pre - feasibility report for delta finochem pvt....
TRANSCRIPT
PPrree -- FFeeaassiibbiilliittyy RReeppoorrtt
FFoorrDelta Finochem Pvt. Ltd.
GGuutt nnoo --335500,, vviillllaaggee --WWaaddiivvaarrhhee,, IIggaattppuurrii ,, NNaasshhiikk--442222440033MMaahhaarraasshhttrraa..
EIA Consultant
M/s. SADEKAR ENVIRO ENGINEERS PVT. LTD.
QCI – NABET accredited EIA consultancy for schedule 5(f) Cat.-‘A’Certificate No – NABET/EIA/1518/SA 021
NABL Accredited Laboratory, Valid up to 29.06.2018Lab. Recognized by MoEF& CC, GOI, Valid up to 2.01.2019
Certified by ISO 9001:2008 & BS OHSAS 18001:2007
310, Dempo Towers, EDC Patto, Panaji, Goa state, India. PIN: 403001Email :[email protected] / [email protected]
Web site:-www.sadekarenviro.com Telephone :0832-2437048/2437164
June 2017
Delta Finochem Pvt. Ltd. June 2017
Sadekar Enviro Engineers Pvt. Ltd. Page 2
Table of Content
Sr. Title Page
1 Executive summary 3
2 Introduction of the project 5
3 Description of Project 7
4 Site Analysis 26
5 Planning 29
6 Proposed infrastructure 30
7 Rehabilitation and resettlement 31
8 Project schedule and cost estimation 31
9 Analysis of proposal 32
Delta Finochem Pvt. Ltd. June 2017
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1. Executive summary
Salient Features of Project
Name & Address of
Company
Delta Finochem Pvt Ltd
Gut no -350, village -wadivarhe, Igatpuri ,Nashik-422403
Maharashtra
Schedule of project as
per EIA Notification,
2006
5(f)
Category of Project 'A'
Area Statement
Existing, sq. m. Proposed sq. m. Total sq. m.
Total Plot Area 80600 0 80600
Built up area 9500 15000 24500
Green Belt Area 5273.18 10265.55 15338.73
Parking Area 1500 6560 8060
Production details
Existing, MT/A Proposed, MT/A Total, MT/A
Products
API 240 1839.8 2079.8
Intermediates 1982 9557.5 11539.5
Total 2222 11397.3 13619.3
Byproducts 0 1380 1380
Utility requirement
Existing Proposed Total
Water 50 CMD 113 CMD 163 CMD
Electrical power Connected load: 650 kw
Power demand: 500 kva
Connected load: 350 kw
Power demand: 300 kva
Connected load: 1000 kw
Power demand: 800 kva
Boiler 1.1 TPH 2.5 TPH 2.5 TPH
1.1 TPH (standby)
Thermic fluid
heater
-- 1 lakh kcal/hr 1 lakh kcal/hr
D.G. set 550 kva 550 kva 2*550 kva
Fuel Requirement
Fuel oil (FO) 19 MT/month 21 MT/month 40 MT/month
Delta Finochem Pvt. Ltd. June 2017
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High speed diesel
(HSD)
60 L/hr 60 L/hr 120 L/hr
Stack height
Boiler 30 m 30 m 2 boiler stacks of 30 m
height
Thermopack -- 10 m 1* 10 m
scrubber 1*10 m above ground
1*10 m above ground
1*10 m above ground
1*10 m above ground
1*10 m above ground
5 scrubber stacks 10 m
above ground.
D.G. set 10 m above ground 10 m above ground 2 stacks of 10 m high
above ground.
Waste generation
Sewage , CMD 4.0 6.0 10.0
Process Effluent
, CMD
11.3 36.2 47.5
ETP capacity,
CMD
15 45 60
Solid hazardous
waste
HW
Category
Existing Proposed Total Disposal
Distillationresidue
20.31 MT/month 10
MT/month11
MT/monthCHWTSDF
Spent solvents 20.2 10 kL/month 50kL/month
60kL/month
Recycle, reuse/saleto authorized party,CHWTSDF
Discardedcontainers
33.1300 nos/month 900
nos/month1200
nos/monthSale afterdecontamination
ETP sludge 35.3 0.58 MT/A 29.42 MT/A 30 MT/A CHWTSDFNon hazardouswaste
Existing Proposed Total Disposal
Office waste 5 kg/day 3 kg/day 8 kg/day Disposed through
local authority
Man power 180 100 280 Employees
working in 3
shifts
EMP budget Rs. 270 lakh.
Project cost Rs. 2005.48 lakh
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2. Introduction of the project
2.1 Identification of Project Proponent:
Delta Finochem Pvt. Ltd. manufactures Active Pharma Ingredients, Bulk Drug Intermediates and
Organic Specialties. Our products are exported to major markets like USA , Europe , Japan , South
East Asia , Middle East and North Africa. Out of 180 employees, more than 65 % workforce is
chemists and engineers. The company has a very good support from some of our customers and
hence very opportunities open up for the future growth potential.
Our strategy has been to focus on Import Substitution products within the domain our of our core
competencies. Also we have been able to successfully build relationships with major customers in
Europe and USA , with the result ,new opportunities are opening up.
Going forward , we want to position ourselves as a company of choice for our customers and focus
on Innovation and Efficient Green Processes.
2.2 Nature of project:
M/s. Delta Finochem Pvt. Ltd. have valid consent to operate no. Format 1.0/BO/AS(T)/ NK-18813-
15 & NK-19238-15/R-O-A/ GEN- 05810 dated 04/05/2016 for running a API and API
intermediates manufacturing plant. The company is going for expansion of manufacturing capacity
by increasing existing manufacturing capacity and introducing new API and intermediates
chemicals.
The proposed production capacity expansion project of APIs , Intermediates and Specialties will be
established at the existing production facility. The Existing production capacity is 2222 MT/A
which is to be expanded to 13619.3 MT/A. The expansion will be done by building new Production
blocks and additional equipment in the production unit. Total cost of expansion will be 20.05 crore
rupees.
2.3 Need for the project and its importance to the country and or region:
India's Chemical industry is the third largest in the world in terms of volume. Its rank is 14 in terms
of value. India is also one of the top five active Chemical ingredients producers (with a share of
about 6.5%). These products will serve to cut the supply of imports from foreign countries thus
saving currency and at the same time will earn valuable foreign currency by export of the products.
The company is manufacturing APIs ,Intermediates and Organic Specialties. The market for APIs
is growing and there is also a good demand from export markets. Some APIs will be import
substitute and hence will save foreign exchange for the country. About intermediates and Organic
Specialties we see a strong demand from a buoyant Pharma Industry. This project will help the
MAKE IN INDIA concept in our own small way.
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2.4 Demand supply gap
Competition in the Indian Chemical market swelled in recent years, with increasing generic
compounds introduction in the domestic market. The price of the products has reduced substantially
which led to less supply of high profit margin products in the market. A demand- supply gas is
created due to less supply of products. To capture this newly created gap between demand and
supply in the domestic market company wishes to introduce low margin products.
2.5 Import Vs. Indigenous production
The proposed expansion products including production of API and chemical intermediate have
huge demand in the domestic as well as export market. Production of these chemicals domestically
reduces the need to import products along with significant scope for export in these products.
2.6 Export & economic feasibility
The company has great demand from existing as well as new clients for expansion products in
domestic market. Some of the company’s APIs will be exported to Europe, Japan, South-East Asia
and middle East countries which will generate foreign exchange for the country.
2.7 Domestic/ export markets
The finished goods will be sold in domestic market primarily and it would be exported to the
Regulated International Market as per demand.
2.8 Employment generation
Presently the company employs about 180 people at its existing unit in three shifts the company
will employ 100 skilled and unskilled personnel for its expansion facility. It is expected that
proposed expansion will generate employment for semi-skilled and unskilled people.
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3. Description of Project
3.1 Project type:
The project is Production Capacity Expansion of existing products from 2222 MT/A to 13619.3
MT/A and including capacity expansion of existing products as well as introduction of new
products.
3.2 Location
The Company is located at Gat No.350/1, 350/2, 350/3, Wadiwarhe , Tal. Igatpuri , Dist. Nasik
422403. Company has valid consent to operate from Maharashtra Pollution Control Board for
manufacture of APIs, Intermediates and Organic Specialties. The location is shown in the Google
earth image below.
Figure 1: Location of Delta Finochem Pvt. Ltd. on Google Earth
Nearby Industries
Sr. Direction Industry
1 North Agricultural area
2 South Agricultural area
Delta Finochem Pvt. Ltd. June 2017
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3 East Renfro India Pvt. Ltd.
4 West Agricultural area
The unit is well connected by Mumbai- Agra highway (NH-3). The national highway is
approximately 0.5 km away and can be reached by state road network. The nearest railway
station is Nasik road which is approximately 24 km away from site.
The plot layout of Delta Finochem Pvt. Ltd. is given in figure 3. Total plot area is 80600 sq. m.
the location of plant building, utility building, ware house, internal roads, parking area is shown
in the layout.
Delta Finochem Pvt. Ltd. June 2017
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Figure 3: Plot layout of Delta Finochem Pvt. Ltd.
Area statement of Delta Finochem Pvt. Ltd. is explained in following table.
Sr. Particulars Existing, m2 Proposed ,m2 Total Area ,m2
1 Total plot area 80600 0 80600
2 Built up area 9500 15000 24500
3 Green belt area 5273.18 10265.55 15338.73
4 Parking area 1500 6560 8060
3.3 Details of alternate sites considered:
The proponent has adequate land for proposed expansion of manufacturing activity. The site is
well connected by national highway therefore the resources like raw materials, fuel can be
transported easily to the manufacturing facility. Additional water required for expansion will
be met through the Mukane dam situated 2 km away from project site.
Considering all above reasons the alternative site is not considered for proposed expansion of
existing unit.
3.4 Size of operation (Products and Byproducts)
The production capacity with byproducts is given in following table.
Sr. ProductExistingcapacity
Proposedcapacity
Totalcapacity
MT/A MT/A MT/A
1 Tetra butyl ammonium bromide 432 1200 16322 Tetra butyl ammonium hydrogen sulphate 120 0 1203 Tetra propyl ammonium bromide 24 0 244 Tetra ethyl ammonium bromide 24 0 245 Benzyl tributyl ammonium chloride 12 0 126 Tramadol HCl BP 120 -110 10
7 Fenofibrate BP 120 0 1208 Methyl alpha bromo 2-chlorophenyl acetate 300 -150 150
9ALPHA BROMO 2-CHLOROPHENYL aceticacid
300 -150 150
10 DIBENZO (b,f)[1,4]thiazepine-11 (10H)one 40 80 12011 Ethyl triphenyl phosphonium bromide 300 100 40012 N-hexyl bromide 400 2000 2400
13 1 (2H) pthalazinone 30 0 30
A TOTAL 2222 2970 5192API
14 Acebrofylline 0 30 30
15 Ambroxol Hydrochloride 0 36 36
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16 Amisulpride 0 24 24
17 Apremilast 0 1 1
18 Atazanavir 0 2.4 2.4
19 Avanafile 0 1.2 1.2
20 Azelaic Acid 0 36 36
21 Bamifyline 0 12 12
22 Benfothiamine 0 120 120
23 Bezafibrate 0 12 12
24 Brivaracetam 0 3.6 3.6
25 Carbimazole 0 4.8 4.8
26 Choline Fenofibrate 0 24 24
27 Cycloserine 0 6 6
28 Dapoxetine 0 6 6
29 Deferamine 0 6 6
30 Deferesirox 0 12 12
31 Deferiprone 0 12 12
32 Diphenhydramine Hydrochloride 0 120 120
33 Doxofylline 0 120 120
34 Ecabet Sodium 0 48 48
35 Erdosteine 0 30 30
36 Ethionamide 0 120 120
37 Fenofibric Acid 0 36 36
38 Flavoxate Hydrochloride 0 30 30
39 Folic Acid 0 240 240
40 Hydralazine Hydrochloride 0 36 36
41 Levocloperastine 0 6 6
42 Levosulpride 0 48 48
43 Lomitapide Mesylate 0 3 3
44 Methimazole 0 6 6
45 Nitazoxanide 0 24 24
46 Oxomemazine Base 0 2.4 2.4
47 Oxomemazine Hydrochloride 0 2.4 2.4
48 Pentoxyverine Citrate 0 36 36
49 Piperaquiline TP 0 36 36
50 Piperaquine Tetraphosphate 0 48 48
51 Praziquantel 0 180 180
52 Proglumetacin maleate 0 36 36
53 Propyl thiouracil 0 24 24
54 Prothionamide 0 24 24
55 Pyrihiazine Theocloate 0 6 6
56 Pyronaridine Tetraphosphate 0 36 36
57 Ritonavir 0 3 3
58 Tapentadol 0 6 6
59 Taurolidine 0 6 6
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60 Terizidone 0 6 6
61 Thiamine Hydrochloride 0 120 120
62 Thiooctic Acid 0 60 60
63 Tolmetin 0 24 24
64 Tolperisone 0 6 6
65 Tranexamic acid 0 60 60
66 Vigabatrin 0 12 12
B TOTAL 0 1949.8 1949.8Intermediates Compounds
67 1,4-Dibromobutane 0 480 480
68 2-cyanobenzyl bromide 0 20 20
69 4-cyanobenzyl bromide 0 20 20
70 Allyl bromide 0 300 300
71 Cetyl bromide 0 60 60
72 Cyclobutyl Methyl Bromide 0 1.92 1.92
73 Cyclopropyl Bromide 0 1.92 1.92
74 Cyclopropylmethyl Bromide 0 3 3
75 Decyl bromide 0 600 600
76 Dibromobutenediol 0 9.96 9.96
77 Dimethyl acetylenedicarboxylate 0 10 10
78 Ethyl bromide 0 480 480
79 Isoamyl Bromide 0 60 60
80 Lauryl bromide 0 20 20
81 N Butyl bromide 0 2000 2000
82 N Octyl bromide 0 20 20
83 N Propyl bromide 0 200 200
84 Pentyl bromide 0 6 6
85 Tetrahydrofuryl bromide 0 4.92 4.92
86 Triethylphosphonoacetate 0 240 240
87 Trimethylphosphonoacetate 0 19.2 19.2
88 2-hydroxyethyl piperazinyl Dibenzothiazepine 0 24 24
89 2-aminothiophenol 0 30 30
90 8-chloro dihydrobenzodiazepine 0 19.2 19.2
91 Phenetole 0 199.2 199.2
92 Thioanisole 0 199.2 199.2
93 Benzoyl Praziquantel 0 69.6 69.6
94 Praziquinamine 0 39.6 39.6
95 Benzhydryl Sulfinyl Acetic Acid 0 30 30
96 2-aminodiphenyl sulfide 0 39.6 39.6
97 4-fluorophenyl-2-methylpropionyl chloride 0 49.2 49.2
98 2-chloroethyl trityl ether 0 10 10
99 Bromohexyl 4-phenylbutyl ether 0 1 1
100 aminoacetaldehyde dimethylacetal 0 9.96 9.96
Quaternary Compounds
Delta Finochem Pvt. Ltd. June 2017
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101 Tetrabutylammonium Iodide
0 1200 1200
102 Benzyltrimethylammonium Chloride103 Tetraethylammonium Bromide104 Tetrabutylammonium Hexafluorophosphate105 Methyltributylammonium Chloride106 Methyltrooctylammonium chloride107 Tetraoctylammonium Bromide108 Tetrabutylammnoium Fluoride109 Tetrabutylammonium Acetate110 Ethyltriphenylphosphonium Iodide111 Ethyltriphenylphosphonium Acetate112 Methyltriphenylphosphonium Bromide113 Methyltriphenylphosphonium Iodide
114Methoxymethyl Triphenyl PhosphoniumChloride
115 Tertabutylphosphonium bromide116 Tetraphenylphosphonium Bromide117 Tetrabutylphosphonium hydrogendifluoride118 Benzyltriphenylphosphonium Chloride119 Benzyltriphenyl Phosphonium Bromide120 Butyltriphenyl Phosphonium Chloride121 Butyltriphenylphosphonium Bromide122 Benzalkonium Chloride123 Tetramethylammonium Hydroxide124 Benzyltrimethyl Ammonium Hydroxide125 Tetraethylammonium Hydroxide126 Tetrabutylammonium HydroxideC TOTAL 0.0 6477.5 6477.5
Total Product Capacity (A+B+C) 2222.0 11397.3 13619.3
List of byproducts:
Sr. BYPRODUCTEXISTINGCAPACITY
PROPOSEDCAPACITY
TOTALCAPACITY
MT/A MT/A MT/A1 Aqueous ammonia spent 0 180 1802 Potassium Carbonate solution 0 240 2403 Spent soda ash 0 120 1204 Ammonium sulfate solution 0 240 2405 Aqueous sulfuric acid 0 600 6006 spent phosphoric acid 0 480 480
TOTAL BYPRODUCTS 0 1380 1380
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3.5 Project description with process detail.
The process details and material balance for praziquantel is given in following table..
NH
NH
O
O
OCH3
CH3
2-[(2,2-dimethoxyethyl)amino]-N-(2-phenylethyl)acetamide
NH2+
O
Cl
Cl
NH
Cl
O
2-phenylethan-1-amine chloroacetyl chloride
2-chloro-N-(2-phenylethyl)acetamide
Step-1:Synthesis of NCP1
NH
Cl
O
2-chloro-N-(2-phenylethyl)acetamide
+ NH4OH NH
NH2
O
2-amino-N-(2-phenylethyl)acetamide
NH
NH2
O
2-amino-N-(2-phenylethyl)acetamide
+O
OCH3
CH3Br
2-bromo-1,1-dimethoxyethane
Step-2:Synthesis of NCP2
Step-3:Synthesis of PRA
NH
NH
O
O
OCH3
CH3
2-[(2,2-dimethoxyethyl)amino]-N-(2-phenylethyl)acetamide
+ Dry HCl gas
2-[(2,2-dimethoxyethyl)amino]-N-(2-phenylethyl)acetamide HydroChloride
NH
NH
O
O
OCH3
CH3
ClH
Synthesis of PRA HCl
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Process Description:
Praziquantel
Beta Phenyl Ethyl Amine is reacted with Chloroacetyl Chloride in the presence of
Caustic Soda Solution. The mixture is filtered and the powder is crystallized in
Methylene Dichloride to obtain Stage 1.
Stage 1 is reacted with Aqueous Ammonia and Caustic Soda and the reaction mixture is
filtered. The filtrate is extracted with Methylene Dichloride to obtain Stage 2.
Stage 2 is reacted with Potassium Carbonate and Bromoacetaldehyde Dimethyl Acetal
in Dimethyl Formamide. The reaction is quenched on water and aqueous layer is
extracted with Methylene Dichloride to obtain stage 3.
Stage 3 is reacted with Sulphuric Acid and then reaction mixture is quenched
successively in Water and then Caustic Soda solution. The Aqueous layer is then
extracted with Methylene Dichloride to obtain Stage 4.
+
Step-4:Synthesis of PRZ
ClH
NH
NH
O
O
OCH3
CH3
2-[(2,2-dimethoxyethyl)amino]-N-(2-phenylethyl)acetamide HydroChloride
H2SO4
N
N
O
O
N
NH
O
1,2,3,6,7,11b-hexahydro-4H-pyrazino [2,1-a]isoquinolin-4-one
2-(cyclohexanecarbonyl)-1,2,3,6,7,11b-hexahydro -4H-pyrazino[2,1-a]isoquinolin-4-one
N
NH
O
1,2,3,6,7,11b-hexahydro-4H-pyrazino [2,1-a]isoquinolin-4-one
+ Cl
O
cyclohexanecarbonyl chloride
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Stage 4 is reacted with Cyclohexane Carbonyl Chloride and Caustic Soda solution . The
reaction is monitored for completion and then extracted with Methylene Dichloride to
obtain crude Praziquantel.
Crude Praziuqnatel is crystallsied in a mixture of Acetone and Methyl Tert-Butyl Ether to
obtain Praziquantel.
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Process flow with material balance:
BPE amine (250kgs)CAC( 280kgs)Water( 1200 kgs) Eva. Loss (11 kgs)Caustic soda (102kgs)MDC( 2000 kgs)
layer Separation
Aqueous solution (1585 kgs )Distillation residue (2kgs)Eva. Loss (71kgs)Dist MDC(1800kgs)
FiltrationStage I (354 kgs)Eva. Loss (20kgs)
Stage I(354 kgs)Liq.Ammonia(2000kgs)Caustic soda(285kgs)Water (425kgs)MDC (1000 kgs)
Filtration
Spent soda (300 kg)
Layer Separation
Spent Ammonia ( 2574 kg)
Distillation
Dist MDC(978kgs)Distillation Residue (2kgs)
Stage II (190kgs)
S.S. REACTOR
S.S.Reactor
wet and purestage I
S.S.Reactor
S.S.Reactor
S.S.Reactor
S.S.Reactor
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Stage II (190kgs) Loss to scrubber ( 10kgs)Potassium carbonate(220kgs)Bromoacetdal dimethyl acetal (210kgs)Water(700kgs)MDC (800kgs)
Layer Separation
Aqueous layer(1100kgs)
DistillationDist.Residue(2kgs)Loss to scrubber(18kgs)MDC distillate (750kgs)
Stage III (240kgs)
Stage III (240kgs)Sulphuric acid (4500kgs) Loss to scrubber ( 8kgs)
Soda (400kgs)Water(700kgs)MDC(2100kgs)
Layer Separation
Aqueous layer(2690kgs)
Distillation
Dist.Residue(2kgs)MDC distillate (1900kgs)
Stage IV (160kgs)
S.S.Reactor
S.S.Reactor
S.S.Reactor
G. L. Reactor
MDC Layer
CrudePraziquental
S.S.Reactor
S.S.Reactor
waterQuenching
G.L.Reactor
Stage IV
G.L.Reactor
MDC Layer
CrudePraziquental
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3.6 Raw material details
All basic raw material details with its quantity are given below. The raw materials are available in
domestic market and they will be transported by road to the manufacturing unit. Imported raw
materials will be transported first by airways and then by road to the site.
Bags, carbuoys and drums will be stored in storage area and larger quantity raw materials like
solvents will be stored in tanks. The gases will be stored in the cylinders as per storage
specifications.
Sr.No
Raw Material consumption ( TPD ) Maximum
storagein MT
Sourceof
supply
Means oftransport
ationexisting
proposed
Total
1 Methanol 1.65 4.293 5.946 40 MT Local Road
2 1,3-Dibromopropane 0 0.029 0.029 5 MT Local Road
3 1,4-dibromobutane 0 0.012 0.012 5MT Local Road
4 1-methyl pyrrole 0 0.034 0.034 5MT Imported Air ways
5 2,4-dichlorobenzoic acid 0 0.071 0.071 5MT Local Road
6
2-chloroethyl piperidinehydrochloride 0 0.058 0.058 5MT Local
Road
Stage IV (160kgs)CHCC (180kgs) Loss to scrubber ( 30kgs)
Caustic Soda (50kgs)Water(200kgs)MDC(1200kgs)
Layer Separation
Aqueous layer(442kgs)
Distillation
Loss to scrubber ( 10kgs)MDC distillate (1100kgs)
Stage V
Loss to scrubber ( 50kgs)MTBE(1400kgs) MTBE distillate (1350kgs)
Praziquantel (208kgs)
G. L. Reactor
S.S.Reactor
S.S.Reactor
MDC Layer
CrudePraziquental
S.S.Reactor
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7 3-amino-6-methoxy pyridine 0 0.046 0.046 5MT Imported Air ways
8 3-ethoxy propionitrile 0 0.173 0.173 5MT Imported Sea ways
9
3-methylflavnone 8-carboxylicacid 0 0.069 0.069 5MT Local
Road
10 4,7-dichloro quinoline 0 0.069 0.069 5MT Local Road
11 4-aminophenol 0 0.037 0.037 5MT Local Road
12
4-chloo-4-hydroxybenzophenone 0 0.476 0.476 5MT Local
Road
13 4-Chlorobenzoyl Choride 0 0.042 0.042 5MT Imported Air ways
14 4-cyano Benzoic Acid 0 0.000 0.000 5MT Imported Air ways
15 4-hydrazinobenzoic acid 0 0.010 0.010 5MT Imported Air ways
16 ABC acid 0 1.408 1.408 5MT Local Road
17 Acephylline 0 0.146 0.146 5MT Local Road
18 acetamidine 0 0.090 0.090 5MT Local Road
19 Acetic acid 0 0.004 0.004 5MT Local Road
20 Acetic Anhydride 0 0.208 0.208 5MT Local Road
21 Acetone 0.39 0.209 0.601 5MT Local Road
22 Acetonitril 0.23 1.200 1.431 10MT Local Road
23 Allyl alcohol 0 0.818 0.818 5MT Local Road
24 alpha Naphthol 0 0.014 0.014 5MT Local Road
25 Aluminium chloride 0.09 0.048 0.137 5MT Local Road
26 Ambroxol Hydrochloride 0 0.255 0.255 5MT Local Road
27 Ammonium Chloride 0 0.104 0.104 5MT Local Road
28 Benzhydryl Bromide 0 0.380 0.380 5MT Local Road
29 Benzoyl Chloride 0 0.130 0.130 5MT Local Road
30 Benzyl Cyanide 0 0.029 0.029 5MT Local Road
31 Beta Chloro Propiophenone 0 0.018 0.018 5MT Local Road
32 Bromine 0.23 9.843 10.074 60MT Local Road
33 BPE amine 0 0.692 0.692 5MT Local Road
34
Bromoacetaldehyde EthyleneAcetal 0 0.355 0.355 5MT Local
Road
35 Bromoacetdal dimethyl acetal 0 0.888 0.888 5MT Local Road
36 N BuBr 0 3.462 3.462 5MT Local Road
37 Butanol 0.05 1.492 1.542 5MT Local Road
38 Carbon 0.038 0.680 0.718 5MT Local Road
39 C B Carbinol 0 0.097 0.097 5MT Imported Air ways
40 CAC 0 3.139 3.139 10MT Local Road
41 CHCC 0 0.498 0.498 5MT Local Road
42 Caustic Soda 0 0.300 0.300 5MT Local Road
43 Cetyl alcohol 0 0.337 0.337 5MT Local Road
44 Chloroacetyl Chloride 0 0.054 0.054 5MT Local Road
45 chloroform 0.29 0.403 0.696 5MT Local Road
46 Choline Chloride 0 0.028 0.028 5MT Local Road
47 Citric acid 0 0.013 0.013 5MT Local Road
48 Copper Oxide 0 0.075 0.075 5MT Local Road
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49 Decyl alcohol 0 1.538 1.538 5MT Local Road
50 Dimethyl Amine 0 0.004 0.004 5MT Local Road
51 Dimethylamino Ethanol 0 0.140 0.140 5MT Local Road
52 Dimethylamino ethoxy ethanol 0 0.012 0.012 5MT Local Road
53
DL Homocysteine ThiolactoneHCL 0 0.069 0.069 5MT Imported Air ways
54 DMF 0 0.606 0.606 5MT Local Road
55 ECF 0 0.040 0.040 5MT Local Road
56 Ethyl Bromide 0.25 0.147 0.397 5MT Local Road
57 Ethanol 0 0.701 0.701 5MT Local Road
58 Ethyl acetate 0.29 2.769 3.058 5MT Local Road
59 Ethyl chloroformate 0 0.051 0.051 5MT Local Road
60 Ethyl Cyano Acetate 0 0.738 0.738 5MT Imported Sea ways
61 Ethylene dibromide 0 0.040 0.040 5MT Imported Sea ways
62 Formaldehyde 0.13 0.031 0.158 5MT Local Road
63 Guanidine 0 0.369 0.369 5MT Imported Air ways
64 HBr 0 2.840 2.840 5MT Local Road
65 Hexanol 0 5.198 5.198 10MT Imported Sea ways
66 Hydrochloric acid 0 0.121 0.121 5MT Local Road
67 Hydrogen 0 0.213 0.213 5MT Local Road
68 Hydrogen Sulphide 0 0.042 0.042 5MT Local Road
69 Iodine 1.81 0.001 1.809 5MT Imported Sea ways
70 IPA 0.25 1.238 1.485 5MT Local Road
71 IPA HCL 0.25 0.369 0.616 5MT Local Road
72 Isoamyl alcohol 0 1.479 1.479 5MT Local Road
73 K2CO3 0 1.152 1.152 5MT Local Road
74 KOH 0 4.114 4.114 5MT Local Road
75 Lauryl alcohol 0 0.146 0.146 5MT Local Road
76 Liq.Ammonia 0 5.538 5.538 20MT Local Road
77 Magnesium 0.11 0.057 0.164 10MT Local Road
78 Maltol 0 0.018 0.018 10MT Imported Sea ways
79 MDC 0 3.380 3.380 10MT Local Road
80 MEG 0 0.169 0.169 10MT Local Air ways
81 Methane Sulfonyl Chloride 0 0.010 0.010 10MT Imported Sea ways
82
methyl 2-bromo-2-methylpropionate 0 0.019 0.019 10MT Imported Sea ways
83 MTBE 0 2.588 2.588 10MT Local Road
84 N methyl amine 0 0.015 0.015 10MT Local Road
85 Methyl isobutyl ketone 0.16 0.800 0.959 10MT Local Road
86 n Octanol 0 0.291 0.291 10MT Imported Air ways
87 N Pentanol 0 1.479 1.479 10MT Imported Air ways
88 NPA 0 1.343 1.343 10MT Local Road
89 NEP 0 1.281 1.281 10MT Local Road
90 Net acid 0.31 0.316 0.627 10MT Local Road
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91 N-ethylethanol 0 0.019 0.019 10MT Local Road
92 Nitric Acid 0.19 0.197 0.385 10MT Local Road
93 Nitrile 0 0.209 0.209 10MT Local Road
94 NPA 0 1.344 1.344 10MT Local Road
95 OCPA 0 1.479 1.479 10MT Imported Air ways
96 Octanol 0 0.291 0.291 10MT Local Road
97 Palladium 0 0.118 0.118 10MT Local Road
98 para Terephthaldehyde 0 0.118 0.118 10MT Imported Air ways
99 PCF 0 1.385 1.385 10MT Imported Air ways
100 Phosphoric Acid 0 1.357 1.357 10MT Local Road
101 Phosphorous Oxychloride 0 0.135 0.135 10MT Local Road
102 Phosphorous trichloride 0 0.087 0.087 10MT Local Road
103 Piperazine 0 0.032 0.032 10MT Local Road
104 Potassium Carbonate 0 1.152 1.152 10MT Local Road
105 pyruvaldehyde 0 0.153 0.153 10MT Local Road
106 Red phosphorus 0 0.013 0.013 10MT Local Road
107 Salicylamide 0 0.017 0.017 10MT Imported Air ways
108 Salicylic acid 0 0.017 0.017 10MT Imported Air ways
109 Soda ash 0 1.108 1.108 10MT Local Road
110 Sodium Borohydride 0 0.040 0.040 10MT Imported Air ways
111 Sodium Ethoxide 0 0.036 0.036 10MT Local Road
112 Sodium hydroxide 0.06 2.895 2.957 10MT Local Road
113 Sodium monochloroaectate 0 0.005 0.005 10MT Local Road
114 Sulphur 0 0.576 0.576 10MT Imported Air ways
115 Sulphuric Acid 0.16 1.709 1.870 10MT Local Road
116 Theophylline 0 0.307 0.307 10MT Local Road
117 THF 1.27 1.285 2.554 10MT Local Road
118 THFA 0 0.350 0.350 10MT Local Road
119 TNBA 0 4.662 4.662 10MT Local Road
120 Thiamine Hydrochloride 0 0.043 0.043 10MT Imported Air ways
121 Thioglycolic Acid 0 0.045 0.045 10MT Imported Sea ways
122 Thionyl chloride 0 0.017 0.017 10MT Local Road
123 Thiourea 0 0.038 0.038 10MT Local Road
124 Toluene 1.02 2.038 3.054 10MT Local Road
125 Tripropyl amine 0.03 1.200 1.228 10MT Local Road
126 Tripropyl bromide 0.02 2.000 2.025 10MT Local Road
127 Tripynyl phosphine 0.5 0.800 1.300 10MT Local Road
128 Triethyl amine 0 0.007 0.007 10MT Local Road
129 Triethyl orthoformate 0 0.261 0.261 10MT Imported Air ways
130 Tributyl amine 0.54 2.300 2.842 10MT Local Road
131 Tributyl bromide 0.40 2.400 2.796 10MT Local Road
132 tyramine 0 0.017 0.017 10MT Imported Air ways
Total 10.7 106.6 117.3
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3.7 Resource optimization ( recycle/ reuse):
The existing unit is zero liquid discharge unit consisting of ETP, MEE with ATFD and RO
system
Presently solvent recovery column is installed in the plant which recovers the solvent from
product streams these solvents are reused 3-4 times for that specific product. This reduces
the COD load of ETP and amount of fresh solvent needed for the batch is reduced.
Drip irrigation and water sprinkler system is installed in the existing unit to reduce fresh
water consumption for gardening.
3.8 Availability of water, energy fuel:
The water is presently supplied by a private water supplying vendor. Daily fresh water need for
existing domestic and process water requirement is 32.5 CMD. After proposed expansion 163
CMD water is needed.
After expansion 800 KVA power demand is envisaged. To fulfill the required power demand, a
connected power load 1 MW will be provided by MSEDCL.
Total 40 MT/month of FO will be required after expansion to run proposed 2.5 MT/hr steam
capacity boiler and 1 lakh Kcal/hr capacity thermic fluid heater.
After expansion, total 120 L/hr HSD will be required for running D.G. sets in power failure
situation.
3.9 Quantity of waste to be generated
Total 57.5 CMD process waste will be generated. It will be treated ETP consisting primary,
secondary and tertiary treatment facilities followed by RO and 13 CMD water will be recycled
to the plant. the reject will be treated in MEE and MEE condensate is treated in ETP.
10 CMD domestic sewage will be treated aeration tank of ETP.
Table : Existing Water budget
parameter CTO Input Losses Effluentdomestic process
domestic 10 4.5 0.5 4.0 --process 20 15.0 5.0 -- 10.0coolingtower 14
2.0 1.2 -- 0.8
boiler 9.0 0.5 -- 0.5 8 CMD water
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recyclegardening 2 2.0 2.0 -- --
total 46 32.5 9.2 4.0 11.3
Proposed water budget after expansion
parameter Input Losses Effluent Remarkdomestic process
domestic 12.0 2.0 10.0 --process 56.0 10.0 -- 46.0coolingtower
30.0 1.8 -- 0.9 27.3 CMD water recycle
boiler 25.0 0.3 -- 0.6 24.1 CMD water recyclegardening 40.0 40.0 -- --Total 163.0 54.1 10.0 47.5
Solid hazardous waste which will be generated from the manufacturing activity will be,
Sr.No Particulars Category Existing
Total afterexpansion
Method ofDisposal
1Distillation
residue20.3 1000 kg/ M
10MT/month
CHWTSDF/ saleto MPCB
authorized party
2 Spent solvents 20.210000
L/month50,000L/month
CHWTSDF /MPCB
authorizedrecycler
3Discardedcontainers
33.1300 nos./
month900
nos./monthsale to authorized
party
4 ETP sludge 35.3580
kg/annum30 MT/A CHWTSDF
Non hazardous waste generation will be given as,
Existing After expansion Method of Disposal
Office waste 5 kg/d 8 kg/d Through municipal
waste collection system
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The company environment management plan budgetary allocation for present stage and after
expansion is given in following table.
Sr.No.
Parameters Capital Cost(Rs.)
Recurring Costper annum (Rs.)
1 Air Pollution Control 40,00,000 8,00,0002 Water Pollution Control 2,00,00,000 22,00,0003 Noise Pollution Control 2,00,000 30,0004 Environment Monitoring
and Management0 10,00,000
5 Occupational Health 5,00,000 75,0006 Green Belt 15,00,000 2,00,0007 Solid Waste Management 3,00,000 2,00,0008 Water conservation 5,00,000 50,000
Total cost (Rs.) 2,70,00,000 45,55,000
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3.10 Schematic representation of feasibility drawing for EIA purpose
PRODUCTION ACTIVITY
RESOURCE CONSUMPTION(WATER)
POWER CONSUMPTION
WASTEGENERATION
FINISHED PRODUCTS
MARKET
ECONOMY
EMPLOYMENT
RAW MATERIAL
POLLUTIONABATEMENT
CLEANENVIRONMENT
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4. Site Analysis
4.1 Connectivity:
The project is located in Wadhiware village which is easily accessible from Mumbai- Agra
highway NH-3, further connecting to the project site by internal access roads.
Nearest Railway Station: Nahik road, approximately at a distance of 35 km.
Nearest Airport: Chatrapati Shivaji International Airport approximately at a distance of 200kmLocation and AccessThe area is centrally located and easily accessible through all modes of transport.
Road: The entire industrial area is well connected by internal roads.
Available Road Network: Mumbai – Agra highway (NH 3) at a distance of approximately
500 m from the project site.
4.2 Land Form, Land use and Land Ownership
The Project location is owned by the management of Delta Finochem Pvt. Ltd. The land use of the
proposed expansion site is industrial and it will be developed for industrial purposed.
4.3 Topography:
The co-ordinates of the project site are 19°50'57.69"N and 73°40'34.54"E. the toposheet is given
below to show the topography of surrounding area.
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M/s. Delta Finochem Pvt. Ltd.
Location: Plot no. 350, Wadiware, Igatpuri,Nashik district, Maharashtra State.
Co-ordinates: 19°50'57.69"N & 73°40'34.54"E
Toposheet no. 47E/9
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Environmentally sensitive features within 15 km radius of the plant
The environmentally sensitive features exist around 15 km radial distance from the plant is,
1. Mukane dam is 2 km away from the project site.
2. Darna dam is 8.26 km away
3. Upper Vaitarana dam is 10.6 km away from the existing project.
4. Scattered patches of Reserve Forest exist at an aerial distance of more than 5 km from the
project site.
4.4 Existing land use pattern
The expansion project is located in the industrial estate which has been developed for industrial
development. The existing land use pattern in the 10 km radial distance of the project site
comprises of Industrial, human habitations/settlements, small agricultural/ crop lands, quarrying
land use classes.
4.5 Existing infrastructure:
Presently the industry has all necessary facilities and ancillary facilities required for industrial
production constructed at the site. Additional buildings required for expansion activity will be
constructed as per architectural layout.
4.6 Soil classification:
The soils in the area are formed from the Deccan Trap which is predominating rock formation with
small out crops of Laterite. The soils are medium black and black soil which can be further grouped
as Forest, Varkas, Rice, Khar or Saline, Coastal Alluvium and Laterite as per the location and
topographical situation. At proposed expansion site soil analysis has been carried out by M/s. Civil
Tech Competent Agency for soil testing.
Climatic data from secondary sources
The climate in the area is characterized by hot summer and general dryness throughout the
year except the south west monsoon season.
Climate Classification: Project site features a semi arid climate. In rainy season the climate is very
humid.
Temperature: annual average max. Temperature is 37.2°C and min. temperature is 10.8 °C
Rainfall: The analysis of long term rainfall data indicates that normal annual rainfall over the
district ranges from 0 mm to 201 mm in the plains and it is above 400 mm in the hills. The average
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yearly rainfall around Nashik area is 180 mm.
4.7 Social infrastructure available:
Social infrastructure like schools, road, hospitals, is available near the project location.
5. Planning Brief
5.1 Planning concept:
The expansion work will be stated after receiving the Environmental Clearance. The Time
schedule and planning of expansion will be determined after discussion with architect and civil
contractors.
M/s. Delta Finochem Pvt. Ltd. has valid consent to operate for existing production of API and
API intermediates. The expansion will be done after grant of environmental clearance. It is
expected that total time required for expansion will be around 8 months.
The company is 500 m away from national highway therefore no additional road will be
constructed.
Presently water is supplied through private vendor for daily plant activities, for proposed
expansion the same practice will be followed
Electricity will be provided by MSEDCL. Necessary transformer will be installed.
The construction material is available locally and it will be transported through road network.
Presently fuel requirement is met through the local vendours, for proposed expansion project
similar practice will be followed.
5.2 Population projection:
It is assumed that due to proposed expansion project minor migration of skilled labour in the region
is expected after commissioning of the project.
5.3 Land use planning:
The proposed expansion of manufacturing unit will be done on the open plot owned by the
company for industrial use. No cultivated land or forest land will be utilized for the proposed
expansion unit, therefore the land use pattern will be remain unchanged.
5.4 Assessment of Infrastructure demand
The major physical infrastructure like road and rail connectivity, water supply is available in the
area . The electricity will be supplied by MSEDCL The industrial infrastructure will be constructed
after grant of EC. The need of social infrastructure is not presently envisaged.
5.5 Amenities:
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Basic amenities like internal road, electricity, water for industrial and domestic uses are presently
available at site. The drinking water will be provided by further purification of process water by
RO purification unit. In the plant personal hygiene facilities are provided to workers as per the rule.
6. Proposed infrastructure:
6.1 Industrial area
The proposed expansion of Delta Finochem Pvt. Ltd. will be carried out at existing
manufacturing site at Gat no 350, Wadiwarhe, Igatpuri , Nasik 422403. Total plot area is 80600
sq. m. Total built up area after expansion will be 24500 sq. m. for proposed expansion new
manufacturing plant and allied ancillary installations like utility building, warehouse, water
tank will be constructed in the plot premise.
.
6.2 Residential area
The unit is located close to Wadiwarhe and therefore there is no need of Residential
Infrastructure.
6.3 Green belt
Based on this survey and the CPCB guidelines native plant species have been proposed for the
green belt development plan. A thick green belt around the boundary of company is proposed
to be developed within the project site (33% of the open area after expansion). The general
considerations involved while proposing the green belt plan are:
Local/ Native fast growing trees & shrubs will be used for plantation
They should have large leaf area index
They should have higher Air Pollution Tolerance Indices
They should not have any noticeable effect on the plant yield due to gaseous pollutants
Total 15338.73 sq. m. area covering green belt will be provided in the plant. The proposed
expansion will need construction of new buildings; however, the existing green belt will remain
intact.
6.4 Social infrastructure:
The project is approximately 4 kms from Wadiware Village. All basic social infrastructure is
available in the area.
6.5 Connectivity
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The site can be accessed by national Highway NH-3. Excellent road network is available.
Igatpuri and Nasik road are major railway stations nearby. Chhatrapati Shivaji International
Airport is 166 km away and connected by national highways.
6.6 Sewerage system
The internal storm water drains are provided. The existing ETP plant of 30 CMD capacity is
provided. The plant is operated on Zero Liquid Discharge basis.
6.7 Industrial waste management
High TDS/ COD effluent will be treated by MEE followed by ATFD. The MEE condensate and
low COD effluent will be treated at existing ETP consisting of primary, secondary and tertiary
treatment. After expansion the ETP capacity will be increased to 60 CMD. The effluent will be
further treated by RO system and permeate will be recycled to plant. The Plant is operated on
Zero Liquid Discharge basis.
The Hazardous Solid Waste generated is disposed through CHWTSDF, Ranjangaon.
6.8 Solid waste management
The hazardous waste will be segregated as per category in schedule I of “Hazardous and Other
Wastes (Management and Trans-boundary Movement) Rules, 2016” and it will be stored in
demarcated area. The hazardous waste will be treated at CHWTSD facility or it will be sold to
MPCB authorized re-processor.
6.9 Power requirement/ supply/ source
A 1 MVA capacity transformer will be installed in the company for connected load of equal
amount. The connected load will be around 1 MW for proposed unit. The power demand will
be 800 KW. Electrical power will be supplied by MSEDCL.
Total 40 T/month FO will be required for running boiler and thermic fluid heater. Total 120
L/hr HSD will be used for running 2 D.G. sets of 550 KVA capacity in case of power failure.
Fuel will be arranged from local vendors.
7. Rehabilitation and resettlement:
The expansion activity will be done on open area of the plot owned by company therefore no
rehabilitation and resettlement will be envisaged.
8. Project schedule and cost estimation
1. The proposed schedule for approval and implementation.
Sr.No.
Description Time Cost in %
1. Obtaining all statutory permission withrespect to industry
7 Months 10%
2. Design and Engineering Plan 3 Months 10%
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3. Factory Set Up 8 Months 70%4. Testing and Commissioning 1 Months 5%5. Actual Starting 1 Months 5%
It is proposed that the project will be commissioned after 8 months from grant of EC. The cost
estimation is presented in CA certificate attached as annexure.
9. Analysis of proposal
Proposed production activity will provide employment to the local residents, resulting financial
and social benefits of the nearby people.
Indirect employment will be generated by the proposed unit like canteen, transportation
facilities to workers.
The export will result in generation of foreign exchange to the country.
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Annexure 1: CA certificate