for tor expansion case. 1. basic information of the...

SEAC, Gujarat: of 21

SEAC, Gujarat [TOR – Expansion Case]

For TOR – Expansion Case.

1. Basic Information of the Project:

i Name & Address of the Project site (Complete details with plot no./Survey no., Landmark etc.)

Mahavir Synthesis Private Limited

Block No: 304B, 305 Sachin- Magdalla Road, G.I.D.C., Sachin-394 230, Tal. Chorasi, Dist. Surat, Gujarat

ii Name of the Applicant Mahavir Synthesis Private Limited

iii Address for correspondence Block No: 304B, 305 Sachin-Magdalla Road, G.I.D.C., Sachin-394 230, Tal. Chorasi Surat, Gujarat

iv Contact no. and e-mail ID of the Applicant Mo. no. : 98251 16035

e-Mail: [email protected]

v Aerial distance of nearest Habitat (KM) Nearest Town: Sachin at 3.28 km

vi Longitude & Latitude of the Project Site: (4 corners of the site)

1.Latitude:21°6’15.60”N Longitude: 72°51’18.86”E

2.Latitude:21°6’13.82”N

Longitude: 72°51’23.97”E 3.Latitude:21°6’9.28”N

Longitude: 72°51’17.98”E 4.Latitude:21°6’9.79”N

Longitude: 72°51’25.70”E

vii Total cost of Proposed Project

(Rs. in Crores):

Existing: 4.58 crore Proposed: 20 crore Total: 24.58 crore

viii Total Plot area ( sq. meter)

Existing: 32271 Proposed: 32271 Total:32271

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

Existing: 7035 Proposed: 7035 Total:7035

x Category as per the Schedule to the EIA Notification 2006 i.e. 1(d), 2(b), 5(f) etc.

5 (f) B

xi Applicability of General Conditions of EIA Notification 2006: i.e. Ensure that

I. Protected areas notified under the Wildlife (Protection) Act, 1972;

II. CEPI areas III. Eco-sensitive areas and IV. Inter-state boundaries and

international boundaries; are not located within 5 km or 10 km (as the case may be) area from the

NA

mailto:[email protected]



boundary of the proposed site.

2. Online application proposal no. : SIA/GJ/IND2/20664/2017

3. Date of application for TOR: 12/10/2017

4. Project status: Expansion

5. Product profile: Dyes intermediates

Sr. no.

Name of the Products

CAS no. Quantity MT/Month

End-use of product Existing Proposed

Total Max

Production

1. Schaffer's Acid 93-01-6 35 35 -

2. Broenner's Acid 93-00-5 25 25 -

3. Amino G Acid 86-65-7 25 25 -

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

5. Aryl Sulfonamide - 30 30 -

6. Pyrazolones 108-26-9 30 30 -

7. Condensation Products

4275-07-4 60 60 -

8. Aryl Sulfonic Acid - 55 55 -

AP Group

1 AP-1

1.1 3:5 Dichloro

Aniline(3:5-DCA)

OR

626-43-7 -

12.5

50

1.2 3-

(Trifluoromethyl)

Acetophenone:

(TFMAP) OR

349-76-8 - 25

1.3 Para Cresol 106-44-5 50

1.4 Cyclopropyl

Methyl Ketone

(CPMK)

765-43-5 50

50

2 AP-2

2.1 4-Nitro O-Xylene

(4-NOX) OR

99-51-4 100

200`

2.2 3-Nitro O-

Xylene(3-NOX)

83-41-0 +100

2.3 4-Nitro m-Xylene

or 4-Nitro 1:3-

Xylene(4-NMX)

OR

89-87-2 100

2.4 2-Nitro m-Xylene

or 2-Nitro 1:3-

Xylene(2-NMX)

81-20-9 +17.5

2.5 P – nitro cumene

OR

1817-47-6 50



2.6 O-Nitro cumene 6526-72-3 +40

3 AP-3

3.1 2:3- Dimethyl Aniline OR

87-59-2 75

75


95-64-7 75


87-62-7

75

3.4 2:4-Dimethyl Aniline OR

95-68-1 75

3.5 2-Nitro cumene OR

6526-72-3 75

3.6 4-Nitro cumene 1817-47-6 75

4 AP-4

4.1 2-(2- Amino-

ethoxy)-2’-Chloro-

Diethyl Sulfone

Hydrochloride

Solution

-

25

125

4.2 2:3-Dibromo

Propionyl

Chloride (DBPC)

OR

18791-02-1

25

4.3 2-5-Dihydroxy 1-

4- Dithiane

(DHDT)

40018-26-6

100

MCP Group

5.1 4 - Amino Benzene Sulphonamide

- 50 50

5.2 Broenner’s Acid 93-00-5 25 25

5.3 Amido G Acid 86-65-7 25 25

5.4 Sulpho Gamma Acid(MI007)

90-40-4 25 25

J Acid(MIF005) - 3.75 3.75

5.5 Broenner's Acid Recovered (MII02R)

- 10.625 10.625

Amido G Acid Recovered (MI003R)

- 14.375 14.375

5.6 G-Salt (MDC003) 842-18-2 60 60

R-Salt (MDC004) 135-51-3 10.5 10.5

5.7 Aniline 2:5-Disulphonic Acid (ONCB route)

76684-33-8

50 50



5.8 Aniline 2:5- disulphonic acid

98-44-2 50 OR 50

5.9 2-Amino 4-Hydroxy Benzene Sulfonic Acid

98-37-3 50 50

5.10 2 - Amino 4- Methoxy Benzene Sulphonic Acid (AMBSA)

13244-33-2

20 20

5.11 K-Acid 118-03-6 50 50

5.12 Tobias Acid 117-62-4 100 100

In Organic Product

5.13 Ferrous Sulphate 2500 2500

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

6. Product wise Raw material consumption:

Sr. no.

Name of the Products

Name of the Raw Materials

CAS no. of raw materials.

Quantity MT/Month

Existing Proposed Total

AP Group

1. AP-1

3:5 Dichloro Aniline(3:5-DCA)

98% H2SO4 7664-93-9 - 1.75 1.75

2:6 DCPNA 99-30-9 - 1.15 1.15

35% Nitrosyl Sulfuric Acid

7782-78-7 - 2 2

Water 7732-18-5 - 2.5 2.5

Iron 7439-89-6 - 0.6 0.6

Acetic Acid 64-19-7 - 0.05 0.05

50% H3PO2 soln

63.3-21-5 - 1.5 1.5

48% NaOH soln

1310-73-2 - 0.075 0.075

Toluene 108-88-3 - 1.5 1.5

1.2 3- (Trifluoromethyl) Acetophenone: (TFMAP)

TFMA 455-14-1 - 0.075 0.075

98% H2SO4 7664-93-9 - 1.5 1.5

40% NaNO2 7632-00-0 - 0.95 0.95

50% aldoxime

- 1.03 1.03

Acetic Acid 64-19-7 - 1.025 1.025

CuSO4.5H2O 7758-99-8 - 0.885 0.885

Toluene 108-88-3 - 0.125 0.125

30% HCl 7647-01-0 - 0.075 0.075

Water 7732-18-5 - 1.2 1.2

48% NaOH 1310-73-2 - 1.3 1.3

-



1.3 Para Cresol Water 7732-18-5 - 7.5 7.5

98% H2SO4 7664-93-9 - 5.2 5.2

p-toluidine 106-49-0 - 3 3

Sodium sulphate

7757-82-6 - 0.35 0.35

40% w/w NaNO2

7632-00-0 - 1.96 1.96

-

1.4 Cyclopropyl Methyl

Ketone (CPMK)

Ethyl Acetate

141-78-6 -

10.75 10.75

Sodium Methoxide

124-41-4 - 3 3

Gamma Butyro Lactone

‎96-48-0 -

4 4

80% H2SO4 7664-93-9 - 2.8 2.8

Methanol 67-56-1 - 1.2 1.2

30% HCl 7647-01-0 - 7.1 7.1

Toluene 108-88-3 - 6 6

50% NaOH 1310-73-2 - 3.6 3.6

Water 7732-18-5 - 12.425 12.425

2 AP-2 -

2.1 4-Nitro O-Xylene

(4-NOX) OR 3-

Nitro O-Xylene(3-

NOX)

O-Xylene 95-47-6 -

8.6 8.6

72% w/w HNO3

7697-37-2 - 8.9 8.9

10% NaOH 1310-73-2 - 5 5

98% H2SO4 7664-93-9 - 10 10

2.2 4-Nitro m-Xylene OR 2-Nitro m-Xylene

m-Xylene 108-38-3 - 8.8 8.8

70 % w/w HNO3

7697-37-2 - 3.8 3.8

28% NaCl soln

7647-14-5 - 6 6

98% H2SO4 7664-93-9 - 4.6 4.6

5% NaHCO3soln

144-55-8 - 1.2 1.2

2.3 P – nitro cumene

OR O-Nitro

cumene

Cumene 98-82-8 -

4.3 4.3

98% H2SO4 7664-93-9 - 7.5 7.5

60% HNO3 7697-37-2 - 4.1 4.1

Soda ash 498-19-8 - 0.1 0.1

water 7732-18-5 - 4.4 4.4

3 AP-3 -



3.1 Xylidine or

Dimethyl Aniline

Water 7732-18-5 -

15 15

Iron 7439-89-6 - 4.5 4.5

Acetic Acid 64-19-7 - 0.3 0.3

Nitro Xylene 81-20-9 4.01 4.01

Soda ash 498-19-8 - 0.3 0.3

-

3.2 2-Nitro cumene OR 4-Nitro cumene

Water 7732-18-5 - 15 15

Iron 7439-89-6 - 4.06 4.06

Acetic Acid 64-19-7 0.3 0.3

Nitro Xylene 81-20-9 - 3.975 3.975

Soda ash 498-19-8 - 0.3 0.3

-

4 AP-4 -

4.1 2-(2- Amino-

ethoxy)-2’-Chloro-

Diethyl Sulfone

Hydrochloride

Solution

2-AEE 929-06-6 -

0.65 0.65

30% HCl 7647-01-0 - 1.65 1.65

Thionyl chloride

7719-09-7 - 0.85 0.85

Methanol 67-56-1 - 2.9 2.9

NaOH flakes 1310-73-2 - 0.6 0.6

2-Mercapto ethanol

60-24-2 - 0.55 0.55

Chlorine gas 7782-50-5 - 0.725 0.725

NaHSO3 7631-90-5 - 0.09 0.09

Water 7732-18-5 - 2.375 2.375

4.2 2:3-Dibromo Propionyl Chloride (DBPC) OR

Acrylic Acid 79-10-7 - 0.3 0.3

Bromine 7726-95-6 - 0.66 0.66

Thionyl Chloride

7719-09-7 - 0.59 0.59

4.3 2-5-Dihydroxy 1-4-

Dithiane (DHDT)

Water 7732-18-5 - 4.8 4.8

Vinyl Acetate Monomer

108-05-4 - 5.7 5.7

Chlorine Gas

7782-50-5 - 4.7 4.7

NaOH (48% Sol.)

1310-73-2 - 10.8 10.8

EDCI 1892-57-5 - 4 4

NaSH 16721-80-5 - 12 12

IPA 67-63-0 - 8 8



MCP Group

5.1 4 - Amino Benzene Sulphonamide

Chloro sulphonic acid

7790-94-5 - 6.2 6.2

acetanilide 103-84-4 - 2.35 2.35

Thionyl chloride

7719-09-7 - 2.5 2.5

Ice 7789-20-0 - 15.7 15.7

30 % H2O2 solution

7722-84-1 - 0.6 0.6

23 % NH3 solution

1336-21-6 - 4.8 4.8

NaOH flakes 1310-73-2 - 0.09 0.09

48 % NaOH solution

1310-73-2 - 3.5 3.5

30% HCl solution

7647-01-0 - 3.6 3.6

Water 7732-18-5 - 20.2 20.2

5.2 Broenner’s Acid 23 % NH3solution

1336-21-6 - 1.625 1.625

NaHSO3 7631-90-5 - 0.15 0.15

Schaffer’s Acid

93-01-6 - 1.08 1.08

48 % NaOH 1310-73-2 - 0.05 0.05

98% H2SO4 7664-93-9 - 0.8 0.8

Water 7732-18-5 - 10 10

5.3 Amido G Acid 23% w/w NH3

1336-21-6 - 1.25 1.25

NaHSO3 7631-90-5 - 0.285 0.285

G-Salt 842-18-2 - 1.1 1.1

Water 7732-18-5 - 1 1

98% w/w H2SO4

7664-93-9 - 0.625 0.625

5.4 Sulpho Gamma Acid(MI007)

48 % NaOH 1310-73-2 - 4.2 4.2

J Acid(MIF005) K – Acid 118-03-6 - 1.925 1.925

98% H2SO4 7664-93-9 - 3.66 3.66

Ice 7789-20-0 0.3 0.3

50% H2SO4 7664-93-9 - 0.15 0.15

Ammonia Gas

7664-41-7 - 0.1 0.1

NaHSO3 7631-90-5 - 0.03 0.03

NaOH Flakes

1310-73-2 - 0.18 0.18

KOH Flakes 1310-58-3 - 0.02 0.02

Water 7732-18-5 - 7.1 7.1

NaNO2 7632-00-0- - 0.072 0.072

5.5 Broenner’s Acid Recovered

MI001 ML - - 26 26



Amido G Acid Recovered

Ammonia Gas

7664-41-7 1.225 1.225

23% Ammonia liq.

1336-21-6 - 4.7 4.7

Sodium Bi-sulphite

7631-90-5 - 0.525 0.525

98% H2SO4 7664-93-9 - 1.15 1.15

Water 7732-18-5 - 2.025 2.025

5.6 G-Salt (MDC003) 98% H2SO4 7664-93-9 - 2.05 2.05

R-Salt (MDC004) 23% Oleum 8014-95-7 - 3.05 3.05

Β-Naphthol 90-15-3 - 1.7 1.7

Water 7732-18-5 - 9.275 9.275

KCl 7447-40-7 - 2.8 2.8

NaOH Flakes

1310-73-2 - 0.85 0.85

Aniline oil 62-53-3 -- 0.16 0.16

10% w/w NaCl soln

7647-14-5 - 1.05 1.05

30% w/w HCl

7647-01-0 - 0.6 0.6

NaCl - 0.475 0.475

5.7 Aniline 2:5-Disulphonic Acid (ONCB route)

23% oleum 8014-95-7 - 4.8 4.8

ONCB 88-73-3 - 1.65 1.65

Na2CO3 497-19-8 - 0.575 0.575

NaCl 7647-14-5 - 4.225 4.225

48% w/w NaOH

1310-73-2 - 1.625 1.625

NaHCO3 144-55-8 - 0.2 0.2

NaHSO3 7631-90-5 - 1.25 1.25

30% HCl 7647-01-0 - 3.2 3.2

Iron powder 7439-89-6 - 1.5 1.5

Acetic acid 64-19-7 - 0.025 0.025

Water 7732-18-5 - 14.5 14.5

-

5.8 Aniline 2:5- disulphonic acid

Nitrobenzene

98-95-3 - 1.275 1.275

65% oleum 8014-95-7 - 1.5 1.5

Na2CO3 144-55-8 - 0.875 0.875

Lime 8006-28-8 - 0.725 0.725

Iron 7439-89-6 - 1.55 1.55

CH3COOH 64-19-7 - 0.075 0.075

48% w/w NaOH

1310-73-2 - 0.125 0.125

23% oleum 8014-95-7 - 5.55 5.55

‘C’ powder 7440-44-0 - 0.125 0.125

NaCl 7647-14-5 - 1.7 1.7

Water 7732-18-5 - 23.7 23.7

98% H2SO4 7664-93-9 - 0.65 0.65



5.9 2-Amino 4-Hydroxy Benzene Sulfonic Acid

NaOH flakes

1310-73-2 - 4.6 4.6

Aniline 2:5- DiSA

98-44-2 - 3.2 3.2

Water 7732-18-5 - 2.4 2.4

NaOH 1310-73-2 - 0.5 0.5

30% w/w HCl

7647-01-0 - 14.8 14.8

5.10

2 - Amino 4- Methoxy Benzene Sulphonic Acid (AMBSA)

MAPSA 58-22-0 -

1 1

48 % NaOH 1310-73-2 - 2.85 2.85

Acetic Anhydride

108-24-7 - 0.95 0.95

NaCl 7647-14-5 - 1.75 1.75

MCB 68411-45-0 - 7.5 7.5

NaOH 1310-73-2 - 0.575 0.575

Dimethyl Sulphate

77-78-1 - 0.65 0.65

Soda Ash 498-19-8 - 0.6 0.6

30% HCL 7647-01-0 - 4 4

Water 7732-18-5 - 12.3 12.3

5.11

K-Acid Amino G Acid

86-65-7 - 1.7 1.7

98% H2SO4 7664-93-9 - 1.45 1.45

65% Oleum 8014-95-7 - 5.6 5.6

Water 7732-18-5 - 10.5 10.5

Ice 7789-20-0 - 6.5 6.5

KCl 7447-40-7 - 0.75 0.75

5.12

Tobias Acid EDCl 1892-57-5 - 14 14

BN 10043-11-5 - 3.1 3.1

CSA - 2.75 2.75

45% w/w NaOH

1310-73-2 - 2.45 2.45

23% w/w NH3 soln

1336-21-6 - 6.35 6.35

(NH4)2SO3 10196-04-0 - 2.4 2.4

Darco 7440-44-0 - 0.15 0.15

NaOH 1310-73-2 - 0.15 0.15

98% w/w H2SO4

7664-93-9 - 3.45 3.45

Ice 7789-20-0 - 7.8 7.8

Water 7732-18-5 - 8.8 8.8

Total 640.012

5.13

Ferrous Sulphate Spent Acid - 100 100



Iron Powder 7439-89-6 - 25 25

7. Compliance status of the existing project:

Sr. no.

Particulars Brief Information/Details Remarks

1 Earlier EC details F. No. J-11011/276/2007-IA-II (I)

Earlier Aqua Ace Acid & Intermediate Pvt Ltd, plot no 304-B and 305, GIDC, Sachin, Surat) obtained Environmental Clearance vide letter dated 9th January, 2008.

2 Compliance of EC Compliance of EC vide letter J-11011/276/2007 - IA II (I) dated January 1, 2008 submitted to RO Bhopal

3 Status of inspection by RO-MoEFCC, Bhopal.

NA

4 Status of submission of half yearly return to concern authorities.

Last submitted on December 2016 to Bhopal.

5 Compliance of existing CC&A

1) CCA order No: - AWH-71783, Dated- 13/07/2015 under various Environmental Acts/Rules. 2) Consent is Valid upto 03/04/2020.

6 Legal actions/Closure directions/SCN etc. issued by GPCB.

NA

7 Any Public Complaints NA

8 Is there any litigation pending before any court of Law against the Project ?

NA

8. Water, Air and Hazardous waste management:

Sr. no.

Particulars Details

A Water i Source of Water Supply The entire water



(GIDC, Bore well, Surface water etc...) requirement will be met through Sachin GIDC

Status of permission from the concern authority. Necessary permission shall be taken from concerned authority for the increased load of wastewater to be sent into CETP.

Ii Water consumption (KL/day)

-

Existing KL/day

Proposed (Additional) KL/day

Total after Expansion KL/day

Remarks

(A) Domestic 6.5 10 16.5 -

(B) Gardening 2 0 2 -

(C) Industrial -

Process 92 279 371 -

Washing 1.5 10 11.5 -

Boiler 41 0 41 -

Cooling 11 50 61 -

Others(Scrubber) 7 15 22 -

Total (A+B+C) 161 364 525 -

-

Iii

Waste water generation (KL/day)

-

Category Existing KL/Day

Proposed (Additional) KL/day

Total after Expansion KL/day

Remarks

(A) Domestic 6.5 10 16.5 -

(B) Industrial -

Process 68 153 (Low

Concentrated Stream)

345 -

124 (High

Concentrated Stream)

-

91 (Spent Acid to FS

Plant)

-

-

Washing 1.4 9.6 11 -

Boiler 37 0 37 -

Cooling 1.8 8 9.8 -

Others 1.5 5 6.5 -

Total Industrial waste water

116.2 309.6 425.8 -

-

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

Waste water stream will be segregated into different stream. Dilute, Low TDS stream (@ 42.5 KL/Day) shall be sent to



CETP of Globe Enviro Care Ltd, GIDC, Sachin. Low Acidity, High TDS stream (@125 KL/Day) is sent to Common facility of MEPPL for further treatment. Balance Neutral and High TDS stream of 242 KL/Day shall be treated in captive ZLD plant. Captive ZLD plant will consist of product specific MEE/MVR, Spray Dryer, Biological Treatment Unit and RO plant to achieve ZLD.

v Mode of Disposal & Final meeting point

Domestic: To STP

Industrial: 1) 42.5 KL/Day to CETP of Globe Enviro Care Limited 2) 125 KL/Day to Common MEE/MVR facility of MEPPL, GIDC, Sachin, Surat 3) 242 KL/Day Captive ZLD Plant consisting of MEE/MVR, Spray Dryer, SBT Plant and RO Plant

vi Reuse/Recycle details (KL/day) 200 KL/Day treated water reused in to the plant.

vii

B Air (Existing and Proposed) i Flue gas emission details

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

-

SR.

no.

Source of

emission

With

Capacity e.g.

Boiler (8

TPH)

Stack

Height

(meter)

Name of

the fuel

Quantit

y of

Fuel

MT/hr &

MT/Day

Type of

emission

s i.e. Air

Pollutant

s

APC

M

NAAQS

(National

Ambient

Air Quality

Standards

)

Existing

1.

Thermic Fluid Heater

Height :

30

Natural Gas -

1000 m3/Day

PM SO2 NOx

- PM-150

mg/NM3



No. 1 Capacity : 800 U

Meters

Dia. 800

mm

SO2- 100

ppm

NOx-50

ppm Thermic Fluid Heater No. 2 Capacity : 800 U

Natural Gas -

1000 m3/Day

2.

Baby Boiler Height :

12.5

Meters

Dia.:

200 mm Natural Gas

500 m3/Day

-

3.

Thermopack

Height :

12.5

Meters

Dia.:

150 mm

-

4.

10 TPD Syngas generator attached with Steam Boiler

Capacity : 2 MT/Hr

Height - 30 Meter Diamete

r - 750

mm

Non Hazardous

Waste (like

Paper Waste,

Chindi Waste,

Wood, Wood

Brickets, Wood

Pillets,

Agrowaste,

Bagasse, Coke,

RDF etc.) @

10 MT/Day (i. e.

Syngas @ 21,600

SCM/Day)

-

5.

D. G. Set Capacity - 175 KVA

Height :

11

Meters

Natural Gas

200 m3/Day -



6.

D. G. Set - Stand By Capacity : 125 KVA

Height :

11

Meters

LDO

40 Liters/Hr -

7.

Spray Dryer (1 KL/Hr)

Height - 30 Meter Diamete

r - 400

mm

Syn gas from Syn

Gas generator

-

PROPOSED ADDITIONAL

8.

Thermic

Fluid

Heater No.

3

Capacity :

800 U

Height :

20

Meters

Dia. 800

mm

Natural

Gas -

1000

m3/Day

PM SO2 NOx

-

PM-150

mg/NM3

SO2- 100

ppm

NOx-50

ppm

9.

Thermic

Fluid

Heater No.

4

Capacity :

800 U

Height :

20

Meters

Dia. 800

mm

Natural

Gas -

1000

m3/Day -

10.

Thermic

Fluid

Heater No.

5

Capacity : 1600 U

Height :

30

Meters

Dia.:

1000

mm

Coal

5000

Kg/Day

-



11.

Spray

Dryer (1.5

KL/hr)

Height -

30

Meters

Diamete

r - 500

mm

RDF 450

Kg/hr

OR

Bio-

Briquette

s 375

kg/Hr

OR

Coal 300

Kg/hr

-

12.

D. G. Set -

Stand By

Capacity :

2 x 375

KVA

Height :

11

Meters

LDO

100

Liters/Hr -

-

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

-

Sr.

no.

Source of

emission

Type of

emission

Stack/Vent

Height

(meter)

APCM

NAAQS

(National

Ambient Air

Quality

Standards)

EXISTING :-

1

Sulfonator SO3 Height - 15

Meters

Diameter -

200 mm

SO3 40 Mg/ NM3

Condensation

with ammonia NH3 NH3

175 Mg/ NM3

Storage tanks SO3, SO2,

HCl

SO3, SO2,

HCl

20 Mg/ NM3

Reduction H2s H2s 45 Mg/ NM3

2

Chlorination

with SOCl2 SO2

Height - 15

Meters

Diameter -

150 mm

SO2 40 Mg/ NM3

Chlorination

with SOCl2 HCl HCl

20 Mg/ NM3



Chlorination

with Cl2 Cl2 Cl2

9 Mg/ NM3

3 Pulverizer SPM

Height - 12

Meters

Diameter -

150 mm

PM

150 Mg/ NM3

4 Rotary Vacuum

Dryer PM

Height - 11

Meters

Diameter -

150 mm

PM

150 Mg/ NM3

5 Isolation Vessel SO2, NH3

Height :

12.5 Meters

Dia.: 100

mm

SO2, NH3

40 Mg/ NM3

173 Mg/ NM3

6

Fluid Bed Dryer

– 2 Nos

PM

Height - 9

Meters

Diameter -

100 mm

PM

150 Mg/ NM3

Spin Flash

Dryer – 2 Nos

PROPOSED ADDITIONAL

7

Sulfonator SO3 Height - 15

Meters

Diameter -

200 mm

SO2 40 Mg/ NM3

Condensation

with ammonia NH3 NH3

175 Mg/ NM3

Storage tanks SO3, SO2,

HCl

SO3, SO2,

HCl

20 Mg/ NM3

Reduction H2s H2s 45 Mg/ NM3

8 Isolation Vessel SO2, NH3

Height :

12.5

Meters

Dia.: 100

SO2

NH3

40 Mg/ NM3

173 Mg/ NM3



mm

9 Fluid Bed Dryer

– 2 Nos PM

Height - 9

Meters

Diameter -

100 mm

PM 150 Mg/ NM3

10 Fluid Bed Dryer

– 2 Nos PM

Height - 9

Meters

Diameter -

100 mm

PM 150 Mg/ NM3

11 Coal based

TFH PM

Height- 20

Mtrs

Diameter-

250 mm

PM 150 Mg/ NM3

-

v Fugitive emission details with its mitigation measures. (Existing and Proposed)

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

i

Sr. no.

Type/Name of Hazardous waste

Source of generation

Category and Schedule as per HW Rules.

Quantity (MT/Annum)

Disposal Method

Existing Additional

1 Iron oxide

waste

From

Process

26.1 632.16 MT/Year

3315 MT/Year

Sent to

cement

industries /

to TSDF

site for

Secured

Land filling.

2 ETP Sludge From ETP 34.3 359.16

MT/Year

630 MT/Year

Sent to

TSDF site

for Secured

land filling /

to cement

industry for



co-

processing

3 Evaporated

salt

From

MEE

26.1 2243.4

MT/Year

5664 MT/Year

Sent to

TSDF site

for Secured

Land filling

4 Used oil Used as a

lubricant

5.1 10 0.10

MT/Year

- Sent to

GPCB

approved

recycler / to

TSDF site

for suitable

treatment.

5 Spent Carbon From

process

35.3 12

MT/Year

150 MT/Year

Sent to

TSDF site

for

incineration

6 Discarded

Containers /

Bags

From raw

material

packaging

33.3 5400

Nos/Year

10800

Nos/Year

Sent back

to supplier /

to GPCB

approved

recycler / to

TSDF site

for suitable

treatment

7 Spent

Solvent**

From

process

20.2 12

MT/Year

- Reused in

the next

Batch / Sent

to approved

spent

solvent

recycler

8 Distillation

Residue**

From

process

20.3 2.4

MT/Year

108 MT/Year

Sent to

TSDF site

for

incineration.



9 Sodium

Hydrosulfide

From

process

D 3 5.4

MT/Year

- Reused

back into

process /

sold as a by

product to

authorized

end user.

10 Hydrochloride

Acid

From

process

D2 827.99

MT/Month

i. e.

9935.88

MT/Year

2922 MT/Year

Reused

back into

process /

sold as a by

product to

authorized

end user.

11 Sodium Bi

Sulfite

Solution

From

process

D3 3050.88

MT/Year

549 MT/Year

Used as a

raw

material

(after

recovered

from spray

evaporator)

12 Sodium

Hypochlorite

From

process

C 7 308.4

MT/Year

- Reused

back into

process /

sold as a by

product to

authorized

end user.

13 Ammonium

Sulfate

From

process

C1 2070.12

MT/Year

- Reused

back into

process /

sold as a by

product to

authorized

end user.

14 OR



15 Sodium

Sulfate

Crystals

From

process

D3 2226.96

MT/Year

1380 MT/Year

Reused

back into

process /

sold as a by

product to

authorized

end user.

16 OR

17 Ferrous

Sulfate

From

process

28 4359.84

MT/Year

26100 MT/Year

Sold as by

products.

18 Spent Acid

(H2SO4)

From

process

D2 3170.628

MT/Year

27307.5 MT/Year

Reused

back into

process /

sent to

ferrous

Sulfate

Plant.

19 Ammonium

Liquor

From

process

C1 331.716

MT/Year

652.50 MT/Year

Reused

back into

process

20 Ammonium

Sulphite

From

process

C1 252

MT/Year

5233.50 MT/Year

Reused

back into

process

Quantity of discarded containers must be in MT/Annum.

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

Dilute, Low TDS stream shall be sent to CETP of Globe Enviro Care Ltd, GIDC, Sachin. Low Acidity, High TDS stream is sent to Common facility of MEPPL for further treatment.

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

Not Applicable

D

i Spent Solvent management (If any)

Spent solvent shall be Collect / Store / Transport / reuse in to Process / send to GPCB approved recycler.

ii VOC emission sources and its mitigation measures

Not Applicable



9. Details of Environmental Consultants:

Sr. no.

Particulars Details

i Name of the Consultant Enpro Enviro Tech and Engineers Pvt. Ltd. ii Validity of Certificate of accreditation

issued by the NABET, QCI Valid up to Jan 10, 2019

iii Accreditation for the categories 1. Metallurgical industries (ferrous & nonferrous) - Cat. A 2. Synthetic organic chemicals industry (dye & dye intermediates; bulk drugs and intermediates excluding drug formulations; synthetic rubber; basic organic chemicals, other synthetic organic chemicals and chemical intermediates)- Cat. A 3. Common hazardous waste treatment, storage and disposal facilities (TSDFs) - Cat. A 4. Common Effluent Treatment Plant (CETPs) - Cat. A 5. Common Municipal Solid Waste Management Facility (CMSWMF) - Cat. B

iv Any other details Contact: 9825436776

Name & designation of the Applicant: Vatsal Naik

Stamp & Signature of the Applicant: __________ Date: 11-10-2017

General Instructions

Format shall be in WORD Format (Page size-A4, Font type- Arial, Font size- 11)

Provide authenticated (with stamp & Signature) hard copy during presentation.

Kindly mail to : [email protected] and copy to all members.

Above data should be as per application Form-1 & PFR.

Incorporate relevant details in respective column of the above format. Do not attach

as Annexure in Format.

mailto:[email protected]

for tor expansion case. 1. basic information of the...

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