Ammonia stripper.

Treated effluent will be evaporated in in-house MEE. Low COD stream will be treated in ETP-2 followed

by RO plant. RO reject will be evaporated in in-house MEE. MEE condensate and RO permeate will be

reused back in process.

Committee noted that coal and briquette will be used as fuel for boilers and thermo pack. Multi Cyclone,

bag filter and water scrubber as APCM will be attached with boilers and thermo pack separately. Two

stage scrubbers will be provided as APCM with each process stacks. Technical expert addressed

hazardous waste management including scrubber bleed liquor and spent solvent disposal.

Committee noted that PP has addressed LDAR and solvent recovery, green belt development, EMP and

CER for proposed project. PP explained regarding safety control measures for process hazard and

Hazardous chemical storage and its management. Committee discussed in length regarding fire hydrant

system, evacuation plan, storage and safety measures of hazardous chemicals and Risk assessment for

Hazardous chemicals considering worst case scenario.

Since, the unit falls in B2 category as per the MoEF&CC‘s amended EIA Notification vide S.O. 1223(E)

dated 27.03.2020, the public consultation is not applicable as per paragraph 7(i) III (i) (e) of the

Environment Impact Assessment Notification-2006.

Committee found that presentation and documents submitted by Project Proponent satisfactory.


Gujarat for grant of Environment Clearance with the following specific condition.


1) PP shall comply conditions of any subsequent amendment or expansion or change in product

mix, after the 30th March 2021, considered as per the provisions in force at that time as

mentioned in the Notification vide S.O. 1223 (E) dated 27/03/2020 and S.O. 3636 (E) dated

15/10/2020.

2) PP shall carry out proposed project/activities in respect of Active Pharmaceutical Ingredients

(API) as per the amended EIA Notification vide S.O. 1223 (E) dated 27/03/2020 and any

subsequent amendments.

3) PP shall submit six monthly compliance report of Environmental Clearance without fail and the

same shall be critically assessed by the regulatory authority.

4) Wastewater shall be fed to in-house MEE only after providing adequate treatment in such a way

that no pollutant get air borne during evaporation to avoid adverse impact on Human Health &

Environment.

5) Unit shall obtain all required permissions from the Narcotics Control Bureau for manufacturing,


6) Close loop solvent recovery system with adequate condenser system shall be provided to recover


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7) Leak Detection and Repair (LDAR) program shall be prepared and implemented as per the CPCB


8) PP shall maintain Complete Zero Liquid Discharge [ZLD] status all the time and there shall be no

drainage connection from the premises and no wastewater discharge outside premises by any

means.

9) (a) R & D products shall be of similar chemistry in line with the EIA Notification vide S.O. 1223 (E)

dated 27/03/2020 and the pollution load shall remain the same as committed. (b) Project

proponent shall not take continuous/commercial production of the R & D materials. Necessary

approvals shall be obtained from the concern authorities prior to commercial production of R & D

materials. (c) Unit shall submit relevant details of R & D products like raw materials, its safety

measures to the regulatory authority well before R & D activity. (d) Unit shall submit relevant

details of R & D products like different wastes generated (Quantity & Quality) and its management

to the regulatory authority within a month of R & D activity.

10) The unit shall submit the list of authorized end users of hazardous wastes along with MoU signed

with them at least two months in advance prior to the commencement of production. In the

absence of potential buyers of these items, the unit shall restrict the production of the respective

items.

11) Unit shall strictly Compliance of ODS (Ozone Depleting Substances) Rules 2000 and its

amendments time to time for use of ODS chemicals as raw material in proposed project.

12) PP shall obtain CGWA permission for ground water source i.e. bore well within premises before

start production activity.

13) Domestic wastewater generation shall not exceed 6.35 KL/day for proposed project and it shall

be treated in ETP. It shall not be disposed off in soak pit and septic tank.

14) Unit shall provide buffer water storage tank of adequate capacity for storage of treated waste

water in case of any shut down of MEE.

15) Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB directions to all


emission as per pollutants discharge/emission from respective project and an arrangement shall

also be done for reflecting the online monitoring results on the company's server, which can be



16) The PP shall develop green belt within premises (4823.6 m2 i.e. 33 % of the total plot area) as per

the undertaking submitted before SEAC. Green belt shall be developed with native plant species

that are significant and used for the pollution abatement as per the CPCB guidelines. It shall be


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17) Safety & Health:

a) PP shall provide Occupational Health Centre (OHC) as per the provisions under the Gujarat


b) PP shall obtain fire safety certificate / Fire No-Objection certificate (NOC) from the concern


2016.

c) Unit shall adopt functional operations/process automation system including emergency


d) PP shall carry out mock drill within the premises as per the prevailing guidelines of safety and


accident.

e) PP shall obtain PESO permission for the storage and handling of hazardous chemicals. (If

applicable)

f) Flame proof electrical fittings shall be provided in the plant premises, wherever applicable.

g) PP shall install adequate fire hydrant system within premises and separate storage of water

for the same shall be ensured by PP.

h) PP shall take all the necessary steps for control of storage hazards within premises ensuring



i) PP shall take all the necessary steps for human safety within premises to ensure that no any


j) Unit shall store Bromine Bottle in cool dry separate area, out of direct sunlight.

k) Unit shall provide water sprinkler to the ammonia storage drum/barrel.

l) Unit shall provide safety valve and rupture disc with hydrogenation reactors.

m) Unit shall provide safety valve and rapture disc, as well as auto dump or auto quench/,

suppress system for nitration vessel and exothermic reaction vessel safety.

n) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam


8. SIA/GJ/IND2/173537/2020 M/s. Adarsh Dye Chem (Unit-II)

Plot No. A-1/3621 & 3620, Opp. ETL, GIDC

Estate Ankleshwar, Dist.: Bharuch

Appraisal

Project proponent (PP) submitted application by proposal no- SIA/GJ/IND2/173537/2020 for obtaining

Environmental Clearance.

Project proponent (PP) has e-mail, requesting for withdrawal of Environmental Clearance application

vide e-mail on dated 14/12/2020.

Proposal was considered in the SEAC meeting dated 17/12/2020.

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During SEAC meeting dated 17/12/2020, Committee noted that PP stated reason for withdraw the

Environmental Clearance application for the proposed project.

PP submitted that, they have changed mode of disposal from In house ZLD to NCTL for CETP discharge

in this expansion proposal. However, they have not yet received booked effluent load certificate.

In view of the above, Committee decided to recommend to permit project proponent for

withdrawal of their application of Environmental Clearance and to delist the proposal from the list

of pending applications & to close the file.

9. SIA/GJ/IND2/173557/2020 M/s. Zeni Healthcare

Plot No. C-349, GIDC- Saykha, Ta:Vagara,

Dist.: Bharuch

Appraisal


Project status: New







tabulated below,

Sr. No.


API OR INTERMEDIATE

CAS no. Quantity

MT/Month *End-use of products

1.

Alpha Ketoanalogue to Isoleucine Calcium Salt

API 51828-96-7

150 MT/MONTH

API / Nutritional Supplement for kidney disease

2.

Alpha Ketoanalogue

to Leucine Calcium Salt

API 51828-95-6

3.

Alpha Ketoanalogue

to Phenylalanine Calcium Salt

API 51828-93-4

4.

Alpha Ketoanalogue

to Valine Calcium Salt

API 51828-94-5

5.

Alpha Hydroxy Methionine

Calcium Salt API 4857-44-7

6. Iron Sucrose API 8047-67-4 API / Increase Haemoglobin

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Page 161 of 232

7. Diacerein API 13739-02-1 API /used to

treat joint diseases

8. Tolfenamic

Acid API 13710-19-5 API / Chronic Pain

9. Diosmin API 520-27-4 API / Varicose Veins

10.

1,2,4 Triazolo [4,3-A] Pyridin-3-One (T.P.O)

Intermediate 6969-71-7 Trazodone HCl/

treat CNS

11. Ferric Carboxy

Maltose API 9007-72-1

API/ Increase Haemoglobin

12. Sucroferric

Oxyhydroxide API 12134-57-5


13. Couple Amine Hydrochloride

Intermediate 141109-19-

5

Clopidogrel Bisulphate/preventin

g strokes 14. Azithromycin API 83905-01-5

API/Respiratory System

15. Clarithromycin API 81103-11-9

16.

Erythromycin Ethyl-

Succinate API 1264-62-6

17. Erythomycin

Stearate API 643-22-1

18. Roxithromycin API 80214-83-1

19. Ciprofloxacin Hydrochloride

API 86393-32-0

API/Infection of Lungs 20. Levofloxacin API

100986-85-4

21. Ofloxacin API 82419-36-1

22.

Alpha Ketoanalog to

Isoleucine Magnesium

Salt

API 1560-54-9

API/ Nutritional Supplement for kidney disease

23.

Alpha Ketoanalog to

Leucine Magnesium

Salt

API 816-66-0

24.

Alpha Ketoanalog to

Methionine Magnesium

Salt

API 59-51-8

25.

Alpha Ketoanalog to Phenylalaine Magnesium

Salt

API 150-30-1

26.

Alpha Ketoanalog to

Valine Magnesium

Salt

API 516-06-3

27. Ketoconazole API 65277-42-1 API/skin infection

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Page 162 of 232

28. Quetiapine

Hemifumarate API

111974-72-2

API/schizophrenia

29. 2-(Phenylthio) benenamine

Intermediate 1134-94-7

Quetiapine Hemifumarate/ schizophrenia

30.

Phenyl 2-(Phenylthio)

phenylcarbamate


3

31.

Dibenzo[b,f][1,4] thiazepine-11-(10H)one


32.

1,1-piperazinyl-dibenzo[b,f]

[1,4] thiazepine


4

33. Acyclovir API 59277-89-3 API/cold Sores

34.

Diacetylacyclovir(9-[(2-

Acetoxyethoxy)methyl] -N2-acetylguanine

Intermediate 59278-00-1 Acyclovir/Cold sores

35. Telmisartan API 144701-48-

4

API/treat high blood pressure strokes, Kidney problem

36.

Methyl 4 bromomethyl biphenyl-2-carboxylate


2

Telmisartan/ treat high blood pressure

strokes, Kidney problem

37. Telmisartan Methyl Ester


2

38. Sulindac API 38194-50-2 API/treat high blood pressure strokes, Kidney problem

39.

3.-(4-Floro Phenyl) 2-

Methyl Propionic Acid


Sulindac /treat high blood pressure strokes, Kidney

problem

40.

6-Flouro-2-Methyl 2-3-dihydro-1H-indon-1-one


41.

5-fluro-2-methylindene-

3-Acid Intermediate 399-72-4

42. Sulindac Acid Intermediate 38194-50-2

43. Irbesartan API 138402-11-

6

API/treat high blood pressure strokes, Kidney problem

44.

4‘-Bromomethyl-

2-Cyanobiphenyl


2 Irbesartan/ treat

high blood pressure strokes, Kidney

problem 45.

4‘((2-Butyl-4-Oxo-1,3-


8

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Page 163 of 232

diazaspirol[4,4]non-1-en-3-yl)methyl)-

[1,1‘-biphenyl]-2-carbonitrile

46. Irbesartan

Crude Intermediate

138402-11-6

47. Valacyclovir

Hydrochloride API

124832-27-5

API/cold sores

48.

N-[(benzayloxy)c

arbonyl]-L-valine-2-[2-amino-1,6-

dihydro-6-oxo-9H-purin-9-yl) methoxy] ethyl

ester


1 Valacyclovir

Hydrochloride/cold sores

49. Valacyclovir

acid Intermediate

124832-26-4

50.

6-Amino-2,4-dihydroxy-5-

nitrosopyrimidine

Intermediate 5442-24-0 Uracil/synthesis of

enzymes in the body

51. Phenyl

Acetonitrile Intermediate 83552-81-2

Peniciline G/ Antibiotic

52. Phenyl Acetic

Acid API 103-82-2 API/Antibiotic

53.

Tetra Butyl Ammonium

Bromide API 1643-19-2

API/Levitrasetam Phase transfer

catalyst

54. Tramadol

Hydrochloride API 27203-92-5 API /Painkiller

*R&D 100 Kg/Month

TOTAL 150 MT/Month

ENDUSE OF PROPOPOSED PRODUCTS

Sr. No.

Name of the Product CAS No. (Product)

Type/ Category of Product (API/ Intermediate)


Said API is used for/End Use of said API


Name of API in which Intermediate Used/ End use of said Intermedi

CAS no. (API)

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ate

1. Alpha Ketoanalogue

to Isoleucine Calcium Salt

51828-96-7

API - - - API / Nutritional

Supplement for kidney disease

2. Alpha Ketoanalogue to Leucine Calcium

Salt

51828-95-6




to Phenylalanine Calcium Salt

51828-93-4




to Valine Calcium Salt 51828-94-5



5. Alpha Hydroxy

Methionine Calcium Salt

4857-44-7



6. Iron Sucrose 8047-67-

4 API - - -

API / Increase Haemoglobin

7. Diacerein 13739-02-1

API - - - API /used to treat joint

diseases

8. Tolfenamic Acid 13710-19-5

API - - - API / Chronic Pain

9. Diosmin 520-27-4 API - - - API / Varicose Veins

10. 1,2,4 Triazolo [4,3-A] Pyridin-3-One (T.P.O)

6969-71-7

Intermediate of API

n-1 Trazodon

e HCl 25332-39-2

Trazodone HCl/ treat CNS

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11. Ferric Carboxy

Maltose 9007-72-

1 API - - -


12. Sucroferric

Oxyhydroxide 12134-57-5

API - - - API/ Increase Haemoglobin

13. Couple Amine Hydrochloride

141109-19-5

Intermediate of API

n-1

Clopidogrel

Bisulphate

120202-66-6

Clopidogrel Bisulphate/preventing

strokes

14. Azithromycin 83905-01-5

API - - - API/Respiratory System

15. Clarithromycin 81103-11-9


16. Erythromycin Ethyl-

Succinate 1264-62-

6 API - - - API/Respiratory System

17. Erythomycin Stearate 643-22-1 API - - - API/Respiratory System

18. Roxithromycin 80214-83-1


19. Ciprofloxacin Hydrochloride

86393-32-0

API API/Infection of Lungs

20. Levofloxacin 100986-

85-4 API - - - API/Infection of Lungs

21. Ofloxacin 82419-36-1

API - - - API/Infection of Lungs

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22. Alpha Ketoanalog to

Isoleucine Magnesium Salt

1560-54-9

API - - - API/ Nutritional


23. Alpha Ketoanalog to Leucine Magnesium

Salt 816-66-0 API - - -

API/ Nutritional Supplement for kidney

disease


Methionine Magnesium Salt

59-51-8 API - - - API/ Nutritional



Phenylalaine Magnesium Salt

150-30-1 API - - - API/ Nutritional


26. Alpha Ketoanalog to Valine Magnesium

Salt 516-06-3 API - - -

API/ Nutritional Supplement for kidney

disease

27. Ketoconazole 65277-42-1

API - - - API/skin infection

28. Quetiapine

Hemifumarate 111974-

72-2 API - - - API/schizophrenia

29. 2-(Phenylthio) benenamine

1134-94-7

Intermediate of API

n-4

Quetiapine

Hemifumarate

111974-72-2


30. Phenyl 2-(Phenylthio)

phenylcarbamate 111974-

73-3 Intermediate

of API n-3

Quetiapine

Hemifumarate

111974-72-2


31. Dibenzo[b,f][1,4] thiazepine-11-

(10H)one

3159-07-7

Intermediate of API

n-2

Quetiapine

Hemifumarate

111974-72-2


32. 1,1-piperazinyl-

dibenzo[b,f] [1,4] thiazepine

111974-74-4

Intermediate of API

n-1

Quetiapine

Hemifumarate

111974-72-2


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33. Acyclovir 59277-89-3

API - - - API/cold Sores

34.


Acetoxyethoxy)methyl] -N2-acetylguanine

59278-00-1

Intermediate of API

n-1 Acyclovir 59277-89-3

Acyclovir/Cold sores

35. Telmisartan 144701-

48-4 API - - -

API/treat high blood pressure strokes, Kidney

problem

36.

Methyl 4 bromomethyl biphenyl-2-carboxylate

114772-38-2

Intermediate of API

n-2 Telmisart

an 144701-48-4

Telmisartan/ treat high blood pressure strokes,

Kidney problem

37. Telmisartan Methyl

Ester 528560-

93-2 Intermediate

of API n-1

Telmisartan

144701-48-4

Telmisartan/ treat high blood pressure strokes,

Kidney problem

38. Sulindac 38194-50-2

API - - - API/treat high blood

pressure strokes, Kidney problem

39. 3-(4-Floro Phenyl) 2-Methyl Propionic Acid

22138-73-4

Intermediate of API

n-4 Sulindac 38194-50-2

Sulindac /treat high blood pressure strokes,

Kidney problem

40. 6-Flouro-2-Methyl 2-

3-dihydro-1H-indon-1-one

37794-19-7

Intermediate of API

n-3 Sulindac 38194-50-2


Kidney problem

41. 5-fluro-2-

methylindene-3-Acid 399-72-4

Intermediate of API

n-2 Sulindac 38194-50-2


Kidney problem

42. Sulindac Acid 38194-50-2

Intermediate of API

n-1 Sulindac 38194-50-2


Kidney problem

43. Irbesartan 138402-

11-6 API - - -

API/treat high blood pressure strokes, Kidney

problem

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44. 4‘-Bromomethyl-2-

Cyanobiphenyl 114772-

54-2 Intermediate

of API n-3

Irbesartan

138402-11-6

Irbesartan/ treat high blood pressure strokes,

Kidney problem

45.

4‘((2-Butyl-4-Oxo-1,3-diazaspirol[4,4]non-1-en-3-yl)methyl)-[1,1‘-

biphenyl]-2-carbonitrile

138401-24-8

Intermediate of API

n-2 Irbesarta

n 138402-11-6


Kidney problem

46. Irbesartan Crude 138402-

11-6 Intermediate

of API n-1

Irbesartan

138402-11-6


Kidney problem

47. Valacyclovir

Hydrochloride 124832-

27-5 API - - - API/cold sores

48.

N-[(benzayloxy)carbonyl]-L-valine-2-[2-amino-1,6-dihydro-6-oxo-9H-purin-9-yl) methoxy]

ethyl ester

124832-31-1

Intermediate of API

n-2

Valacyclovir

Hydrochloride

124832-27-5

Valacyclovir Hydrochloride/cold sores

49. Valacyclovir acid 124832-

26-4 Intermediate

of API n-1

Valacyclovir

Hydrochloride

124832-27-5

Valacyclovir Hydrochloride/cold sores

50. 6-Amino-2,4-dihydroxy-5-

nitrosopyrimidine

5442-24-0

Intermediate of API

n-1 Uracil 66-22-8 Uracil/synthesis of

enzymes in the body

51. Phenyl Acetonitrile 83552-81-2

Intermediate of API

n-1 Peniciline

G - Peniciline G/ Antibiotic

52. Phenyl Acetic Acid 103-82-2 API - - - API/Antibiotic

53. Tetra Butyl

Ammonium Bromide 1643-19-

2 API - - -

API/Levitrasetam Phase transfer catalyst

54. Tramadol

Hydrochloride 27203-92-5

API - - - API /Painkiller

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Sr. no.

Particulars Details


Total Project

8.92Crores



Land 2.50

Building 2.00

Machinery 2.50


Sr. No

Unit Detail

Capital Cost

(Rs. In Lakhs)

Operating Cost/ Month (Rs. In Lakhs)

Maintenance Cost /

Month (Rs. In Lakhs)

Total Recurring Cost / Month (Rs. In Lakhs)

1 Waste Water

ETP: 68 KLD + Stripper: 65 KLD

80.00 27.95 2.80 30.75

Membership 1.00 6.45 6.45

2 Air & LDAR

4 No. Scrubber, 1 No. MCS,

Cyclone, Bag Filter & Water

Scrubber

30.70 0.77 0.38 1.15

3 Hazardous

Management

Membership & Disposal + Incineration

1.00 8.10 - 8.10

Transportation - 0.08 - 0.08

4 Fire & Safety

Fire Hydrant & pipeline System

19.10 0.10 0.05 0.15

Safety equipment/PPES

6.75 0.02 0.01 0.03

Fire Extinguisher & Foam Trolley

4.36 0.05 0.10 0.15

Integrated DCS 20.00 1.00 0.02 1.02

Trailer Driven Pump (6000

LPM) 4.00 0.05 0.10 0.15

5 AWH

Monitoring In House

Monitoring 1.50 0.20 0.05 0.25

6 Green Belt

Development 632 Trees 3.48 0.35 0.15 0.50

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7 Occupational

Health

OHC, Training & Medical Checkup

2.00 0.05 0.10 0.15

8 CER

Activities

2% as per OM dated

01/05/2018 18.00 0.06 0.04 0.10

Total 191.89 49.03

Summary

Cost of Project in Crores 8.88Crores

EMP Capital Cost in Crores 1.91Crores

EMP Recurring Cost in Crores 0.49 Crores

A-3 Details of CER as per OM dated 01/05/2018 (In case of project falls under CPA/SPA, CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide 31.10.2019.)

% as per the OM

Rs. in Lakhs

2% 18.00


Activities

(On basis of Needs Assessment)

Phase Wise Budget (Rs. In Lakhs)

1st Year

2nd Year

TOTAL

Health-

Provide Ambulance with medical equipment (No.1) –Village Vorasamni

8.0 - 8.0

Infrastructure-

Solar Panel to Gram Panchayat Offices: 6

KW X 2 Nos (2 lakh each) Village- Vilayat,

Bhersam

2.0 2.0 4.0

Solid Waste Management–

Installation of OWC 500 Kg X 3 Nos @ 2 Lacs/Unit – Village Ankot, Saran, Cholad

Bins for segregation of waste

Operation & Maintenance of OWC

Training

3.0 3.0 6.0

Total Cost Approx. INR 18.0 Lakhs

B Land / Plot ownership details: Possession Receipt on the name of Proprietor – Mansukh N Radadia vide letter No. GIDC/DEE(Road)/BRH/60 on Dated: 05/02/2020

B-1 Plot area

Total Plot area

9576.272Sq. m.

B-2 Brief note on Area adequacy in line to proposed project activities: Company will store its raw material in Drums &Tanks (We procure Raw Materials from

the local market. 90% of these rawmaterials are easily available from this market. Hence,

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no excess quantity of raw materials will be stored). List of Hazardous chemicals stored in tanks shown below.


Tank Number of

Tanks Total Qty. to be store (KL)

PESO Tank 12Nos.

1 Methylene Chloride 15 KL 15 KL X 5 No 75 KL

2 Toluene 15 KL 1 No 15 KL

3 Ethyl Acetate 20 KL & 10 KL 20 KL X 2 Nos. 10 KL X 1 No

50 KL

4 Denatured Spirit 15 KL 2 No 30 KL

5 Acetic Acid 5 KL 1 No 5 KL

Non-PESO Tank 6 Nos.

1 Sulphuric Acid 10 KL 2 20 KL

2 Hydrochloric Acid 10 KL 2 20 KL

3 Sodium Hydroxide 10 KL 1 10 KL

4 Liq. Ammonia 10 KL 1 10 KL

Area required for ETP 210.0m²

120.0 m² area provided for the Boiler & TFH.

700.0 m² (G+2) area will be provided for the manufacturing of the proposed products.

S.N. Particulars Criteria for

Storage Inventory Required (MT)(KL)

Area Required

m2

Area Proposed

m2

1 Finished product

storage area (2 week inventory)

1 MT/ 1m2 75.00 75.00 120.00

2 Raw Material Store area

(2 week inventory) 1 MT/ 1m2 300.00 300.00 455.00

3 Drum Storage Area (Storage at a time)

1 MT/ 1m2 50.00 50.00 240.00

4 Petroleum Storage Area

(PESO) (Storage at a time)

- 175.00 350.00 720.00

5 Tank farm Area (Non-

PESO) (Storage at a time)

- 60.00 120.00 510.00

6 Cylinder Storage Area

(Nitrogen gas) (Storage at a time)

- 0.18 5.00 20.00

7 Hazardous Waste

Storage Area (G+1) (90 Day Inventory)

- 350 & 73 (Fly Ash)

423.00 500.00

1083.18

MT 1248.00

m2 2565.00

m2

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Hence, Adequate area is available for proposed Bulk drug intermediate mfg.

Facility.

B-3 Green belt area

Total (Sq. meter)

Area in Sq. meter 3161.00 Sq. m. (33 % of total plot area) Within plant premises

% of total area 33%


Total

50 Employees Direct = 40 Employees

Indirect = 10 Employees

D WATER

D-1

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

GIDC Water Supply Authority

Status of permission from the concern authority. Letter No.: GIDC/DEE (WS)/BRH/626 Dated: 19/09/2020.


Sr. No.

Category

Total Fresh Water Consumption (KL/Day)

Remarks Total Water

Reused/ Recycled

Fresh Water

1. Domestic 2.30 - 2.30 GIDC Water Supply

Authority 2. Gardening 12.60 - 12.60

3. Industrial

Process 45.00 - 45.00

Worst Case: (1,1-piperazinyl-dibenzo[b,f] [1,4]

thiazepine)

Boiler 54.00 43.2 10.8

Total Water requirement: 54 KLD

Condensate Recovery: 43.2 LD

Make up Water: 10.8 KLD

Cooling 7.00 7.00 -

Washing 1.00 0.50 0.50

Scrubbing 4.00 2.00 2.00

Total Industrial 111.00 52.70 58.30

Total (1 + 2 + 3) 125.90 52.70 73.20


Total Water Requirement of the proposed project will be 125.90 KLD, out of which Water Consumption for Process will be 45.0 KLD.

Worst Case Scenario;

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S.N Product Name Water req. (in KL)

for 1 MT production

Total Production (MT/Month)

Total water req. (KLD)

1.

1,1-piperazinyl-dibenzo[b,f] [1,4]

thiazepine 9.0 150.0 45.00

Hence Worst Case Considered is 45 KLD

- Summary of water requirement Quantity

KLD Remarks

Total water requirement for the project (A)

125.90 -

Quantity to be recycled / reused (B)

52.70 Reused & Recycled

Total fresh water requirement (C)

73.20 GIDC Water Supply Authority

Ensure Total water requirement = Fresh water + Recycled water i.e. A = B + C






Boiler Condensate 38.5 KLD (Boiler)

pH: 7.5-8.0 TSS: < 60mg/l

TDS: <900 mg/l BOD: <10 mg/l COD: <30 mg/l Yes, it is

feasible.

From ETP

9.5 KLD (Cooling,

Washing & Scrubbing)

pH: 6.5-7.5 TSS: < 75 mg/l

TDS: <1000 mg/l BOD: <90 mg/l

COD: <250 mg/l

In case of no reuse/recycle of waste water, Give brief note on justification as why no reuse/recycle. -


Category

Proposed (KL/Day)

Remarks

1. Domestic 1.80 Will be treated in ETP

2. Industrial

Process 51.20 Worst Case: (Telmisartan)

Boiler 0.70

Cooling 0.70

Washing 1.00

Scrubbing Solution

(25-30% NaCl) 1.00

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Scrubbing Solution

(18-20% Na2SO3) 1.00 End User

Scrubbing Solution

(25-30% Liq. Ammonia) 1.00 Reused within premises

Scrubbing Solution (25-30%HBr/NaBr)

1.00 End User

Total Ind. 57.60

Total (1 + 2) 59.40

-

Brief Note on worst case scenario for waste water generation (Qualitative and Quantitative):

Total Waste Water Generation of the proposed project will be 59.40 KLD, out of which Waste Water Generation for Process will be 51.2KLD.

Worst Case Scenario;

S.N Product

Waste Water Gen. (in KL)

for 1 MT production

Total Production (MT/Month)

Total Waste water Gen. (KLD)

Characteristics

1. Telmisartan 10.24 150.0 51.2

pH – 6.5 to 7.5 (Neutralization at source) TSS-190 mg/l TDS-23560 mg/l BOD- 7820 mg/l COD-26122 mg/l

Hence Worst Case Considered is 51.2 KLD

Brief justification in case of no process effluent generation or no industrial effluent generation or no high concentration effluent generation from proposed project (Whichever is applicable).

Not Applicable. There will be effluent generation. The detail has been furnished in water Balance.


Domestic: Domestic wastewater@ 1.8 KLD will be Subjected to ETP.

Industrial: Total Effluent 54.79 KLD will be treated in ETP.

45.00 KLD discharged to CETP of Saykha GIDC and 9.5 KLD treated water will be reused in Cooling,Washing & Scrubbing.

- Clearly mention about final disposal


For Domestic waste water: Capacity of STP: Not Applicable

For Industrial waste water: Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc. Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed. Treatment facility within premises with capacity [In-house ETP (Primary, Secondary, Tertiary), MEE, Stripper, Spray Dryer, STP etc.

Hydraulic Load – In-house Stripper: 51.20 KLD

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In-House ETP:54.79 KLD

Capacity— In-house Stripper: 65.0 KLD In-House ETP: 68.0 KLD

Stream 1 - Waste water from process @ 51.20 KLD will be subjected to solvent stripper. Outlet

of stripper @50.59 KLD will be treated in ETP (Primary & Secondary).

SR.

No.

Para Unit

Worst case Process Water After Solvent

Stripper Telmisartan

Quantity (KLD) 51.20 50.59

1 pH pH Unit 6.5-7.5

(Neutralization at source) 6.5-7.5

2 TSS mg/L 190 190

3 TDS mg/L 23560 23560

4 BOD mg/L 7820 3910

5 COD mg/L 26122 10449

6 Ammo. Nitrogen mg/L Nil Nil

Stream 2 - Waste water from 0.7 KLD Boiler Blow Down, 0.7 KLD cooling blow down, 1.0 KLD Washing

and 1.0 KLD Scrubbing Soln (25-30% NaCl Sol.) = 3.4 KLD will be Subjected to ETP (Primary & Secondary).

Sr. No.

Parameter

Unit

Stream from other utilities Characteristics Combine

Effluent Boiler Cooling Washing Scrubbin

g

Quantity (KLD) 0.7 0.7 1.0 1.0 3.4

1 pH pH Unit 7.5-8.0 7.5-8.0 6.0-8.0 6.0-8.0 6.0-8.0

2 TSS mg/L 56 87 150 120 109

3 TDS mg/L 500 1200 2500 500 1232

4 BOD mg/L 10 16 487 190 204

5 COD mg/L 30 50 2298 524 846

6 Ammo.

Nitrogen mg/L Nil Nil Nil Nil Nil

Stream 3 – Totally 53.99 KLD (Stream 1: 50.59 KLD After Solvent Stripper + Stream 2: 3.4 KLD Dilute

Stream) will be allowed to in-house ETP (Primary).

Sr. No.

Parameter Unit

After Solvent stripper

Combine Effluent (Dilute

Stream)

Composite Effluent

After Primary

treatment

Quantity (KLD) 50.59 3.4 53.99 52.99

1 pH pH Unit

6.5-7.0 6.0-8.0 6.5-7.5 6.5-7.5

2 TSS mg/L 190 109 185 55

3 TDS mg/L 23560 1232 22154 23262

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Primary treated Waste water @52.99 KLD along with Domestic Waste Water @1.8 KLD will

be allowed in Secondary ETP.

Sr. No.

Parameter

Unit

After Primary Treatme

nt

Domestic

Composite Effluent

After Secondar

y Treatmen

t

After Tertiary

Treatment

Quantity (KLD) 52.99 1.8 54.79 54.29 9.50

1 pH pH Unit

6.5-7.5 6.0-8.0 6.5-7.5 6.5-7.5 6.5-7.5

2 TSS mg/L 55 300 64 74 <50

3 TDS mg/L 23262 750 22522 22522 <1000

4 BOD mg/L 2941 250 2853 428 <90

5 COD mg/L 7875 10 7617 1143 <250

6 Ammo.

Nitrogen mg/L Nil Nil Nil Nil Nil

Stream 4(Scrubbing Solution) – 1.0 KLD 25-30% NaCl Scrubbing Soln will be treated in-house ETP. 1.0 KLD 18-20% Na2SO3 and 1.0 KLD 25-30 % NaBr/HBr scrubbing soln will be sent to end

users registered under Rule-9. 1.0 KLD 25-30% Liq. Ammonia will be reused within premises.

4 BOD mg/L 3910 204 3677 2941

5 COD mg/L 10449 846 9844 7875

6 Ammo.

Nitrogen mg/L Nil Nil Nil Nil


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. Total Effluent 54.79 KLD will be treated in ETP.

45.00 KLD discharged to CETP of Saykha GIDC and 9.5 KLD treated water will be reused in Cooling, Washing& Scrubbing.

Brief note on adequacy of ZLD (In case of Zero Liquid Discharge): Not Applicable – Total Effluent 54.79 KLD will be treated in ETP.

45.00 KLD discharged to CETP of Saykha GIDC and 9.5 KLD treated water will be reused in Cooling, Washing& Scrubbing.


Common ETP of M/s. GIDC - Saykha

Membership of Common facility (CF) mentioning total capacity, consented quantity, occupied capacity and spare capacity and norms of acceptance of effluent from member units in-line with the direction given by GPCB vide Letter No. GPCB/P-1/8-G (5)/550706 dated 08/01/2020.

Common ETP of M/s. GIDC – Saykha Permission Letter No. GIDC/BRH/XEN/WD/975 on dated 17/09/2020.


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E AIR

E-1 Brief Note on fuel based Heat energy requirement and worst case scenario thereof:

SN Fuel Based Heat Energy

Proposed Fuel

Calorific Value (kcal/kg)

Working Hours (Worst Case)

Fuel Consumption in worst case

1 Boiler 3.0

TPH

Natural Gas

7900 – 8500 kcal/kg

18 Hrs 5085SCM/Day

OR

Bio Coal 3800-4300 kcal/kg 18 Hrs 11.0 MT/Day

2

Thermic Fluid Heater

(5 Lac KCal/Hr.)

Natural Gas

7900 – 8500 kcal/kg

24 Hrs 2000 SCM/Day

OR

Bio Coal 3800-4300 kcal/kg 24 Hrs 4.0 MT/Day


Sr. No.

Stack attached

to

Stack Height&

Dia (Meter)

Type of Fuel

Fuel Consumpt

ion APCM

Concentration of Pollutants

1. Boiler (3.0

TPH) 30/0.5

Natural Gas OR

Bio Coal

5085 SCM/Day

OR 11.0

MCS + Bag Filter+ Water

Scrubber &

PM < 150 mg/Nm3

SO2 < 100 ppm

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MT/Day Adequate Stack height

NOX < 50 ppm

2.

Thermic Fluid

Heater (5 Lac

KCal/Hr.)

30/0.5

Natural Gas OR

Bio Coal

2000 SCM/Day

OR 4.0

MT/Day

Cyclone + Water

Scrubber&Adequate

Stack height

3.

D.G. Set Stand by

(125 KVA)

11/0.25 Diesel 20 lit/Hr. Adequate

Stack height

4.

D.G. Set Stand by

(450 KVA)

11/0.25 Diesel 60 lit/Hr.


Sr. no.



Type of emission

Stack/Vent Height & Dia

(meter)

Air Pollution Control

Measures (APCM)

1

Reaction Vessel-1 (Sulphonation) Couple Amine Hydrochloride

SO2: 40 mg/Nm3

18/0.2 Two Stage

Alkali Scrubber

2

Reaction Vessel-2 (Chlorination)

6-Flouro-2-Methyl 2-3-dihydro-1H-indon-

1-one

HCl: 20 mg/Nm3

18/0.2 Two Stage Alkali

Scrubber

3

Reaction Vessel-3 (Ammination)

5-fluro-2-methylindene-3-Acid

NH3: 175 mg/Nm3

18/0.2 Two Stage Water

Scrubber

4

Reaction Vessel-4 (Bromination)

Tramadol Hydrochloride

HBr: 30 mg/Nm3

18/0.2 Two Stage Alkali

Scrubber

Note: Details of gaseous raw materials used in proposed project Estimation of process gas emission (Product wise and Total) Requirement of the scrubbing media (KL per Day) considering solubility (Product

wise and Total) Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and


Sn

Product

Gaseous Raw Materia

l

Process

Gas Emiss

ion

Total Emiss

ion (MT/D

ay)

Requirement of

Scrubbing Media (KL Per

Day)

Solution /

bleed liquor

s

Solubility (%)

Solution / Bleed liquors

(MT/Annum)

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(KLD)

1

Couple Amine

Hydrochloride

Thionyl Chlorid

e SO2 0.2

0.8 (Caustic)

1.0 > 90 365 KL

(18-20% Na2SO3)

2

6-Flouro-2-Methyl

2-3-dihydro-

1H-indon-1-one

Thionyl Chlorid

e HCl 0.3

0.7 (Caustic)

1.0 > 90

365 KL (25-30 %

NaCl)

3 5-fluro-2-

methylindene-3-Acid

Ammonium

Acetate NH3 0.3

0.7 (Water)

1.0 > 90

365 KL (25-30%

Liq. Ammoni

a)

4 Tramadol

Hydrochloride

m-Bromo Anisole

HBr 0.3 0.7

(Caustic)

1.0 >90

365 KL (25-30% NaBr/HB

r)


To mitigate fugitive emissions, the following steps would be taken:

Minimum number of flanges, joints and valves in pipelines

Selection / use of state-of-the art leak proof valves

Provision of mechanical seals in pumps

Proper preventive maintenance of roofs and seals for tanks

Monitoring and preventive maintenance of valves, flanges, joints, etc.

Fugitive emission over reactors, formulation areas, centrifuges, chemical loading, transfer area, shall be collected through hoods and ducts by induced draft and controlled by dust collector.

For particulate / dust emissions from the coal handling system: Water will be sprinkled to control particulate / dust emission from coal storage area.

Green belt will be developed along the plant premises

De-dusting system will be provided at solid product finishing area.

All transfer points will be fully closed.

Overflow system with return line to storage tank from batch tank will be provided to prevent hazardous material overflow.

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



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calculations shall be incorporated in EMP details separately. Disposal to scrap vendors/vendors/traders is not allowed


Sr. no.

Type/Name of

Hazardous waste

Specific Source of generation (Name of the

Activity, Product etc.)

Category and

Schedule as per HW

Rules.

Quantity

(MT/ Annu

m)

Management of HW

1 ETP

Sludge ETP

35.3/ SCH-I

550.0 Collection, Storage, Transport, and Disposal at nearest TSDF.

2

Process Waste

(Inorganic)

Mfg. Process

5-fluro-2-methylindene-3-

Acid

28.1/SCH-I

360

3 Used Oil Maintenance

Activities 5.1/SCH-I 0.5

Collection, Storage, Transportation; reuse as lubricant or by selling to Authorized re- refiners.

4

Discarded Container

s/ Bags/Line

rs

Raw Material Supplier

33.1/SCH-I

50.00 (Nos. 5000

Container)

(Nos. 50000

0 Bags/Liners)

Collection, Storage, Transportation; Decontamination and Reuse or Sale to Authorized Vendor.


Mfg. Process

Levofloxacin

20.3/SCH-I

1152

Collection, Storage, Transportation & Disposal by selling to Pre /Co-processing unit (Cement Industries) or by incineration at CHWIF.

6 Process Waste

(Organic)

Mfg. Process


Acetoxyethoxy)methyl] -N2-

acetylguanine

28.1/SCH-I

864.0

7 Spent

Carbon/ Hyflow

Mfg. Process

Acyclovir

28.3/SCH-I

216.0

8 Spent

Solvent

Mfg. Process

Levofloxacin

28.6/SCH-I

*58340

Collection, Storage, Handling & Subjected to distillation assembly to recover the solvent & Reuse

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within premise.

From Solvent Stripper

222.65

Collection, Storage, Transportation & send to pre/co processing unit (Cement Industries) OR send to CHWIF.

9

Scrubbing Solution

25-30% NaCl

From Scrubber

6-Flouro-2-Methyl 2-3-dihydro-1H-indon-1-one

28.1/SCH-I

365 KL

Collection, Storage &treat in ETP

10

Scrubbing Solution

25-30% Liq.

Ammonia

From Scrubber

5-fluro-2-methylindene-3-

Acid

28.1/SCH-I

365 KL

Collection, Storage & Reuse within premises.

(In the Mfg. process of Azithromycin: 4320 MT/Annum )

11

Scrubbing Solution

18-20% Sodium Sulphite (Na2SO3)

From ScrubberCoupl

e Amine Hydrochloride

28.1/SCH-I

365 KL Collection, Storage,

Transportation& Sell to End Users having permission under Rule-9.

12

Scrubbing Solution

25-30% HBr/NaBr

From ScrubberTrama

dol Hydrochloride

28.1/SCH-I

365 KL

13

Off Specificati

on Product

Mfg. Process

(Batch Failure)

28.4/SCH-I

1

Collection, Storage Transportation & send to Pre /Co-processing unit or send to CHWIF

*Justification for spent solvent generation & Captive reused

Product Name Solvent Fresh

Qty. Used MT/Day

Qty. Recovered

MT/Day

Qty. Used MT/Day

Tank Storage (At a Time)

Levofloxacin

Methylene Chloride

3.75 71.25 75.00 75 KL

(15 KL X 5 No.)

Toluene 0.68 12.83 13.50 15 KL

(15 KL X 1 No.)

Ethyl Acetate 2.00 48.00 50.00 50 KL

(20 KL X 2 Nos. 10 KL X 1 No.)

Denatured 1.17 28.08 29.25 30 KL

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Spirit (15 KL X 2 No.)

Acetic Acid 0.10 1.90 2.00 5 KL

(5 KL X 1 No.)

Total MT/Day 7.70 162.06 169.75

Total MT/Year 2770.2

58339.8 ~ 58340

61110


Details of Membership letter no. & Date with spare capacity of the Common Facility. M/s. BEIL, Dahej For Land Filling Letter No. Nil Dated: 11/11/2020 For Incineration Waste Letter No. Nil Dated: 11/11/2020


Sr. no.


Specific Source of generation

(Name of the Activity,

Product etc.)

Quantity (MT/Annum)


1 Fly Ash Boiler & TFH

Fuel (Bio-coal)

292.0

Collection, storage, transportation & send to Brick manufacturer

OR farmer for agricultural purposes

OR TSDF for Landfilling.


G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse of recovered Solvents etc.


The Following methodology to be adopted during LDAR study: Identify the Chemical streams that must be monitored. Types of components (pumps, valves, connectors, etc.) to be monitored Frequency of monitoring. Actions to be taken if a leak is detected. Length of time in which an attempt to repair the leak must be performed. Actions that must be taken if a leak cannot be repaired within guidelines. Record-keeping and reporting requirements.


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

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

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

materials in particular solvents through hoods and ducts by induced draft, and control by condenser to be ensured.

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

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

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

Primary Condenser HE-01: Cooling Tower water or Chilled water at 5 °C will be used to condense the solvents depend on the vapor pressure at its operating conditions and the non condensed vapors will be condensed in a Secondary Condenser.

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

Emission of VOCs can be trapped from breathing and loading losses from storage tanks, venting of process vessels, leak from piping and equipment by means of hood connected with blower and send to condenser as shown in following diagram.

Condensed VOCs will be send to spent solvent recovery plant.

H SAFETY details



Tank Number of

Tanks

Hazardous Characteristics

of Chemical

PESO Tank 12 Nos.

1 Methylene Chloride 15 KL 15 KL X 5 No Flammable

2 Toluene 15 KL 1 No Flammable

3 Ethyl Acetate 20 KL & 10 KL 20 KL X 2

Nos. 10 KL X 1 No

Flammable

4 Denatured Spirit 15 KL 2 No Flammable

Non-PESO Tank 6 Nos.

1 Sulphuric Acid 10 KL 2 Toxic

2 Hydrochloric Acid 10 KL 2 Toxic

3 Sodium Hydroxide 10 KL 1 Toxic

4 Liq. Ammonia 10 KL 1 Flammable


PESO Tank- 12 nos. (Underground)

Non-PESO- 6 Nos Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels, Carboys, Bags etc.

Some chemicals will be received at plant in drums by road truck and stored in a separate drum storage area.

FLP type light fittings will be provided. Proper ventilation will be provided in go down. Proper label and identification board /stickers will be provided in the storage

area. Conductive drum pallets will be provided. Drum handling trolley / stackers/fork lift will be used for drum handling. Separate

dispensing room with local exhaust and static earthing provision will be made.

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Materials will be stored as per its compatibility study and separate area will be made for flammable, corrosive and toxic chemical drums storage.

Smoking and other spark, flame generating item will be banned from the Gate. Safety details of Hazardous Chemicals:


Safety measures

PESO Tank Safety Measures for PESO Underground storage tank farm: The underground vessels shall be placed within concrete

or brick masonry pit with a gap of 1.0 meter between the walls of the pit and the vessel as well as in between the vessels.

The underground vessels shall be installed on a firm foundation and firmly secured to the foundation so as to prevent movement of floatation.

Class A Petroleum products will be received through road tanker and stored in u/g storage tank as per PESO Rule.

Tank farm will be constructed as per explosive department requirement and separation distance will be maintained.

The underground vessels covered by earth (Mound) shall be a designed to withstand external pressure due to load of the earth cover. o Provided with external anti-corrosive coating or

cathodic protection to prevent corrosion ; o Covered by earth, sand or any other non-corrosive

material free from abrasive particles likely to damage the anti-corrosive coating of the vessel-the thickness of the covering material above the top surface of the vessel shall not be less than 0.5 meter;

o Having the discharge level of the safety relief valves at least 2 meters above the top surface of the vessel, but in any case not less than 3 meters from the ground level;

o Fitted with the necessary piping's, fittings, valves and other mounting on top of vessel in such a manner that they can be operated and maintained without disturbing the earth cover. In case of above ground vessel with earth cover (mound), liquid outlet pipe at the bottom may be allowed provided the control valve and emergency valve of this line is just outside the earth cover for the purpose of operation and maintenance from outside.

Static earthing provision will be made for road tanker as well as storage tank.

Flame arrestor with breather valve will be provided on vent line.

Road tanker unloading procedure will be prepared and implemented.

Fire load calculation will be done and as per fire load hydrant system will be provided as per NFPA std. and fire extinguishers will be provided as per fire load calculation.

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Spark arrestor will be provided to all vehicles in side premises

Lightening arrestor will be provided on the top. Flame proof type equipment and lighting will be provided. Trained and experience operator will be employed for

tank farm area. NFPA label (hazard identification) capacity and content

will be displayed on tanks Solvents will be transferred by pump only in plant area

and day tank will be provided. Overflow line will be return to the storage tank or Pump On-Off switch will be provided near day tank in plant.

Jumpers will be provided on solvent handling pipe line flanges & Flexible SS hose will be used for road tanker unloading purpose and other temp. connection

PESO Area Storage & Handling Safety: (UNLOADING)

Ensure that the transfer of petroleum takes place only through electrically continuous sound hose having oil tight couplings at both ends.

Couplings of the hose at the discharge ends of the tank trucks as well as at the fill pipe end of the underground tank shall not be leaky.

Unloading operations should not commence without ensuring earthing of the tanker body to a proper earthing point. For this purpose, a proper earthing point shall be provided near filling points.

Before commencing unloading operations tanker should be parked in the retail outlet in such a manner that it can be taken out of the retail outlet immediately in case of emergency.

Dip pipe of the underground tank shall not be kept open during unloading operations.

The dealer, supervisors and pump attendants shall be trained in all aspects of safety in RO including the provisions of Petroleum Rules, 2002 in Chapter IV on Electric Installation, Rules 117 to 119,122,125 and conditions 6 to 12, 15,16,18 to 21of licence Form XIV for the RO‘s under the said Rules.

Before starting unloading of petroleum, it must be ensured that at least a safe distance of 3 M is kept clear of any kind of movement of other vehicles that come for fuelling and that there is no source of any spark in the area. In case of retail outlets that are in congested areas operations of fuelling automobiles in the retail outlet may be discontinued.

Do not use plastic hose pipes for unloading purposes. Do not use hose pipe fitted with metallic pipe

(bent pipe) at the discharge end. Do not use Hose pipes not conforming to OISD

135. Proper tightening of hose connections using

screwed/cam lock couplings.

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Make sure that there shall be no collection of leaked petroleum through hose pipe connection at tanker discharge faucet end in the plastic bucket kept on the ground below.

Provision of electrical earthing / bonding by means of flexible cable between tanker chassis and earth boss/fill pipe.

Proper training to the retail outlet staff regarding hazards associated with the petroleum road tanker decantation operation in the retail outlets.

Non PESO tank

Safety measures for Acid storage Tank: Storage tank will be stored away from the process plant. Tanker unloading procedure will be prepared and

implemented. Caution note and emergency handling procedure will be

displayed at unloading area and trained all operators. NFPA label will be provided. Required PPEs like full body protection PVC apron, Hand

gloves, gumboot, Respiratory mask etc. will be provided to operator.

Neutralizing agent will be kept ready for tackle any emergency spillage.

Safety shower, eye wash with quenching unit will be provided in acid storage area.

Material will be handled in close condition in pipe line. Dyke wall will be provided to all storage tanks, collection pit

with valve provision. Double drain valve will provided. Level gauge will be provided on all storage tanks. Safety permit for loading unloading of hazardous material

will be prepared and implemented. TREM CARD will be provided to all transporters and will be trained for transportation Emergency of Hazardous chemicals.

Fire hydrant system with jockey pump as per TAC norms will be installed.

Safety Measures of Non PESO Tank Leakage / spillage mitigation plan Tank shall be rubber lined to prevent the corrosion Dyke wall shall be provided for containment Rubber type hand gloves and chemical splash goggles

and full-face cartridge type mask and PVC apron shall be used while manual handling

Lime shall be readily available during leak to neutralize the spill material

Safety shower, eye wash with quenching unit will be provided in acid storage area.

Material will be handled in close condition in pipe line. Double drain valve will provided. Level gauge will be provided on all storage tanks. Fire hydrant system with jockey pump as per TAC norms

will be installed

Applicability of PESO: Will be obtained.

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H-2 Types of hazardous Processes involved and its safety measures: (Hydrogenation process, Sulphonation, Chlorination process, Bromination Reaction etc.)

Type of Process


Hydrogenation

DCS base process controls and operation of plant will be

installed.

All electrical equipment‗s shall be installed as per Hazardous

Area Classification.

Total enclosed process system.

Instrument & Plant Air System.

Nitrogen blanketing in Hydrogenation reactor.

Emergency dumping vessel will be provided during

unforeseen circumstances.

Safety valve and Rupture disc provided on reactor.

Cooling, Chilling and alternate power arrangement have

been made on reactor.

Process area and Hydrogen cylinder bank shall be far away

as per standards practice.

PRV station with shut off valve, safety valve provision will be

made for hydrogenation reaction safety.

Standard Operating procedure shall be followed during

operation of Hydrogen Gas charging in to reactor and after

completion of reaction Nitrogen purging will be done.

Flame arrestor will be provided on vent line of reactor and it

will be extended above the roof level.


SOP will be displayed and operators will be trained for the

same.

Static earthing and electric earthing (Double) will be provided.

Jumpers for static earthing on pipeline flanges of flammable

chemical will be provided.

Hydrogen gas detector will be installed for early

detection of gas leak.

Bromination All end nozzles in bromine charging hose will be blinded after use.

Charging of bromine will be done when reactor is in

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vacuum and POP coated funnel will be used during charging.

Excess bromine will be neutralize or discharged by adding Sodium Bisulfite.

Make sure the absorber unit (scrubber) is working and capable of handling vented bromine fumes.

Structure of bromine bottle area will be periodically inspected to ensure stability.

Personnel employed with bromine handling are made aware of potential hazards of bromine and of appropriate first-aid measure.

Exhaust hood connected with alkali scrubber and ventilation system will be available. Exhaust hood has been provided to maintain to concentration of bromine vapor well below PEL.

Work instructions for bromine charging will be displayed in local language/Hindi.

Safety shower and eye-wash fountains will be available nearby handling and charging facility. The location of such item will be inspected and tested at fixed interval to make sure that it is in good condition.

Hypo solution, lime water slurry or soda ash solutions will be available so as to pour them over a liquid bromine spill on the floor. The bromine and neutralizer is then washed to the sump with cold water hose.

Personal Hygiene – the following personal protective equipment will be used.

Chemical safety goggles, face shields, SCBA sets, Aprons, rubber gloves, etc.

Only trained employees handled bromine charging. Training will be given to employees for bromine handling and charging.

Sulphonation & Chlorination (Only Through

Thionyl Chloride)

Provision of Safety valve & rapture disc on reactor.

Provision of auto dumping vessel.

Required PPEs like full body protection PVC apron, Hand gloves, gumboot, Respiratory mask etc. will be provided to operator.

To avoid runaway reaction, TC charging will be done gradually & slowly to avoid runaway reaction, TC charging will be done gradually & slowly.

Charging will be done only through closed line and system. Scrubber attached with closed system.

Make sure the absorber unit (two stage Alkali scrubber) is working and capable of handling vented SO2 / HCl fumes.

Neutralizing agent will be kept ready for tackle any emergency spillage.

Safety Shower and eye wash will be provided near process area.

For Thionyl Chloride evacuate area in down wind direction up to 0.3 km ( 300 meter) in small spillage.

Emergency siren and wind sock will be provided. Tele Communication system and mobile phone will be used

in case of emergency situations for communication.

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Total close process will be adopted for Thionyl chloride charging.

Caution note and emergency first aid will be displayed and train for the same to all employees.

First Aid Boxes will be available in process area. Emergency organization and team will be prepared as per

On site-Off site emergency planning. Emergency team will be prepared and trained for scenario

base emergency. Like Toxic control team, Fire control team, First aid team, communication and general administration team, Medical team etc.

Do not touch damaged containers or spilled material unless wearing appropriate protective clothing.

Use water spray to reduce vapors; do not put water directly on leak, spill area or inside container. Keep combustibles (wood, paper, oil, etc.) away from spilled material.

Cover with DRY earth, DRY sand or other non-combustible material followed with plastic sheet to minimize spreading or contact with rain.


Total Plot Area: 9576.27Sq.mt

Area utilized for plant activity:

700Sq.mt

Area utilized for Hazardous Chemicals Storage:

500Sq.mt

Number of Floors Area:

Sr. No

Plant / Building/Facility Name

Total No. of floor

Details of Floor

Area of the floors and

galleries

in sq meter

1 Security Cabin 1 & 2 1 Ground floor 36.00

2 D.G Set 1 Ground floor 8.00

3 OHC 1 Ground floor 20.00

4 Admin Building 1 Ground floor 80.27

5 Process Building 3

Ground floor 700.00

First floor 700.00

Second floor 700.00

6 Non Peso Tank Area 1 Ground floor 510.00

7 Raw Materials Storage 1 Ground floor 455.00

8 Finished Product Storage 1 Ground floor 120.00

9 Drum Storage Area 1 Ground floor 240.00

10 Petroleum Storage Area 1 Ground floor 720.00

11 Boiler & TFH 1 Ground floor 120.00

12 ETP 1 Ground floor 210.00

13 Haz Waste Storage Area 1 Ground floor 500.00

14 Fly Ash Storage 1 Ground floor 40.00

15 Fuel Storage 1 Ground floor 50.00

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16 Cylinder Storage Area 1 Ground floor 20.00

17 Fire Pump House 1 Ground floor 40.00

5269.2

7

Water requirement for firefighting

55,804 Liters

Water storage tank provided for firefighting

4,00,000Liters

Details of Hydrant Pumps:

Fire water Pump will be available. We will have 01 No‘s of electrical fire water Pump located at pump house having capacity 4550.0 litres/min and 01 No‘s of Diesel pump having capacity 4550.0 litres/min. Apart from this we have 01 Nos Jockey Pumps of capacity 1080.0 litres/min which maintains the Fire water Header Pressure at 8.0 kg/cm².

Nearest Fire Station : Fire Station : SEZ Fire Station, Dahej (Distance from project site: 32.38km)

Applicability of Off Site Emergency Plan:

--


Will be Applied




Area provided for OHC: 20Sq. m


Nearest General Hospital : Pipalia Health Care Center, Pipalia

Name of Antidotes to be store in plant : Artificial respiration, First Aid, etc.



Project proponent (PP) and Technical expert of PP, M/s. Greenleaf Envirotech Pvt Ltd remains present

during video conference meeting.

Committee noted that the proposal is for Greenfield project in GIDC Saykha. PP submitted details


depth. Committee noted that PP has shown Tetra Butyl Ammonium Bromide as API and its end use as

phase transfer catalyst which is not in line with MoEF&CC‘s Notification vide S.O. 1223 (E) dated

27/03/2020 in respect of Active Pharmaceutical Ingredients (API) as category B2 projects and hense

asked for clarification regarding it during meeting which is could not presented by PP properly during

SEAC meeting.


segregated. High COD stream will be passed through solvent stripper and then along with Low COD

stream will be partly treated in ETP consist of primary and secondary ETP units and treated effluent will

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be sent to CETP of GIDC Saykha for further treatment and disposal. Rest of treated effluent will be

further treated in tertiary ETP units and treated effluent will be reused back in process. Domestic sewage

will be treated in ETP. Committee discussed regarding stage wise reduction of BOD, COD and TDS in

ETP to achieve CETP inlet norms. Committee insisted for submit adequate treatability report for high

COD stream from process and low COD stream with stage wise reduction of BOD,COD,TDS and

Ammonical nitrogen in ETP to achieve inlet norms of CETP with mentioning characteristic of effluent

generated from each proposed products.

PP submitted that they have proposed boiler, thermo pack and DG set. Fuel used will be Natural gas or

bio coal for boiler and thermo pack.MCS, bag filter and water scrubber as APCM proposed for bio coal

fired boiler. Two stage scrubbers will be provided as APCM with each process reactor stack. PP

submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.





centre (OHC) and process hazard and its safety control measures. Committee noted that PP presented

details of auto control system for critical process and Hazardous chemical storage area with its risk

assessment.


CER, LDAR and solvent recovery etc.

After detailed discussion, Committee unanimously decided to consider the project only after

submission of following documents,

1. Submit clarification regarding Tetra Butyl Ammonium Bromide mentioned as API and its end use

as phase transfer catalyst which is not in line with MoEF&CC‘s Notification vide S.O. 1223 (E)

dated 27/03/2020 in respect of Active Pharmaceutical Ingredients (API) as category B2 projects.

2. Submit clarification regarding proposal of high COD stream from process for disposal in CETP in

place of proposal of MEE for evaporation of high COD stream.

3. Submit adequate treatability report for high COD stream from process and low COD stream with

stage wise reduction of BOD, COD, TDS and Ammonical nitrogen in ETP to achieve inlet norms

of CETP with mentioning characteristic of effluent generated from each proposed products.

10. SIA/GJ/IND2/173540/2020 M/s. Navjeevan-O-Chem

Plot No. 5903/1, GIDC Industrial Estate,

Ankleshwar, Dist-Bharuch

Appraisal


Project status: Expansion


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This is an existing unit and now proposes expansion in manufacturing of synthetic organic chemicals

[API and API Intermediates] as tabulated below.

Sr. no.


API OR INTERMEDIATE

CAS no.

Quantity MT/Month

End-use of the products * Existing Proposed Total

1. Ferric Chloride (Anhydrous and Lumps)

-- 7705-08-0

39.02 -- 39.02

--

2. Meta Nitro Para

Toluidine

API Intermediate

119-

32-4

-- 50.00 50.00

API Intermediate

3. Ethyl Ethoxy

Methylene

Malonate

API Intermediate

87-13-

8

API Intermediate

4. 3.5-Dihydroxy

Benzoic Acid

API Intermediate

99-10-

5

API Intermediate

5. 3.5-

Dichlorobenzoic

Acid

API Intermediate

51-36-

5

API Intermediate

6. 3-Hydroxy

Acetophenone

API Intermediate

121-

71-1

API Intermediate

7. 5-Cyano Phthalide

API Intermediate

82104-

74-3

API Intermediate

8. 2‐Chloromethyl‐4‐

methoxy‐3,5‐dimet

hylpyridine

hydrochloride

API Intermediate

86604‐

75‐3

API Intermediate

9. 2 Hydroxy 5 Nitro

Benzoic Acid

API Intermediate

96-97-

9

API Intermediate

10. R & D Products

(Nitration,

Sulphonation,

Amination,

Chlorination)

AP Intermediate

-- -- 0.10 0.10 API Intermediate

Total 39.02 50.10 89.12

ENDUSE OF PRODUCTS

Sr. No.

Name of the Product CAS No.

Type/ Category of


Said API is used

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(Product) Product (API/ Intermediate)


Name of API in which Intermediate Used/ End use of said Intermediate

CAS no. (API)

for/End Use of said API

2.

Meta Nitro Para Toluidine 119-32-4 API

Intermediate

n-2 Cyclizine

82-92-8

To Prevent Nausea, Vomiting

3.

Ethyl Ethoxy Methylene Malonate 87-13-8 API

Intermediate

n-2

4:7-Dichloro Quinoline

86-98-6

Discoid lupus

erythematosus and

systemic lupus

erythematosus

4.

3.5-Dihydroxy Benzoic Acid 99-10-5 API

Intermediate

n-2 Phenylephri

ne 59-

42-7 Stuffy Nose,

Sinus

5.

3.5-Dichlorobenzoic Acid 51-36-5 API

Intermediate

n-2

Alkylresorcinol

39341-78-

1

Metabolite, used in Human Urine

infection

6.

3-Hydroxy Acetophenone 121-71-1 API

Intermediate

n-2 Phenylephri

ne 59-

42-7 Stuffy Nose,

Sinus

7.

5-Cyano Phthalide 82104-74-3

API Intermediat

e

n-2 Citalopram

59729-33-

8

Anti-Depression

8. 2‐Chloromethyl‐4‐methoxy‐3,5‐dimethylpyridine hydrochloride

86604‐75

‐3

API Intermediat

e

n-1 Omeprazol

e

73590-58-

6 Peptic Ulcer

9.

2 Hydroxy 5 Nitro Benzoic Acid 96-97-9 API

Intermediate

n-1

Mesalamice 89-

57-6

Treat Bowel isease, Stomach

Pain







(Rs. in Crores):

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Existing

Proposed

Total

2.45 Crores 3.5496Crores 6.00Crores


Details Existing

(Rs. In Crores)

Proposed

(Rs. In

Crores)

Total

(Rs. In

Crores)

Land 2.45 -- 5.9996

Buildings 0.73

Plant & Machinery 1.43

EMP Cost 1.3896

Total 2.45 3.5496 ≈ 6.00

A-2 Details of Environment l Management Plan (EMP) As below:

Sr. No Unit Detail Capital Cost (Rs. In Crore)

Operating Cost (Rs. In Crore

Maintenance Cost (Rs. In Crore)

Total Recurring Cost (Rs. In Crore)

1 Waste Water

Modification of ETP and getting membership of RO

0.5 1.4524 0.045 1.4974

Provision of RWH Pit

0.015 - 0.005 0.005

2 Air

Provision of APCS During Construction Phase

0.005 - 0.002 0.002

Installation of Stack/Vent & it‘s Monitoring Facilities and Provisio

0.3 0.032 0.003 0.035

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n of Air Pollution Control System

Provision of Odour Control System

0.01 0.0018 0.0002 0.002

Provision of VOC Detectors

0.015 0.0028 0.0002 0.003

Provision of CCTV Camera

0.01 0.0004 0.0001 0.0005


Getting Membership of TSDF Site

0.02 0.2016 - 0.2016

4 Fire & Safety

Provision of Safety Measures including Fire Detectors, Sensors, Alarm, Fire Hydrant, Fire Extinguishers, Lightening arrestors etc.

0.16 0.0326 0.0025 0.035

Provision of PLC based DCS type Automization

0.15 0.0208 0.0012 0.029

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Page 196 of 232

system

5 AWH Monitoring

To conduct EMS efficacy & environment monitoring

- 0.02 - 0.02


Development of Greenbelt Area

0.05 0.0065 0.0005 0.007

7 Occupational Health

Provision of Occupational Health Centre with Antidotes

0.045 0.0185 0.0015 0.02

8 Noise

Installation of Acoustic Enclosure for D.G Set & Noise Control

0.01 0.0069 0.0006 0.0075

9 Provision of Solar Light within Plant Area

0.03 - 0.0004 0.0004

10 CER Activity 0.0696 0.005 0.0002 -

Total 1.3896 1.8013 0.0624 1.8654

Summary

Cost of Project in Crores per Annum: 6.00 Crores


Percentage:

1.3896Crores

(23.16%)


and Percentage:

1.8654Crores

(31.09%)

A-3 Details of CER as per OM dated 01/05/2018(In case of project falls under CPA/SPA,

CER fund allocation to be at least 1.5 times the slabs given in the OM dated 01.05.2018 for SPA and 2 times

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for CPA in case of Environmental Clearance as per the mechanism published vide MoEF&CC‘s OM vide

31.10.2019.)

% as per the OM

Rs. in Crores

2% 0.0696Crores


Sr. No.

Activities Location Year Budget

(Rs. In Lacs)

Basis Consideration

1. Provision of 15 Nos. Solar street light (Solar pole, battery, panel, LED light complete) on village road.

BhakrolVillage & Surrounding

villages* 2021 4.50

As per request received from Bakrol gram panchayat & surrounding

other villages on first cum first request

basis.

2. Provision of Dustbins at various internal village street, mosquito fogging machine.

2022 2.46

Total 6.96


Land has been procured by GIDC, Ankleshwar. Letter No.

GIDC/SO/ANK/ALT/2154

B-1 Plot area

Existing

Proposed

Total

5000.00Sq. m. -- Sq. m. 5000.00Sq. m.


Unit is going for expansion of project and expansion will be carried out within

existing premises. Total plot area is 5000 m2.

At present, open space available within plant premises is also 2540 m2.

Unit will continue its existing production capacity as per consent is 39.02 MT/

Month.

Unit will manufacture any products on either and/or (Max 05 Products) basis but

the total production capacity of each group will not exceed as per mentioned

separately. Hence, additional production capacity will be 50.00 MT/Month.

Unit has proposed 0.10 MT/Month R & D Category product.

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Hence, Total Production capacity will be 89.12 MT/month

Presently, 130.00 m2 area is provided for production plant having floor in plant

(G+1) for production of ferric chloride plant and for proposed production, 300 m2

additional area will be provided having (G+2) So, total production plant area is

1160 m2.

At present, 50.00 m2area is allotted for storage of raw material having G+1 floor,

which is utilized for existing project. Additional 800 m2 area will be allotted for

storage of raw material having G+1 floor. Thus proposed RM storage area will

be 1700 m2.

At present for packing material & finished goods storage 70 m2 is allotted having

G+1 floor. For proposed expansion project, additional 126 m2 having (G+1) area

will be provided.

For utilities 100.0 m2 area is allotted will be utilized for expansion project.

Separate 20 m2 area is allotted for storage of hazardous/solid waste, and

additional 80 m2 area will be provided. So, total 100 m

2 area will be available for

HWSA.

B-3 Green belt area

Existing

Proposed

(Sq. meter)

Total

(Sq. meter)

Area in

Sq. meter

2010.00 Sq. m -- 2010.00 Sq. m

% of total

area

40.20 % -- 40.20 %


Existing

Proposed

Total

16 (Male- 16,

Female- 00)

13 (Male- 13,

Female- 00)

29 (Male- 29,

Female- 00)

D WATER

D-1


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

GIDC, Ankleshwar

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Page 199 of 232


Unit will get permission from GIDC for additional water requirement

D-2


Category

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(J) Domestic

0.50 0.81 1.31 --

(K) Gardening

0.10 4.70 4.80 --

(L) Industrial

Process 1.40 16.40 17.80 * Considering Maximum Water consumption will be take place in product no. 7

2‐Chloromethyl‐4‐methoxy‐3, 5‐dimethylpyridine hydrochloride

Washing - 2.00 2. 0 -

Boiler - 30.00 30.00 --

Cooling - 2.00 2.00 --

Others (Scrubber) - 2.00 2.00 --

Others (Fire

Hydrant)

- 0.89 0.89# #Considering

Fire water

requirements

once in a six

month due to

mock drill

Industrial Total 1.40 53.29 54.69

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Grand Total

(A+B+C)

2.00 58.80 60.80


For Calculating Worst Case Scenario, Maximum process water consumption

will be take place in product no. 7 2‐Chloromethyl‐4‐methoxy‐3,

5‐dimethylpyridine hydrochloride.For worst case scenario, first of all product

water consumption is calculated by considering fully applied production

capacity. After that maximum water consumption took into consideration and

then divide quantity by number of working days per month. In addition

maximum boiler working hour, washing water requirement per day is also

taken into consideration. For in-house gardening around 4 L/m2 water is

considered. For domestic purposed around 45 Li/person/day water is

considered. Based on this our maximum water consumption shall not exceed

60.80 KLD.

-

Summary of water

requirement

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

Total water

requirement for

the project (A)

2.00 58.80 60.80

Quantity to be

recycled (B)

-- 34.42 34.42 --

Total fresh water

requirement (C) 2.00 24.38 26.38

Ensure Total water requirement = Fresh water + Recycled water

i.e. A = B + C



Source of waste

water for reuse

in KLD (From where

Application

area with

quantity in

Characteristics of

waste water to be

reused (COD, BOD, TDS

Remarks

regarding

feasibility

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Page 201 of 232

it is coming) KLD (Where it is

used)

etc.) to reuse

RO Permeate –

17.92 KLD

Washing: 2.00

KLD

Cooling: 2.00

KLD

Scrubber: 2.00

KLD

Boiler: 11.92

KLD

COD <250 mg/L

BOD <90 mg/L

TDS <250 mg/L

Feasible for

Reuse

Boiler Condensed

Steam – 16.5-

KLD

Boiler Makeup

Water – 16.50

KLD

COD < 30 mg/lit

BOD < 10 mg/lit

TDS < 10 mg/lit

Feasible to

reuse



Treated effluent will be utilized for preparation of dosing chemicals Solution

for ETP.

Treated effluent will be utilized in scrubber of APCS, attached with boiler flue

gas stack & same will allow in collection tank of ETP for its further treatment.

RO Permeate water (17.92 KLD) will be reused in Washing (2.00 KLD),

Cooling (2.00 KLD), Scrubber (2.00 KLD), Boiler (11.92 KLD).


Category

Existing

KLD

Proposed

(Additional)

KLD

Total after

Expansion

KLD

Remarks

(G) Domestic

0.50 0.55 1.05 --

(H) Industrial

Process 0.50 22.34 22.84** ** Considering Maximum Wastewater Generation will be from

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product no. 7 – 2‐Chloromet

hyl‐4‐methoxy‐3,

5‐dimethylpyridine hydrochloride

Washing -- 2.00 2.00 --

Boiler -- 1.35 1.35 --

Cooling -- 0.20 0.20 --

Others (Scrubber) - 0.54 0.54 --

Others (Fire

Hydrant)

- - -

Total Industrial

waste water

0.50 26.43 26.93

Brief Note on worst case scenario for waste water generation(Qualitative and

Quantitative):

Maximum Wastewater Generation will be from product no. 7 – 2‐Chloromethyl‐4‐methoxy‐3,

5‐dimethylpyridine hydrochloride. For worst case, first we have calculated waste water

generation from process for each products, as per fully applied quantity and from that we

have identified those products, which will generate more wastewater is carried out and same

is taken into consideration. In worst case we also have taken consideration boiler blow

down, cooling waste water and scrubber waste water including washing waste water. In any

case our industrial waste water generation shall not exceed 27.98 KLD.

Quality of Effluent-High COD Stream – Existing

Quality of Raw Effluent – After Expansion

Quality of Effluent-High COD Stream (24.84 KLD) – After Expansion

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Quality of Effluent-Low COD Stream (27.23 KLD)

NOTE: *Due to efficient removal of solvent in stripper. # Considering mixing of domestic, Low COD Stream & Solvent Free Effluent Stream with low COD effluent (11% dilution). ** Due to efficient removal of Organic matter in primary treatment.

Brief justification in case of no process effluent generation or no industrial effluent

generation or no high concentration effluent generation from proposed project

(Whichever is applicable).

Whichever is applicable).

Not Applicable

D-4 Mode of Disposal & Final meeting point (Existing and Proposed)

Existing and Proposed

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Domestic: Existing– Domestic effluent shall be disposed in to Septic tank / Soak pit

system.

Proposed– Domestic effluent shall be sent to ETP along with Low COD

industrial effluent.

Industrial: Existing – Industrial wastewater generated from process and other

ancillary operation is treated in to in-house for primary treatment and after

confirming CETP inlet norms it is send to CETP of M/s. ETL for the further

treatment and final disposal.

Proposed –Domestic and Industrial wastewater generated from

manufacturing process and other ancillary operation shall be segregated in

two different streams like low COD and high COD stream for which unit will

provide two separate collection tank for the same.

High COD stream of effluent (24.84 KLD) will be allow into ETP-1 for

primary (neutralization) treatment and then sent to solvent stripper to

remove mixed solvent. After than solvent free effluent (24.59 KLD) will be

mixed with domestic effluent (1.05 KLD) &Low COD stream of effluent (2.09

KLD) generated from boiler, cooling & scrubber will be allow in ETP-2 for

primary treatment to remove organic matter, VOC etc. From ETP – 2, 0.5

KLD treated water will be sent to CETP of M/s. ETL for further treatment and

final disposal. Unit has valid CTO/CCA. And remaining treated water (27.23

KLD) will be sent to In-house MEE from where water will be concentrated to

recover salt and condensed water. Condensed water will be allowed in RO

Plant. RO Reject water will be allowed to inlet of MEE for further treatment

and RO Permeate water will be reuse in washing, cooling, scrubber and

boiler. Hence, proposed expansion will be ZLD

-

Clearly mention about final disposal


For Domestic waste water: 1.05 KLD

Capacity of STP: Not Applicable (Domestic Water < 10 KLD)



Treatment scheme including segregation at source. (Give Characteristics of each stream i.e. COD, BOD, TDS etc.) In case

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of stream segregation, Separate ETP (ETP-1, ETP-2….) for each stream shall be proposed.

In-house ETP 1 (High COD Stream) of Capacity 25.00 KLD will be installed having Primary

Treatment (pH Adjustment).

In-house ETP 2 (Low COD Stream) of Capacity 30.00 KLD will be installed having Primary

Treatment.

In Hose MEE of Capacity 2 m3/h

Quality of Effluent-High COD Stream – Existing

Quality of Raw Effluent – After Expansion

Quality of Effluent-High COD Stream (24.84 KLD) – After Expansion

Quality of Effluent-Low COD Stream (27.23 KLD)

NOTE: *Due to efficient removal of solvent in stripper. # Considering mixing of domestic, Low COD Stream & Solvent Free Effluent Stream with low COD effluent (11% dilution). ** Due to efficient removal of Organic matter in primary treatment.

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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. Unit will maintain ZLD for proposed expansion project.


Domestic effluent shall be sent to ETP along with Low COD industrial effluent.

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

allowed segregated in two different stream: Low COD and High COD

High COD stream of effluent (24.84 KLD) will be allow into ETP-1 for primary (neutralization)

treatment and then sent to solvent stripper to remove mixed solvent. After than solvent free

effluent (24.59 KLD) will be mixed with domestic effluent (1.05 KLD) & Low COD stream of

effluent (1.84 KLD) generated from boiler, cooling & scrubber will be allow in ETP-2 for

primary treatment to remove organic matter, VOC etc. From ETP – 2, 0.5 KLD treated water

will be sent to CETP of M/s. ETL for further treatment and final disposal. Unit has valid

CTO/CCA. And remaining treated water (27.23 KLD) will be sent to In-house MEE from where

water will be concentrated to recover salt and condensed water. Condensed water will be

allowed in RO Plant. RO Reject water will be allowed to inlet of MEE for further treatment and

RO Permeate water will be reuse in washing, cooling, scrubber and boiler. Hence, proposed

expansion will be ZLD

D-6 In case of Common facility (CF) i.e. CETP, Common Spray dryer, Common MEE, CHWIF etc.


CETP: M/s ETL, Ankleshwar.


occupied capacity and spare capacity and norms of acceptance of effluent from

member unitsin-line with the direction given by GPCB vide Letter No.

GPCB/P-1/8-G (5)/550706 dated 08/01/2020.

Unit has membership form M/s. ETL for wastewater disposal letter no

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Page 207 of 232

ETL/ANK/2009/519 dated 01/08/2009


(Existing and Proposed)

WATER BALANCE DIAGRAM (EXISTING – As Per CCA))

FOR EXISTING PRODUCTS AFTER EXPANSION

E AIR

E-1 Brief Note on fuel based Heat energy requirement and worst case

scenario thereof:

Electric power requirement for project is 125 KVA. After expansion, One D. G. Set of capacity

100 KVA will be installed.

After Expansion, boiler of Capacity 1.5 TPH will be installed.

Maximum steam required from Steam Boiler will be around 1200 kg/hr.

of 232


Page 208 of 232

Fuel Requirement:

Existing: Solid – Steam Coal – 0.3 MT/Day

Additional: Gaseous – Natural Gas - 3000 m3/Day Or Solid – Briquettes of Bio Coal – 5.5

MT/day



(In case of Project located within CPA/SPA , APCM shall be in line to the mechanism published in the

MOEFCC‘s OM vide dated 31.10.2019)

Existing & Proposed

Sr. no.

Source of emission

With Capacity

Stack Height (meter)

Type of Fuel

Quantity of Fuel MT/Day

Type of emissions

i.e. Air Pollutants

Air Pollution Control

Measures (APCM)

EXISTING

1. Furnace 30.0 m Steam

Coal

0.3

MT/day

PM, SO2,

NOX

Adequate stack

height provided

PROPOSED

2. Boiler (Capacity: 1.5 TPH )

30.0 m

Natural Gas OR

3000

m3

/day

PM, SO2,

NOX

Adequate stack height will be

provided

Briquettes of Bio Coal

5.5 MT/Day

PM, SO2,

NOX

Multi Cyclone Separator +

Water Scrubber

3.

D. G. Set (Stand by) (Capacity: 100 KW

7.0 HSD 27 Lit/h PM, SO

2,

NOX

Adequate stack height will be

provided

E-3 Process gasi.e. Type of pollutant gases (SO2, HCl, NH3, Cl2, NOxetc.)

Existing & Proposed

Sr. no.



Type of emissions

i.e. Air Pollutants (SO2, HCl, Cl

etc.)

Stack/Vent Height (meter)


EXISTING

1 Reactor HCl/ Cl2 30.0

Two Stage Water Scrubber followed by Alkali Scrubber

PROPOSED

2 Reaction Vessel (Product No. 6, 7 Process: Sulphonation#)

HCl 20.0 Two Stage Water Scrubber followed by Alkali Scrubber

3 Reaction Vessel (Product No. 3, 5, 6, 7, 8 Process: Sulphonation)

SO2 20.0 Two Stage Alkali Scrubber

of 232


Page 209 of 232

4 Reaction Vessel (Product No. 6 Process: Amination)

NH3 20.0 Two Stage Water Scrubber

5 Reaction Vessel (Product No. 1, 4, 7 Process: Nitration)

NOx 20.0

Adequate Stack Height will be provided

Note:

Details of gaseous raw materials used in proposed project

No any Gaseous RM will be used

Estimation of process gas emission (Product wise and Total)

Sr. No.

Product No. Type of

emission Max. Emission

(MT/Day)

1. 3 SO2 0.08

2. 5 SO2 0.09

3. 6

SO2 1.35

HCl 1.03

NH3 0.01

4. 7 SO2 0.51

HCl 0.03

5. 8 SO2 0.01

Requirement of the scrubbing media (KL per Day) considering solubility (Product wise

and Total)

Sr. No.

Type of emission Name of Scrubbing Media Requirement of

Scrubbing media (Kl/Day)

1. HCl Two Stage Water Scrubber

followed Alkali Scrubber 2.40

2. SO2 Two Stage Alkali Scrubber 3.16

3. NH3 Two Stage Alkali Scrubber 0.02

Yearly generation of all bleed liquors (MT/KL per Annum) as mentioned above and its

sound management in HW matrix.

Sr. No.

Type / Name of Hazardous waste

Specific Source of generation (Name

of the Activity, Product etc.)

Total Quantity (MT/Year)

Management of HW

of 232


Page 210 of 232

1. Sodium Sulfite (25- 41 %)

Scrubber

(Product No. 3, 5, 6, 7, 8)

1624.08

Collection, Storage, Transportation (through GPS mounted vehicle) and Disposed by selling to authorized end user whom have valid permission from GPCB as per Haz. Waste Rule-9

-


Raw materials will be stored in isolated storage area and containers will be kept tightly closed. To

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

liquid material will be charged through closed pipeline.

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 leakages.

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

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

and material handling will be minimized.

To minimize fugitive emission due to vehicle movement, regular water sprinkling will be carried out

on road and paved road will be maintained.

F Hazardous waste

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

Note:





calculations shall be incorporated in EMP details separately.



Existing & Proposed

Sr. no.

Type/ Name of

Hazardous waste

Specific Source of generation(Name of

the Activity, Product etc.)

Category and

Schedule as per

HW Rules.

Quantity (MT/Annum)

Management of HW Existing

Proposed

Total

1 Process

Waste Process 13.20 0.18 - 0.18

Collection, Storage,

Transportation &

Disposal at TSDF

BEIL

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Page 211 of 232

2

Empty

Barrels /

Container

s / Liners

contamin

ated with

hazardou

s

chemicals

/ Wastes

Raw

Materials

&

Finished

Products

33.1

(Sch. I) - 40.00 40.00


Transportation

(Through GPS

Mounted Vehicles)

and Disposal by

selling to registered

recycler approved by

GPCB / CPCB /

reuse within

premises

3 ETP

Sludge

Effluent

Treatme

nt Plant

35.3

(Sch. I) - 81.89 81.89


Transportation

(Through GPS

Mounted Vehicles)

and Disposal at

TSDF site – for

secured landfill

4 MEE Salt MEE

Plant

35.3

(Sch. I) - 317.45

317.4

5


Transportation

(Through GPS

Mounted Vehicles)

and Disposal at

TSDF site – for

secured landfill

5 Used or

Spent Oil

D. G. Set

&

Machiner

y

5.1

(Sch. I) - 2.50 2.50


Transportation

(Through GPS

Mounted Vehicles)

and Disposal by

selling to Registered

Re-refiners approved

by GPCB / CPCB

/reuse for lubrication

6 Spent

Solvent

Process

(Product

No. 1, 6,

7)

28.6

(Sch. I) - 5702.46

5702.

46

Collection, storage,

recovered through

in-house distillation

and 100 % reuse

within premises in

(Product No. 1, 6, 7)

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Page 212 of 232

7 Mixed

Solvent Stripper

28.6

(Sch. I) - 90.00 90.00


Transportation

(through GPS

mounted vehicle)

and Disposed by

selling to authorized

end user whom have

valid permission from

GPCB as per Haz.

Waste Rule-9

8 Distillation

Residue

Process

Distillatio

n

(Product

No. 1, 6,

7)

20.3

(Sch. I) - 36.36 36.36


Transportation

(Through GPS

Mounted Vehicles)

and Disposal for

incineration for

existing quantity and

proposed quantity

will be sent for co-

processing

9

Sodium

Bisulfate

(20 –

30%)

Process

(Product

No, 5)

28.1

(Sch. I) - 797.34

797.3

4


Transportation

(through GPS

mounted vehicle)

and Disposed by


end user whom have


GPCB as per Haz.

Waste Rule-9

10 Sodium

Sulfite

Scrubber

(Product

No. 3, 5,

6, 7, 8)

28.1

(Sch. I) - 1624.08

1624.

08


Transportation

(through GPS

mounted vehicle)

and Disposed by


end user whom have


GPCB as per Haz.

Waste Rule-9

of 232


Page 213 of 232

11

Dil. HCl

Solution

(10 -

25%)

Scrubber

(Product

No. 6, 7)

28.1

(Sch. I) - 739.32

739.3

2


Transportation

(through GPS

mounted vehicle)

and Disposed by


end user whom have


GPCB as per Haz.

Waste Rule-9

12

Liquor

Ammonia

(10 –

25%)

Scrubber

(Product

No. 6)

28.1

(Sch. I) - 12.12 12.12

Collection, Storage

and

entire 100% quantity

will be reuse in

process

(Product No. 6)

13

Off

Specificati

on

Products

Mfg.

Process

(Batch

Failure)

28.4

(Sch. I) -- 1.00 1.00


Transportation

(Through GPS

Mounted Vehicles)

and Disposal co-

processing

-


(For HW management)


Unit has taken membership for TSDF site of M/s. BEIL. Ankleshwar dated 03/08/2009.

Unit has obtained NOC membership for TSDF & co-processing site of M/s. BEIL. Ankleshwar

for proposed waste generation.


(MSW and others)

Sr. no.



Quantity (MT/Annum)


Existing Proposed Total

1 Fly Ash Boiler & APCS

-- 198.00 198.00

Collection, Storage, Transportation (through GPS mounted vehicles) & Disposal by selling to Cement /Brick manufacturing unit/ Local road contractor.

of 232


Page 214 of 232

Sr. No.

Type of Waste Source of

Generation

Category of

Waste Disposal

1. Concrete and Bricks material

Proposed construction

activity

C & D Waste

Temporary store, reuse to increase plinth level and in road area

Steel, glass, wood To be sell local scrap vendor

2. Domestic Waste (Food waste, Plastic, Paper etc.)

Employees working in the

premises

MSW Collected in separate bin and disposed to bin of GIDC.

3. Industrial Waste (Glass wool [Insulating Material, Scrap])

Steam Pipe & Vessels

ISW Sell to local scrap vendor

4. Industrial Waste (Wooden pellets)

From Raw Material

&Product storage area

ISW Sell to local scrap vender

5. E-waste Entire Plant E-waste Collection, Storage and disposal to GPCB authorized E-Waste Management facility


G-1 Brief Note on types of solvents, Details of Solvent recovery, % recovery, reuse

of recovered Solvents etc.

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

reused in process and residue will be disposed for co-processing.

Type of solvents % recovery % Losses

Air Water Haz

Ethylene DiChloride 97.57 0.1215 0.243 1.8225

Meta dichloro benzene 98.65 0.0675 0.135 1.0125

Methanol 96.5 0.175 0.35 2.625

Methylene Dichloride 97.88 0.106 0.212 1.59

Toluene 98.93 0.0535 0.107 0.8025


LDAR programs will be done by Instrument monitoring and Physical inspection.

of 232


Page 215 of 232

Physical inspections will be done for heavy liquids below the vapor pressure thresholds.

Physical inspections rely on the visual detection of dripping liquids.

In In addition to LDAR program, following safety measures will be taken to prevent losses of

solvent in atmosphere;

To achieve more than 95% recovery, unit will provide vacuum distillation, double

condensers with second condenser using chilled water as cooling media. The

condensers shall be provided with sufficient Heat Transfer Area and residence time

for maximum recovery.

VOC detectors will be installed to detect any solvent leakages during storage and

handling.

In warding, storage and consumption of solvents in various products shall be

measured through Level Transmitters and Load cells weighing systems resp. The

quantity at each stage shall be reconciled periodically to arrive at Losses.

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


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

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

Regular maintenance of valves, pumps, flanges, joints and other equipment will be done to

prevent leakages and thus minimizing the fugitive emissions of VOCs.

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

and temperature.

Ensure minimum number of flanges, joints and valves in pipelines.

Proper preventive maintenance of roofs and seals for tanks

Monitoring and preventive maintenance of valves, flanges, joints, etc.

VOC detectors will be installed to detect any solvent leakages during storage and handling.

of 232


Page 216 of 232

Justification of Reuse of solvent

Name of Solvent Total requirement Total quantity of solvent recovered

Ethylene DiChloride 33.00 32.20

Meta dichloro benzene 237.41 234.20

Methanol 2750.00 2653.75

Methylene Dichloride 2104.85 2060.23

Toluene 172.70 170.85

H SAFETY details



-


Tank

Number of

Tanks

Hazardous

Characteristi

cs of

Chemical

-- -- -- -- --


Brief note on storage of Hazardous chemicals other than Tanks i.e. Drum, Barrels,

Carboys, Bags etc.

Safety Precaution for storage & Handling of Methanol:

Methanol is Flammable. Vapors may form explosive mixtures with air. Vapors may travel to

source of ignition and flash back. Containers may explode when heated. Vapors may form

explosive mixtures with air.

Keep in a dry, cool and well-ventilated place. Keep Tank tightly closed in a dry and well-

ventilated place. Keep away from heat and sources of ignition. Proper and sufficient fire

fighting arrangement will be provided in and around the storage.

Avoid contact with skin and eyes. Do not breathe vapors or spray mist. Remove all sources of

ignition. Use only non-sparking tools.

Wash hands before breaks and immediately after handling the product. Keep away from open

flames, hot surfaces and sources of ignition.

To avoid ignition of vapors by static electricity discharge, all metal parts of the equipment

must be grounded. Take precautionary measures against static discharges. Adequate

earthing shall be provided during unloading & its transfer.

Safety Precaution for Storage & Handling of Acetic Anhydride:

Acetic Anhydride is a highly corrosive chemical and contact can severely irritate and burn the

of 232


Page 217 of 232

skin and eyes with possible eye damage. Breathing Acetic Anhydride can irritate the nose,

throat and mouth. High concentration can cause severe lung damage with coughing. It can

cause skin allergy.

Store in tightly closed drum in a cool, dry and well-ventilated area. Keep away from

heat/sparks/open flames/hot surfaces. Keep away from water.

Safety shower and eye washer will be provided nearby storage area.

Personnel working with Acetic Anhydride should be trained on its proper handling and

storage. Proper personal protective equipment such as gloves, safety goggles and face mask

shall be provided.

Safety Precaution for Storage and Handling of Liquid Ammonia:

Avoid contact with skin and eyes. Avoid inhalation of vapour or mist.

Store in cool place. Keep container tightly closed in a dry and well-ventilated place.

Containers which are opened must be carefully resealed and kept upright to prevent leakage.

Storage area have cross air ventilation, no direct sun light, storage temp. below 40 deg. C.

Safety Precaution for Storage & Handling of Nitric Acid

Nitric acid will be stored in Drum. Storage Drum will be stored away from the process plant.

During handling of nitric acid, adequate PPE‘s will be provided to worker like chemical safety

glasses, a face shield for splash protection, gloves etc.

Tanker unloading procedure will be prepared and implemented. The unloading area should

be built in such a way that acid from leaks, spillage and overflow will be collected and led to a

safe place.

The hose material and the couplings used for unloading must not react with nitric acid (for

example, bronze couplings are unsuitable).

Caution note and emergency handling procedure will be displayed at unloading area and

trained all operators.

NFPA label will be provided.

Safety shower, eye wash with quenching unit will be provided in storage area.

Vehicle drivers who transport nitric acid by road must carry the protective equipment which is

specified in the TREM card for road traffic, readily available in the vehicle.


Type of

Hazardous

Chemicals

Safety measures

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Page 218 of 232

Explosive Standard Operating procedure shall be made for before Gas

charging into reactor and after completion of reaction

SOP will be prepared and operators will be trained for the

same..

Safety valve and Rupture disc will be provided on reactor.


Flame arrestor will be provided on vent line of reactor and it will

be extended above the roof level.

Static earthing and electric earthing (Double) will be provided.

Gas detector will be installed for early detection of gas leak.

Toxic and

Corrosive

Storage area have cross air ventilation, no direct sun light,

storage temp. below 40 deg. C.

Containers which are opened must be carefully resealed and

kept upright to prevent leakage.

Charging in reactor shall be carried out through vacuum pump.

Avoid contact with skin and eyes. Avoid inhalation of vapour or

mist. during handling using protective gloves/ protective

clothing/ eye protection / face with proper respiratory

protection. Proper label and identification board /stickers will be

provided in the storage area. Safety showers and eye wash

stations will be installed near the storage area.

Flammable Keep in a dry, cool and well-ventilated place. Keep Tank tightly

closed in a dry and well-ventilated place.

Keep away from heat and sources of ignition. Flammables

area.

Avoid contact with skin and eyes. Do not breathe vapors or

spray mist. Remove all sources of ignition. Use only non-

sparking tools.

Wash hands before breaks and immediately after handling the

product. Keep away from open flames, hot surfaces and

sources of ignition.

To avoid ignition of vapors by static electricity discharge, all

metal parts of the equipment must be grounded. Take

precautionary measures against static discharges.

Dyke wall will be provided at tank storage area.

of 232


Page 219 of 232

Applicability of PESO : Will be taken


(Hydrogenation process, Nitration process, Chlorination process, Exothermic Reaction etc.)

-

Type of

Process


Nitration

process

Nitration will be done in closed S.S vessels.

Nitric acid will be used for nitration process. Nitric acid is an

extremely corrosive acid capable of causing severe chemical

burns very rapidly. Because of the hazards posed by nitric acid, it

is important to take safety measures whenever handling it.

In our nitration process, exothermic reaction will be controlled by

adequate dosing of reaction chemicals in a fixed time (not short

duration) having adequate cooling water circulation in jacket of

reaction vessels. Thus, any energy generated due to exothermic

reaction will be controlled by external cooling circulation and

therefore vessels will not be pressurized.

The nitration reaction will be controlled by systematic cooling

design to withdraw the energy evolved.

Adequate pressure relief valve will be provided for each vessels

having pressure release capacity will be kept below -3 kg/cm2than

that of reaction vessels.

Exothermic

Reaction

Exothermic reaction will be controlled by adequate dosing of reaction

chemicals in a fixed time (not short duration) having adequate cooling

water circulation in jacket of reaction vessels. Thus, any energy

generated due to exothermic reaction will be controlled by external

cooling circulation and therefore vessels will not be pressurized.


-

Total Plot Area: 5000.00 Sq. meter

Area utilized for plant activity: 430.00 Sq. meter

Area utilized for Hazardous Chemicals

Storage:

100.00 Sq. meter

Number of Floors: G + 2

Water requirement for firefighting in KLD : 5652Ltr

of 232


Page 220 of 232

Water storage tank provided for firefighting in

KLD:

Existing: 50000 Ltr Proposed: 150000 Ltr

Details of Hydrant Pumps: 2

Nearest Fire Station : Fire Station,

Ankleshwar GIDC:

2.25 km

Applicability of Off Site Emergency Plan: Will be Prepared

-


Unit will take fire NOC after getting EC


-



Area provided for OHC: 30 Sq. m.


Nearest General Hospital : General Hospital, Ankleshwar 0.50 km

Name of Antidotes to be store in plant : Diazem – 1 mg/Kg.(Intravenous)

Epinephina, Efidrine, Ethanol, Milk of

Magnesia, Soda Water, Castor Oil,

Soframycine, Hydrocortisone (200 mg at

every 4 hrs.). Milk of Magnesia, Ascorbic

acid for eye injury; Paracetamol for Gastric

damage effect.



Project proponent (PP) and Technical expert of PP, M/s. Envirocare Technocrats Pvt. Ltd remains

present during video conference meeting.

Committee noted that the proposal is for expansion project in GIDC Ankleshwar. Unit is having valid CCA

of the Board for existing plant. Committee noted that self certified compliance report of CCA is submitted

by the unit. PP submitted details regarding area adequacy. Source of water is GIDC. Product profile

along with end use discussed in depth. Committee insisted for R & D production capacity in Kg/Month

and PP later on submitted revised product profile with mentioning R & D product capacity-100 Kg/Month.

of 232


Page 221 of 232

Committee noted that PP has submitted undertaking regarding there is no legal court case and public

complaint against unit. PP informed that two Show cause notice (SCN) issued by GPCB in last three

years and compliance reply of SCN presented by the unit. Looking to plot area and existing inorganic

production plant and proposal of new API products, Committee insisted for submit revised layout plan

with mentioning separate existing and proposed production plant and floor wise emergency stair case in

different location of plant area which is later on submitted by PP.


segregated. High COD stream will be passed treated in ETP-1 and then mixed with low COD stream for

further treatment. Low COD stream along with treated high COD stream will be treated in ETP -2 and

partly treated effluent will be sent to CETP of M/s ETL for further treatment and rest of treated effluent

will be evaporated in in-house MEE.MEE condensate will be further treated in RO Plant. Committee

asked for compliance of Direction under section 18(1) (B) ,PP informed that waste water discharge

quantity is not increase after expansion and also mentioned quality of waste water discharge with stage

wise reduction of BOD, COD, Ammonical nitrogen and TDS in ETP and MEE.

PP submitted that they have proposed boiler and DG set. Fuel used will be Natural gas or bio coal for

boiler. MCS and water scrubber as APCM proposed for bio coal fired boiler. Committee insisted for

adequate stack height for coal fired furnace and PP later on submitted revised stack height of 30 meter

for coal fired furnace. Two stage scrubbers will be provided as APCM with each process reactor stack.

PP submitted Hazardous Waste Matrix as per Hazardous Waste Rules – 2016.





centre (OHC) and process hazard and its safety control measures. Committee noted that PP presented

details of auto control system like PLC with SCADA system. Committee insisted for provision of Proximity

suit & Trolley pump and provides the Fire water Storage tank capacity of 200 KL and PP later on

submitted revised fire water tank and fire extinguisher details.


CER, LDAR and solvent recovery etc.







& 14/11/2019.


of 232


Page 222 of 232





amendments.



5. GPCB shall ensure compliance of direction under section 18 (1) (b) of the Water (Prevention and

Control of Pollution) act, 1974 issued by CPCB regarding compliance of wastewater disposal from

common ETP and also that the pollution load is not increased in the CPA/SPA for the compliance of

Hon‘ble NGT order.

6. PP shall use natural gas for utilities preferably but in case use of other fuel, PP shall put properly

designed APCM with regular/periodic stack monitoring system to ensure that there shall be no

increase in pollution load for the compliance of directives of Honorable NGT.

7. Unit shall install CEMS [Continuous Emission Monitoring System] in line to CPCB directions to all


emission as per pollutants discharge/emission from respective project and an arrangement shall also

be done for reflecting the online monitoring results on the company's server, which can be



8. Wastewater shall be fed to MEE only after providing adequate treatment in such a way that no


9. The PP shall develop green belt [2010 m2 inside plant premises i.e. 40.09 % of total plot area] as per

the undertaking submitted before SEAC. Green belt shall be developed with native plant species that

are significant and used for the pollution abatement as per the CPCB guidelines. It shall be
















of 232


Page 223 of 232

applicable)





2016.





accident.











k) Unit shall provide adequate safety system such as water sprinklers, water curtains, foam


l) Unit shall provide safety valve and rapture disc, as well as auto dump or auto quenches/,

suppresses system for nitration reaction vessel safety.

11. SIA/GJ/IND2/57519/2020 M/s. Krimson Polymers LLP

Survey No. 67/2/Paiki, 2 Plot No.1, Shika

rpur, Ta: Bhachau, Dist:

Kutchh

Screening and scoping


Project status: New

This office has received an application vide their online proposal no. SIA/GJ/IND2/57519/2020 dated

17/11/2020 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.

of 232


Page 224 of 232

This is a new unit and proposes for manufacturing of synthetic organic chemicals as tabulated below,

Sr.

No.

Name of the

Products

CAS no. /CI

no.

Quantity

MT/Month

End-use of the products

1 Chloranil 118-75-2 20

In chemical Industries and

in Textile Industries for

printing and dyeing.

2 Carbazole 86-74-8 10

3 Pigment Violet 23 6358-30-1 20

4 Pigment Red 122 980-26-7 20

5 Pigment Yellow 138 30125-47-7 20

Total 90

The project falls under Category B1 of project activity 5(f) as per the schedule of EIA Notification 2006.

The proposal was considered in the SEAC video conference meeting dated 17.12.2020.

Project proponent and technical expert of PP, M/s. Enviro Fluid Consultants remains present during

video conference meeting dated 17/12/2020.

Committee noted that this is Greenfield project at Survey No. 67/2/Paiki 2, Plot no. 1, Village: Shikarpur,

Taluka: Bhachau, District: Kutch. Unit is located outside Notified area.

Committee noted that prefeasibility report (PFR) for proposed synthetic organic chemical product is

prepared by M/s. Enviro Fluid Consultants and they are not accredited as per the Amended EIA

Notification videS.O.648 (E) dated 03/03/2016.

Committee took a note of Minutes of meeting of EAC, MoEF&CC (IA Division-Industry-2 Chemical

sector) dated 24/11/2020. MoEF &CC has insisted on QCI/NABET accredited consultants. While

examining the B1 category of applications, it has refused to consider/entertain the proposals which were

not prepared by QCI/NABET accredited consultants.

In view of the above and after deliberations, it is felt that SEAC shall not consider/entertain Terms of

Reference(ToR) application as it is a part of EIA preparation for B1 category wherein prefeasibility report

prepared by consultant, not accredited with QCI/NABET as per the Amended EIA Notification

videS.O.648 (E) dated 03/03/2016.

After detailed discussion, Committee unanimously decided to defer the project and consider the

same in one of the upcoming meeting of SEAC after satisfactory submission of following details:

1. Prefeasibility report for proposed project shall be prepared by EIA consultants having accreditation

with QCI/NABET as per the Amended EIA Notification vide S.O.648 (E) dated 03/03/2016.

2. Status of EIA Consultant for accreditation with QCI/NABET as per the Amended EIA Notification

vides S.O.648 (E) dated 03/03/2016 for proposed project.

12. SIA/GJ/IND2/55602/2020 M/s. Umiya Enterprise

Plot No. 131, GIDC Talod, Ta. Talod, Dist.

Sabarkantha

Screening and scoping

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Page 225 of 232


Project status: New

This office has received an application vide their online proposal no. SIA/GJ/IND2/55602/2020 dated

21/10/2020 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 and proposes for manufacturing of synthetic organic chemicals as tabulated below,

Sr. No.

Name of Product CAS No. Quantity

MT/Month Final Application

of Product

1. Reactive Yellow HE4G 59112-78-6

45

Most suitable for dyeing of cellulosic fibers like cotton, flax, viscose rayon, acetate and jute, Applicable on Leather and Paper coloration.

2. Reactive Yellow H7GL 61969-35-5

3. Reactive Yellow HE6G 77907-38-1

4. Reactive Yellow ME4GL 129898-77-7

5. Reactive Golden Yellow HR 35642-64-9

6. Reactive Golden Yellow MERL

93050-80-7

7. Reactive Green HE4BD 61931-49-5

8. Reactive Red HE3B 61951-82-4



11. Reactive Red ME4BL 93050-79-4

12. Reactive Red ME6BL 125830-49-1

13. Reactive Orange ME2RL 79809-27-1

14. Reactive Orange HER 91261-29-9

15. Reactive Orange 2R 42986-20-1

16. Reactive Magenta HB ---

17. Reactive Violet C4R 12237-11-5

18. Reactive Black B 17095-24-8

19. Direct Black 168 85631-88-5

20. Direct Red 12B 5001-72-9

21. Acid Red 97 61901-18-6 Acid dyes are used to dye protein fibers such as wool, angora, cashmere, and silk, as well the milk protein fiber called Silk Latte, the soy protein fiber called Soy Silk, and the synthetic polyamide fiber nylon in textile industries.

22. Acid Blue 113 33351-05-1

23. Acid Blue 193 12392-64-2

24. Acid Brown 75 8011-86-7

25. Acid Brown 282 12219-65-7

26. Acid Brown 365 63641-88-3

27. Acid Brown 355 60181-77-3

28. Acid Black 194 61931-02-0

The project falls under Category B1 of project activity 5(f) as per the schedule of EIA Notification 2006.

The proposal was considered in the SEAC video conference meeting dated 17.12.2020.

Salient features of the project including Water, Air and Hazardous waste management as below.

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Page 226 of 232

Sr.

no.

Particulars Details

A

A Total cost of Proposed Project

(Rs. in Crores):

1.10 Crores

B Total Plot area ( sq. meter) 1000 Sq. m.

Green belt area

( sq. meter)

120 Sq. m. (12 %) & remaining 21%

green belt area will be develop in

GIDC area after obtaining permission

of association.

C Employment generation 10

D Water

i


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

GIDC Water Supply

Status of permission from the concern authority. ---

ii Water consumption (KLD)

Category

Quantity

KLD

Remarks

(M) Domestic 1.0

(N) Gardening 1.0

(O) Industrial

Process 9.0

Washing 1.0

Boiler 2.0

Cooling 1.0


Total (A + B + C) 15.0

1) Total water requirement for the project: 15.0 KLD

2) Quantity to be recycled: 8.3 KLD

3) Total fresh water requirement: 6.7 KLD

(Total water requirement = Fresh water + Recycled water)

15.0 = 6.7 + 8.3

iii


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Page 227 of 232

Category Waste water

KLD

Remarks

(I) Domestic 0.8

(J) Industrial

Process 10.5

Washing 1.0

Boiler 0.2

Cooling 0.1

Total Industrial waste

water

11.8

Total [A + B] 12.6

-

iv Treatment facility within premises with capacity


In house ETP (Primary) & RO Plant

Treatment scheme including segregation at source.

Total Industrial Wastewater generation will be 11.8 KLD and will be send to ETP Plant. After

treated effluent will be send to RO plant. RO Permeate water 8.3 KLD will be reuse for industrial

activity and RO rejected water 3.5 KLD will be send to common spray dryer at Chhatral

Environment Management System Pvt. Ltd. Dhanot for spray drying.


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 CETP discharge


Unit will achieve zero liquid discharge by discharge proposed effluent to common spray dryer.

v Mode of Disposal & Final meeting point

Domestic:

Send to Modular STP Plant & treated effluent will send to CEMSPL for spray

drying

Industrial:

Total Industrial Wastewater generation will be 11.8 KLD and will be send to ETP

Plant. After treated effluent will be send to RO plant. RO Permeate water 8.3

KLD will be reuse for industrial activity and RO rejected water 3.5 KLD will be

send to common spray dryer 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 etc. Name of

CF

Chhatral Environment Management System Pvt. Ltd. Dhanot

Membership of Common facility (CF)

(For waste water treatment)

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Chhatral Environment Management System Pvt. Ltd. Dhanot

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

viii Reuse/Recycle details (KLD)

Total reuse 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.)

(mg/L)

Remarks

regarding

feasibility to

reuse i.e.

8.3 KLD Reuse Industrial

Activity

COD – 24

BOD – 6

TDS - 100

--

E Air

i Flue gas emission details


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Page 229 of 232

-

Sr.

no.

Source of

emission

With

Capacity

Stack

Height

(meter)

Type

of

Fuel

Quantity

of Fuel

MT/Day

Type of

emissions

i.e. Air

Pollutants

Air

Pollution

Control

Measures

(APCM)

1

Steam Boiler (800

Kg/Hr)

11 Bio-Coal

1.7 SPM SOX NOX

Cyclone Separator

followed by wet

scrubber

2

Hot Air Generator

(1.5 Lacks KCal)

11 Bio-Coal

0.5 SPM SOX NOX

Cyclone Separator

followed by bag filter

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

- There will be no process gas emission from proposed manufacturing activity.

iii Fugitive emission details with its mitigation measures:

As below:

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 wastes

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

2016.

i

Sr. no.




Quantity (MT/Annum)

Management of HW

1 ETP Sludge

Effluent Treatment Plant

35.3 15 Collection, Storage, Transportation, Disposal at TSDF Site.

2 Used or Spent Oil

Lubricants from Machinery

5.1 0.05

Collection. Storage, Transportation & Disposal by selling to Registered Recycler.

3 Empty Barrels/ From Raw 33.1 5.0 Collection. Storage,

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Containers/ Liners contaminated with hazardous chemicals waste

Material/ Production Section

reuse for packing of ETP waste or sale to Authorized Recycler

4

Fly Ash From Utilities -- 15600

Collection, Storage, Transportation, Disposal at Brick Manufacturing Unit.

-

ii Membership details of TSDF, CHWIF etc.

(For HW management)

We will applied.

iii Details of Non-Hazardous waste & its disposal

(MSW and others)

STP Waste

0.3 MT/ Year & its use as manure in

the premises.


---

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


---

ii VOC emission sources and its mitigation measures

Not Applicable

H Details regarding storage of Hazardous chemicals

Storage details Name of major

Hazardous chemicals

Remarks

Storage tanks Sulphuric Acid (2.9) Hydrochloric Acid (5.5)

---

Drum/Barrel storage Acetic Anhydride (2.1) Sodium Hydroxide (4.4) Ammonia (0.4)

---

Applicability of PESO :

Due to less storage quantity PESO was not applicable.

Technical presentation submitted by PP was considered during SEAC meeting dated 17/12/2020.

Project proponent and technical expert of PP, M/s. Bhagwati Enviro Care Pvt. Ltd remains present during

video conference meeting dated 17/12/2020.

Committee noted that this is Greenfield project at GIDC Talod. PP mentioned that water supply source

will be GIDC water supply.

Consultant is having QCI/NABET accreditation certificate of consultant for sector 5(f) for preparation of

EIA/EMP report.

PP presented layout plan for proposed project and plot allotment letter of proposed project. Committee

deliberated at length regarding GIDC Talod establishment and is of year before 2006.

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PP mentioned that total effluent will be treated in ETP units and then will be sent to common spray dryer

facility of M/s. Chhatral Enviro Management System Pvt. Ltd for evaporation.

PP mentioned that they have proposed bio coal fired steam boiler and Hot air generator. Committee

insisted for adequate stack height and APCM for boiler in place of cyclone separator. PP has submitted

Hazardous Waste Matrix as per Hazardous Waste Rules – 2016. Committee insisted for submission of

notarized undertaking for adoption of automization process for critical process, obtain Fire NOC

certificate and provision of Occupational health centre (OHC) within premises.

After detailed discussion, Committee 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. Submit membership certificate of common spray dryer facility with mentioning booked

quantity, occupied quantity, spare capacity and inlet norms for acceptance of effluent as per

GPCB letter dated 08/01/2020.

2. Submit adequate APCM and stack height for bio coal fired boiler and Hot air generator.

3. Details of three year greenbelt development program including annual budget, types &number

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

with commitment of the management to carry out the tree plantation activities outside the

premises at appropriate places in surrounding area. Notarized undertaking regarding

development of green belt within premises (Minimum 14500 Sq. m i.e. 33.33 % of the total

plot area) as per the commitment before SEAC. Green belt shall be developed with native

plant species that are significant and used for the pollution abatement as per the CPCB

guidelines.

4. Fund allocation for Corporate Environment Responsibility (CER) for various activities therein.

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

The entire activities proposed under CER shall be part of Environment Management Plan

(EMP) as per the MoEF&CC‘s OM no. F. No. 22-65/2017-IA.III dated 30.09.2020.

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

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

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

proposed for energy conservation.

6. Status of all the applicable rules, acts, regulation, clearances in a tabular form.

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7. Adoption of automization process like DCS/PLC including emergency response to eliminate

risk associated with the hazardous processes, fire safety certificate / Fire No-Objection

certificate (NOC) from the concern authority as per the prevailing Rules / Gujarat Fire

Prevention and Life Safety Measures Act, 2016 and provision of Occupational health

Centre(OHC) within premises.

8. Submit technical justification regarding spent sulphuric acid is not mentioned in Hazardous

waste matrix as per Hazardous waste Rules‘2016.

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

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

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

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

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://environment clearance.nic.in/ along with final EIA report.

The meeting ended with a vote of thanks to the chair. ***

Minutes approved by:

1. Shri Akshay Kumar Saxena, Chairman, SEAC

2. Dr. S. C. Pant, Vice Chairman, SEAC

3. Dr. M. N. Patel, Member, SEAC

4. Shri D. C. Chaudhari, Member, SEAC

5. Shri J. K. Vyas, Member, SEAC

6. Shri Anand Zinzala, Member, SEAC

7. Shri B. M. Tailor, Member, SEAC

8 Shri A. V. Shah, Secretary, SEAC

…..

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