PRE-FEASIBILITY...

PPRREE--FFEEAASSIIBBIILLIITTYY RREEPPOORRTT

For Proposed Expansion Project

MMAANNUUFFAACCTTUURRIINNGG OOFF SSPPEECCIIAALLTTYY CCHHEEMMIICCAALL && IINNTTEERRMMEEDDIIAATTEESS

By

M/s. ODYSSEY ORGANICS PVT. LTD. Plot No, B-36, 37, 39, Birwadi M.I.D.C., Taluka: Mahad,

District: Raigad, Maharashtra, India

Conducted & Prepared By

GREEN CIRCLE, INC. Integrated HSEQR Consulting Engineers, Scientists & Trainers

(MoEF Recognized Environment Laboratory) (An ISO: 9001, 14001, NABL/17025:2005, OHSAS: 18001 Certified Organization & GPCB approved Environment

Auditor – Schedule II) Gujarat High Court Stay Order for QCI NABET No. C/SCA/10311/2012 dated 24.01.2013

Green Empire (Anupushpam), Above Axis Bank, Nr. Yash Complex, Gotri Road, Vadodara-390 021 (Gujarat) India Tel: 0265-2371269.

Corp. Office & Environmental Research Laboratory:

Flat No 6 ,Ground Floor,Shakuntala Niwas, M G Road,Borivali (E),Mumbai- 400066

Mumbai office

Tel : 022-28943090 /60 www.greencircleinc.com

ALSO AT

E: [email protected]

BENGALURU RUDRAPUR NEW DELHI HYDERABAD PUNE RAIPUR KOLKATA GOA

OVERSEAS

AUSTRALIA OMAN KUWAIT AFRICA VIETNAM

http://www.greencircleinc.com/�

Project: Manufacturing of Specialty chemical & Intermediates Developer: M/s. Odyssey Organics Pvt. Ltd.

TABLE OF CONTENTS

LIST OF TABLES

Sl. No. Particulars Page No.

1 Introduction 1

2 Benefits of Project 3

3 Project Location 3

4 Cost of Project 5

5 Proposed Product Details 6

6 Raw Material Requirement 8

7 Process Details 14

8 Utility and Requirements 14

9 Stack Details & Fuel Requirement 19

10 Hazardous Waste Generation and Management 20

11 Land Requirement Details 21

12 Green Belt Development 24

13 Storm Water-Collection and Disposal 24

14 Conclusion 24

Table.

No. Particulars Page No.

1 Environment setting of the proposed project 4

2 Proposed Cost 6

3 Name of Product with its Quantity 6

4 Details of Raw Material for Nitro Amino Phenol Group 8

5 Details of Raw Material Requirement for Bulk Drug &

Intermediates 10

6 Details of Water Requirement & Waste Water

Generation 14


LIST OF FIGURES

7 Details of Power Consumption 18

8 Employment Details 19

9 Details of Flue gas Stack 19

10 Hazardous Waste Management 20

11 Non Hazardous Solid Waste Generation 20

12 Details of Land use Break-up 21

Fig. No. Particulars Page No.

1 Google image of propose site 5

2 Water Balance Diagram 15

3 Flow Diagram of Existing ETP 16

4 Flow Diagram of Existing MEE 18

5 Lay-out Plan of Plot no. 36 & 37 22

6 Lay-out Plan of Plot no. 39 23


Pre-Feasibility Report 1

1. INTRODUCTION

M/s. Odyssey Organics Pvt Ltd is situated at Birwadi M.I.D.C. area of Raigad district in

Maharashtra State. M/s Odyssey Organics Pvt Limited is engaged in the manufacturing

of Specialty Chemicals and also expansions as well as new projects to manufacture the

Organic Chemicals which include – “Dyes Intermediates” (Nitro Amino Phenol groups),

Bulk Drug & Bulk Drug Intermediates.

Odyssey Organics Pvt. Ltd is established in 2006. Basically it is a sister concern – “Apte

Organics Pvt. Ltd” – situated at Mahad industrial area –since 1989. The company was

founded by a sound technocrat – Mr. D. V. Apte (M.Sc. By Research).

The company has almost 13 years versatile experience in the field of Organic Chemical

Manufacturing. Odyssey Organics Pvt Ltd having a sound technical knowledge &

hence he provide excellent quality in the market with innovative production process.

Innovative changes in the process, company always get success to overcome from the

process challenge like – Low Yields, Inferior Product Quality, High Raw Material Costs, &

Effluent treatment.

Due to above all, Odyssey Organics Pvt. Ltd has produced the products in competitive

cost with effective reduction in energy, water, raw materials & other resources. They

operate in a responsible manner and comply with all environmental, health and safety

standards. Hence company faces minimal obligations from Government departments

as well as International bodies. This is one of greatest advantageous over our

competitors. Due to it he gives a consistent & continuous supply to customers.

As chemical companies around the world reach out to enhance their strength &

competitiveness. In past 13 years since 2000, Odyssey Organics Pvt. Ltd has entered in

existing product field then he has given tough competition to Chinese origin material.

Before 2000 all materials were imported from China. Company slowly raises our market

share and from 6 years the situation is – the Indian Industry is no more importing the

products from China. Also company has taken a major share of China from global

customers. For the same Odyssey Organics Pvt. Ltd won the “National Awards” from

central govt. H.R. Ministry.

The company upcoming project also includes the same type of products. Which at

present are only manufactured from China. Our Indian consumers are totally

dependent on China. This results in to increase in Import.



1.1. COMPANY PROFILE

Odyssey Organics Pvt. Ltd is established in 2006. Basically it is a sister concern – “Apte

Organics Pvt. Ltd” – situated at Mahad industrial area –since 1989. The company was

founded by a sound technocrat – Mr. D. V. Apte (M.Sc. By Research).

M/s Odyssey Organics Pvt Limited is engaged in the manufacturing of Specialty

Chemicals. The present product is Picric acid, Sodium Picramate and Picramic Acid.

Previously these products were only manufactured in China.

The company has pioneer of the above products in India & supplying the quality

material in Indian & global dyestuff industry. Our Indian market is mainly located at

Gujarat, Rajasthan, while company exports to Japan, Bangladesh, Germany, U.K, Russia

& U.S.A.

1.2. COMPANY MISSION & VISION.

Vision Statement

“We must always look for versatile molecules & should manufacture them with a

Quality & Quantity.”

In an upcoming future the ‘Odyssey –Group’ must be one of the genuine &

reputed group in the Chemical Industry with the diverse specialties.

We are working not only for our own growth counts in “Money” – but we are

working for “Esteem” & “Satisfaction”.

Along with our own growth we aim to contribute & strengthen the Indian

Chemical Industry by Manufacturing the Products, for which our industry

depends on other nations.

“ODYSSEY”- MUST BE ONE OF THE IPORTANT FACTOR FOR INDIAN CHEMICAL

INDUSTRY BY ITS PRODUCT RANGE.”

Mission

The excellent team building, Innovative technologies, & transparent Working

systems are our Strengths.

Follow the International standard Systems & Quality Management Systems and

also bound for the Continuous Improvements & Quality Management through

the same.

Safe Working, Zero Accidents & Green Environment are our mottos.

Complete customer satisfaction & Quality service is our trade mark in the

market.”

1.3. MARKET ANALYSIS

The project is design with the optimum market study & data collection.

The project is based to target mainly the Indian consumers.



The consumers will be the – reputed chemical industries in India as well as some

from Global MNC.

For the project of – Average share of each product varies from min. 20 MT to

Max 60 MT / month.

While the total annual turnover expected from this Project in total is up to 250 Cr.

1.4. EXPORT POSSIBILITY

Most of the bulk export through by Sea from J.N.P.T. Port Bombay.

2. BENEFITS OF PROJECT

I. Reduce Import: It ultimately aiming to enter in to Chinese dominating products - it

will directly reduce the Import of Chinese origin product (Total amount is

approximate 220 Cr/ year).

II. Increase Export: As part of our produced material will get consume globally it will

increase the Export. (Approximate amount will be 45 Cr).

III. Local Economy Rolling: The main raw material required for the above projects will

be purchased locally from Indian Manufacturers. Also the major consumer base

will be in India. Ultimately it contributes in the local rolling of the economy & local

business.

IV. Job Generation: The Project will create direct & indirect employment opportunities

within the surrounding region. The Unit will use good faith efforts to employ local

people from the nearby villages depending upon the availability of skilled & un-

skilled man-power surrounding the project site. In operation phase, the proposed

project would require significant workforce of non-technical and technical

persons. Migration of highly education and skilled experience will result in increase

of literacy in the surrounding villages.

3. PROJECT LOCATION

The Plant is located at plot no. B-36, 37, 39, Birwadi MIDC, Taluka- Mahad, Dist. Raigad,

State-Maharashtra. The Total Plot area of the site is 25,000 sq m. The environmental

setting around the site is given in Table-1 and the Google image of project site is shown

as Figure 1.



Table 1: Environment setting of the proposed project

Sl. No. Particulars Details

1 Latitude 18° 06.147’N

2 Longitude 73°29.369’E

3 Elevation above MSL 60.0 m above Mean Sea Level

4 Present land use at the location Existing Plant

5 Nearest Village Birwadi (3.0 km)

6 Nearest Town/City Town: Mahad (10.0 km)

7 Nearest Railway Station Veer Railway Station (19 km)

8 Nearest Hospital M.M.A Hospital M.I.D.C (3.0 km)

9 Nearest Highway NH 17 (4.0 km)

10 Nearest Airport Mumbai Airport (190.0 km)

11 Nearest Water Body Kal River (1.0 km)

12 Ecologically sensitive zones within

10-km distance

No Eco sensitive Zone present within 10

km of radius.

13 Historical/ Archaeological places Raigad Fort (16 km), Chavdar Tale (8 km)

14 National Parks/Wild Life Sanctuary NA

15 List of Major Industries (within 10 km) Sandoz, Privi, Sudarshan, Vinati,

16 Seismic Zone Zone – III



Specific location and Project Boundary (10 km)

Figure 1 : Google image of Specific location and Project boundary

4. COST OF PROJECT

Estimated Cost of proposed expansion as on date is approx 215.0 crores. Company has

planned to expend 43 crores in Effluent Treatment System include in total proposed

estimated cost. The detailed project cost proposed is as given in Table 2.



Table 2. Proposed Cost

S.No. Description Amount in Crore (INR)

1 Expansion of Current Products 30

2 Starting of 3 New Molecules 80

3 Starting of 2 – Dyes Intermediates 25

4 Starting of Bulk Intermediate 80

Total 215

5. PROPOSED PRODUCT DETAILS

At present the production capacities of M/s Odyssey Organics Pvt. Ltd. is 34.0 MT/Month

and propose to expand manufacturing capacity by 1651.0 MT/Month. The detail

products capacity is given in Table-3.

Table 3 : Name of Product with its Qty.

Sr. No Product Name Quantity, MT/Month

Existing Proposed Total

A Dyes Intermediate – Nitro Amino Phenol Group

1 2,4-Dinitrochlorobenzene Nil 220 220

2 2,4-Dinitrophenol

9.8 (Intermediate

for In-house

Consumption)

106.2 116

3 Picric Acid

12.0

(Intermediate for

In-house

Consumption)

128 140

4 Sodium Picramate 10.0 75 85

5 Picramic Acid 5.0 13.0 18

6 4 - Nap Nil 50 50

7 Dinitro – Sec. Butyl Phenol Nil 100 100

8 N-Amino Dinitro Benzene Nil 30 30

9 4-Nitro-Ortho Xylene Nil 80 80

10 2-Nitro-4-Chloro Sulfonic Nil 29 29





Chlorobenzene

11 2-Nitro-4-Chloro Sulfonamide

Chlorobenzene Nil 23 23

12 2-Amino-4-Chlorosulfonamide

Phenol Nil 17.0 17

13 Monochlorobenzene Nil 150 150

B Bulk Drugs & Intermediates

1 2-Methoxy Naphthalene Nil 80 80

2 2-Acetyl-6-Methoxy

Naphthalene Nil 86 86

3 3-Nitro Acetophenone Nil 32 32

4 3-Amino Acetophenone Nil 26 26

5 3-Hydroxy Acetophenone Nil 20 20

6 3-Acetoxy Acetophenone Nil 10 10

7 4-Amino-Salicyclic Acid Nil 44 44

8 Sodium Pas Nil 40 40

9 3-Amino Pyrazole 4-

Carboxamide Hemisulphate Nil 36 36

10 Allopurinol Nil 10 10

11 C.P.A. Derivative Of Q Acid Nil 174 174

12 Ciprofloxacin –Q Acid Nil 126 126

13 Ciprofloxacin Base Nil 30 30

14 Ciprofloxacin Hydrochloride Nil 29 29

C By-Products

1 80% Spent Sulfuric Acid 10 1820 1830

2 Water White 30% Spent Sulfuric

Acid 100 100 200

3 Dil Acetic Acid Nil 65 65

4 30% Hydrochloric Acid Nil 166 166

5 Ethanol Nil 36 36

6 Copper Oxide Nil 40 40

7 Ammonium Sulfate Nil 80 80

8 Sodium Methyl Sulfate Nil 87 87

9 2-Nitro Acetophenone Nil 22 22

10 Sodium Acetate Nil 6 6





11 Dichlorobenzene Nill 36 36

12 1-Acetyl-2-Methoxy

Naphthalene Nil 10 10

13 Coal Ash Nil 200 200

6. RAW MATERIAL REQUIREMENT

Raw materials is purchased from indigenous and abroad market by roads/sea way.

Details of raw material required for enhancement of existing Products and Proposed

Products given in Table-4 & Table-5.

Table 4 : Details of Raw Material Requirement for Nitro Amino Phenol Group

S.No. Name of Raw

Material

Quantity /

Month Source Transportation Storage Condition

A Basic Raw Material

1 Sulfuric Acid (98%) 1080 Mt Domestic (DMC

Roha) Road Tank

2 Sulfuric Acid (30%) 90 Kl Self Made (Bi-

product) Road Tank

3 Fuming Nitric Acid 185 Mt Domestic (RCF) Road Tank

4 Nitric Acid 70% 175 Mt Domestic Road Tank

5 Caustic Lye (50%) 290 Mt

Domestic &

Imported

(Trader)

Road Tank

6

Sodium Hydrogen

Sulphide 30%

Aqueous Solution

140 Kl Domestic Road Tank

7 Sodium Sulfate

(Na2s) 26 Mt Domestic Road Bag

8 Lime Powder 32 Mt Domestic Road Bag



S.No. Name of Raw

Material

Quantity /


9 Sulphur Powder 20 Mt

10 Urea Only 220

Kg Domestic Road Bag

11 Sodium Chloride

Salt 8.0 Mt Domestic Road Bag

12 Hydrogen

Peroxide 3 Mt Domestic Road Cans

13 Organic Amines 6.0 Mt Domestic Road Tanks

14 20% Aqueous

Ammonia Solution 25 Kl Domestic Road Cans

15 Chloro Sulfonic

Acid 35 Mt Domestic Road Tank

16 Dil. Hydrochloric

Acd 12 Kl Domestic Road Tank

17 Ice 230 Mt Self Produce +

domestic Road Containar

18 Acetic Anhydride 54 Mt Domestic Road Tank

19 Chlorine Gas 120 Mt Domestic Road Cylinders

20 Ferric Chloride 30 Mt Domestic Road Bag

B Solvents - Raw Material

1 Iso Propyl Alcohol 6.0 Mt Domestic Road Tank

2 Methylene Di

Chloridee 10 Mt Domestic Road Tank

3 Ethylene Di

Chloride 10 Mt Domestic Road Tank

4 Ethyl Benzene 50 Mt Domestic Road Tank



S.No. Name of Raw

Material

Quantity /


C Main Organic Raw Material as –

Starting Material

1 Mono Chloro

Benzene 117 Mt Domestic Road Tank

2 2,4- Dinitrochloro

Benzene 226 Mt

Domestic + Self

Made Road Bags

3 2,4- Dinitro Phenol 116 Mt Self Made Road Carboys

4 Picric Acid 104 Mt Self Made Road Carboys

5 Sodium Picramate 22 Mt Self Made Road Carboys

6 2- Secondary Butyl

Phenol 66 Mt Domestic Road Tank

7 Ortho Xylene 60 Mt Domestic +

Import Road / Sea Tank

8 O –Nitro

Chlorobenzene 18 Mt Domestic Road Bags

9

2-Chloro-4-

Chlorosulfon

Chlorobenzene

29 Mt Self Made Road Carboys

10

2-Nitro-4-

Sulfonamide

Chlorobenzene

23 Mt Self Made Road Carboys

11 Benzene 130 Mt Domestic Road Drum

Table 5 : Details of Raw Material Requirement for Bulk Drug & Intermediates

No Particulars Quantity

/ Month Source Transportation Storage Condition





A Basic Raw Materials

1 Sulfuric Acid 584 Mt Domestic Road Tank

2 Caustic Lye 50% 60 Mt Domestic Road Tank

3 Dil Sulfuric Acid 105 Mt Self Made Road Tank

4 Caustic Flex 46 Mt Imported Sea / Road Tank

5 Ice 94 Mt Self Made Road Container

6 Acetic Anhydride 60 Mt Domestic Road Tank

7 Zinc Chloride

Anhydrous 110 Mt Domestic Road Bags

8 Dimethyl Sulfate 164 Mt Domestic Road Tank

9 Sodium Methoxide 35 Mt Import Sea & Road Drums

10 Cyclopropyl Amine 32 Mt Import Sea & Road Drums

11 Sodium Sulfate

Anhydrous 1 Mt Domestic Road Bags

12 Potassium Carbonate 33 Mt Domestic Road Bags

13 Tri Ethyl Ortho

Formate 180 Mt Import Sea & Road Drums

14 Morpholine 110 Mt Import Sea & Road Drums

15 Hydrazine Hydrate 45 Mt Import Sea & Road Drums

16 Formamide 19 Mt Import Sea & Road Drums

17 20% Aqueous

Ammonia 100 Kl Domestic Road Tanks

18 Nitric Acid (72%) 35 Mt Domestic Road Tanks

19 Sodium Nitrate 14 Mt Domestic Road Tanks





20 Sodium Hydrogen

Sulphide 30% 80 Mt Domestic Road Tanks

21 Glacial Acetic Acide 60 Mt Domestic Road Tanks

22 Anhydrous Piperazine 21 Mt Import Sea & Road Bags

23 Carbon Di Oxide Gas 18 Mt Domestic Road Tank / Cylinders

24 Hydrochloric Acid

30% 117 Kl Domestic Road Tanks

25 Dimethyl Sulfoxide 30 Mt Domestic Road Tanks

26 Activated Charcoal 20 Mt Domestic Road Bags

27 H-Flow Supercell 10 Mt Domestic Road Bags

B Solvent – Raw Materials

1 Methanol 30 Kl Domestic Road Tanks

2 Ethanol 5 Kl Domestic Road Tanks

3 Methylene Di

Chloride 30 Kl Domestic Road Tanks

4 Toluene 50 Kl Domestic Road Tanks

5 Dimethyl Carbonate 200 Kl Imported Sea & Road Drums

6 Dimethyl Formamide 80 Kl Domestic Road Tanks

7 Ethyl Acetate 10 Kl Domestic Road Tank

8 Nitrobenzene 20 Mt Domestic Road Tank

9 Butanol 10 Kl Domestic Road Tank

10 Iso Propyl Alcohol 40 Mt Domestic Road Tank

C Main Organic Raw Material as -

Starting Materials





1 Beta Naphthol 77 MT Imported +

Domestic Sea & Road Bags

2 2-Methoxy

Naphthalene 80 MT Self Made Road Carboys

3 Acetophenone 40 MT Domestic +

Imported Sea & Road Tanks

4 3-Nitro

Acetophenone 32 MT Self Made Road Drums

5 3-Amino


6 3- Hydroxy


7 3- Amino Phenol 41 MT Imported Sea & Road Drums

8 4-Amino Salicyclic

Acid 44 MT Self Made Road Drums

9 Cyanoacetamide 22 MT Imported Sea & Road Bags

10 Pyrazole 4-Hydroxy

Hemisulphate 16 MT Self Made Road Carboys

11 Ciprofloxacin “Q –

Acid” 26 MT Self Made Road Carboys

12 Ciprofloxacin Base 26 MT Self Made Road Carboys

13 2,4-Dichloro-5-Fluoro

Acetophenone 120 MT Imported Sea & Road Drums

14

Cyclopropyl Amine

Derivative Of 2,4-

Dichloro-

Acetophenone

174 MT Self Made Road Carboys



7. PROCESS DETAILS

Please refer Exhibit – 2, Manufacturing process of Specialty chemical & Intermediates

along with Process Flow diagram with chemical reaction.

8. UTILITY AND REQUIREMENTS

Company has acquired adequate land and other resources to expand the production

capacity. Other requirements are Power, Water and manpower.

8.1 WATER CONSUMPTION AND WASTE WATER GENERATION

The source of water for the existing as well as proposed expansion meets through MIDC.

Total water requirement for the existing as well as proposed production is 468 KLD (52+

416). 5.4 KLD Domestic effluents shall be disposed through septic tank & soak pit. Existing

Trade effluent generation 26 KLD and proposed additional Trade effluent generation will

be 229 KLD. From existing effluent 16 KLD is recycled through MEE and 10 KLD is send to

CETP. Proposed 229 KLD effluents will be recycled using MEE. Details of water

consumption and waste water generation are tabulated in Table No. 6.

Table 6: Details of Water Requirement & Waste Water Generation

Note: E: Existing, P: Proposed, T: Total after proposed expansion

Sr. No. Particulars

Water Consumption

KL/Day

Waste Water Generation

KL/Day

E P T E P T

1 Domestic 2.5 6.5 9.0 1.5 3.9 5.4

2 Process 23.0 249 272.0

14.0 156 170 3

Gas

Quenching 0.4 11.6 12.0

4 Boiler 15.6 97.4 113.0 12.0 73 85

5 Cooling 2.0 25 27.0 0.0 0.0 0.0

6 Acid Dilution 8.0 22 30.0 0.0 0.0 0.0

7 Green Belt 0.5 4.5 5.0 -- -- --

Total 52 416 468 27.5 232.9 260.4



8.1.1 Water Balance Diagram :

Sock Pit & Septic Tank

Domestic Use 9.0 KLD

(2.5 + 6.5) KLD

17.5.

Total Water Requirement 468 KLD

[Existing 52 KLD+ Proposed 416 KLD

Industrial Use 454 KLD

(49+405) KLD

Gardening 5.0 KLD

(0.5 + 4.5) KLD

Boiler 113 KLD

Disposal at MSWL

Inorganic salts as Sludge from MEE

Process 272 KLD

Acid Dilution 30 KLD

Multiple Effect Evaporator

250 KLD

ETP 255 KLD

170

Evaporation Loss 7.5 KLD

Cooling Tower 25 KLD

Gas Quenching 12 KLD

Sell to other Industries as dilute Acid

5.4 KLD

Condensed Water (90%)

225 KLD

Activated Charcoal

Bed

Recycle & Reuse for Process

85



8.1.2 Effluent Treatment plant :

Effluent is coming from process, boiler feed and gas quenching to be collected

separately in the collection tank. It is to be neutralized, and send to Multiple Effect

Evaporator (MEE). The condensed water obtained from the MEE system is to be send to

Activated Charcoal Bed to remove any traces of Color & Volatile Organic Matter. Thus

this Industrial water can be totally re-cycled & reused. Existing ETP and MEE is shown in

Figure 3 and Figure 4.

Figure 3: Flow Diagram of Existing ETP

At Present Odyssey Organics handles 3 Main Effluent Streams –

Second is Reduction Stream as below:

SPENT SULFURIC ACID

NITRATION PROCESS

STORAGE TANKS

100 % SALE AS BI-PRODUCT

NEUTRALIZATION STORAGE TANKS

MULTIPLE EFFECT EVAPORATOR

(1000 KG / HR)

CONDENSE WATER STORAGE

RECYCLE SLUDGE

M.S.W.L

REDUCTION STREAM



The Third - Hydrolysis Stream Is As Below.

In the below diagram:

A & B– Collection & Primary Treatment Tanks (Neutralization & Hydrogen Peroxide Mixing).

C - Primary Clarifier to settle the Solids,

D – Secondary Tank (aeration)

E – Secondary Clarifier,

V- “V” – Shaped Notch for Sample collection & Discharge to C.E.T.P

HYDROLYSIS STREAM

STORAGE TANKS 1

A B

C

D E

TO C.E.T.P. V



Figure 4 : Flow Diagram of Existing MEE of capacity 1000 Kg/Hour

8.2 POWER CONSUMPTION

The Source of Electricity obtained from M.S.E.B. The power demand for the existing

manufacturing activity is 146 KVA and 3431 KVA will be required for proposed

expansion.

Table 7 : Details of Power Consumption

Sr. No. Particulars Power Consumption (KVA)

Source Existing Proposed Total

1 Operations M.S.E.B 89 2236 2325

2 Effluent Treatment M.S.E.B 55 839 894

3 Other General M.S.E.B 2 356 358

4 DG Set D.G. Set

(Stand By) 125 125*3 125*4



8.3 MANPOWER REQUIREMENT

The Project will create direct & indirect employment opportunities within the surrounding

region. The Unit will use good faith efforts to employ local people from the nearby

villages depending upon the availability of skilled & un-skilled man-power surrounding

the project site. In operation phase, the proposed project would require significant

workforce of non-technical and technical persons. Migration of highly education and

skilled experience will result in increase of literacy in the surrounding villages.

Table 8: Employment Details

Sr.

No. Descriptions

Nos.

Existing Proposed Total after proposed

expansion

1 Direct

employment

55 65 120

9. STACK DETAILS AND FUEL REQUIREMENT :

In the existing unit Briquetes is used as a fuel for Boiler and Diesel is used as a fuel for D.G

set. Details of stacks and D.G. set is given in Table 9. Table 9: Details of Flue gas Stack

Sr.

No

.

Stack

attached to

Capacit

y Status

Stack

Height

(m)

Stack

Dia.

(mm)

Fuel name

& Quantity

Stack

Gas

Temp

(°C)

Air

Pollution

Control

Measure

1 Boiler (Non

IBR) 1

500 kg

/hr Existing 18 400

Briquetes,

60

Mt/Month

130 Stack

2 IBR Boiler 12,000

kg/ hr Proposed 22 600

Coal, 250

MT/Month 180 Stack

3 D.G Set 125 KVA Existing 10 400 Diesel, 500

lit/Month 80 Stack

4 DG Set 125*3

KVA Proposed 10 400

Diesel, 1500

lit/Month 80 Stack



10. HAZARDOUS WASTE GENERATION AND MANAGEMENT

Hazardous waste generated from the process & maintenance. The Management of

Hazardous waste will be done as per Hazardous Waste Management Rules 2008. The

Hazardous waste generation and management are shown in Table 10.

Table 10 : Hazardous Waste Management

Sr.

No

.

Hazardous

Waste

Category

No.

Quantity (MT/Month) Source of

Generation

Stora

ge Disposal

E P T

1 Used Oil 5.1 30 150 180

Plant

Maintenan

ce

Drum

Selling to

registered

Refiner

2 ETP Sludge 26.2 2 13 15 ETP Bag

M.S.W.L. for

Land Fill or

Incineration

3

Solid

Sludge

from MEE

34.4 10 1720 1730 MEE Bag

M.S.W.L. for

Land Fill or

Incineration

4 Organic

Residue 28.1 Nil 25 25 Process Bag M.S.W.L.

5 Process

Waste 26.1 12 1738 1750 Process Bag

M.S.W.L. for

Land Fill or

Incineration

6

Discarded

Bags &

Container

33.3 1200 6000 7200 Production

Section

Store

into

SWSA

Selling to

registered

reuser/recyc

lers

10.1 NON-HAZARDOUS SOLID WASTE GENERATION AND MANAGEMENT.

Table 11 : Non Hazardous Solid Waste Generation

Sr. No Name of solid waste Quantity (Mt/month)

Management E P T

1 Canteen Waste 1 3 4 Send to Municipal

Corporation, Mahad

2 Paper, cardboard,

Metal scrap etc 3 7 10

Selling to registered

reuser/recyclers



3

Total Salt Content As :

Sodium Sulfate &

Sodium Chloride Mixture

Nil 1360 1360 Send to M.S.W.L

4

Total Salt Content As :

Sodium Thiosulfate Nil 360 360 Send to M.S.W.L

5 Total Salts As

Ammonium Chloride Nil 120 120 Send to M.S.W.L

11. LAND REQUIREMENT DETAILS

The existing unit of M/s. Odyssey Organics Pvt. Ltd. is located at plot no. B-36, 37, 39,

Birwadi MIDC, Taluka: Mahad, District: Raigad, Maharashtra. Total Plot area of the plant

is 25000 m2. The break-up area detail is given in Table 12 and the Plant Layout of the unit

is given in Figure 5 & Figure 6.

Table 12: Details of Land use Break-up

S. No. Particulars

Land Area in Sq.m

Existing

Proposed

1 Plant Facilities 798 10,399

2 Administrative Building and

Canteen 2,490 500

3

Effluent treatment plant –

multiple effect evaporator

& other systeems

586 2,475

4 Internal Approach roads 1,515 838

5 Green belt /plantation 1847 3552

6 TOTAL PLANT AREA 7,236 17,764

7 Open space to be use for

Future expansion 17,764 NIL

Total AREA 25,000



Figure 5. Layout Plan of Plot no. 36 & 37



Figure 6. Layout Plan of Plot no.39



12. GREEN BELT DEVELOPMENT

Unit has already developed greenbelt area in 5399 Sq m within plant premises. There

are shrubs and trees developed in the greenbelt area. 21.6 % of the total plot area is

earmarked for green cover and open space development in the existing facility.

Suitable plant species of local varieties will be planted with adequate spacing and

density for their fast growth and survival.

13. STROM WATER MANAGEMENT

Surface drainage has designed based on the maximum rainfall intensity prevalent in the

area. All the building has been provided with a plinth protection all round, sloped

towards the side drain. The storm water collection system has designed in such a

manner so that clean storm water from garden, parking areas, roadways and lawns.

14. Conclusion

Looking at the present market scenario, it is concluded that the project is not only feasible and viable, but it will also increase the employment Opportunity in future.

Date post:	14-Feb-2020
Category:	Documents
Upload:	others
View:	72 times
Download:	1 times

PRE-FEASIBILITY...

Documents