Pre - Feasibility Report For Delta Finochem Pvt....

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.

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



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


Connected load: 1000 kw


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



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



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.



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.



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



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.



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



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



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



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



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



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



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.



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



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


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



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


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



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



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



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



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



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



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



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



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.



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



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



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:



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



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%



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.



Annexure 1: CA certificate

Pre - Feasibility Report For Delta Finochem Pvt....

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