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PRE-FEASIBILITY REPORT

On

Proposed Coal Tar Distillation Project to manufacture 84,000MT/ Annum Coal Tar Pitch and its by – products

OF

M/s. SHOBHA CHEMICAL INDUSTRIES PVT. LTD.At-Jammal, Jharsuguda District,Odisha

Prepared by:- SEPTEMBER-2015

VISIONTEK CONSULTANCY SERVICES PVT. LTD(An Enviro Engineering Consulting Cell)

Plot No.-108, District Centre, Chandrasekharpur, Bhubaneswar-16,Phone No. : 91-674-2744594, 3250790, Fax: 91-674-2744594

[email protected] , [email protected] us at - www.vcspl.org

TABLE OF CONTENTS

Sl. No. Particulars PageNo.

CHAPTER-11 Executive Summary 1

1.0 Introduction 22.0 Project Description 23.0 Site Analysis 44.0 Land Use Planning 55.0 Proposed Infrastructure 56.0 Rehabilitation & Resettlements (R & R) Plan 57.0 Project Schedule & Cost Estimates 68.0 Analysis of Proposal 6

CHAPTER-2 INTRODUCTION2.1 Introduction 72.2 Identification of Project & Project Proponent 72.3 Description of Nature of the Project 72.4 Need of the Project & its importance to the Country and/or Region 82.5 Supply- Demand Gap 82.6 Employment Generation(Direct & Indirect) due to the Project 9

CHAPTER-3 PROJECT DESCRIPTION3.1 Type of Project 123.2 Location & Accessibility 123.3 Site Selection 153.4 Size of Magnitude of Operation 153.5 Project Description 153.6 Plant Layout 213.7 Water and power requirement 243.8 Pollution sources and its Control measures 243.9 Schematic representations of the feasibility drawing which give information of eia

purpose.26

CHAPTER-4 SITE ANALYSIS4.1 General 284.2 Connectivity 284.3 Topography 284.4 Existing Land Use Pattern 284.5 Existing Infrastructure 284.6 Climate Data 29

CHAPTER-5 PLANNING BRIEF5.1 Planning Brief 305.2 Population Projection 305.3 Land Use Planning 305.4 Amenities & Facilities 31

CHAPTER-6 PRPOSED INFRASTRUCTURE

6.1 Industrial Area 326.2 Residential Area 326.3 Green Belt 326.4 Social Infrastructure 326.5 Connectivity 336.6 Drinking water Management 336.7 Sewerage System 336.8 Run- off Management 336.9 Industrial Waste Management 34

6.10 Solid Waste management 356.11 Power Requirement and supply/source 35

CHAPTER-7 REHABILITATION & RESETTLEMENT(R & R) PLAN7.1 Policy to be adopted for R & R w.r.t Project 36

CHAPTER-8 PROJECT SCHEDULE & COST ESTIMATES8.1 Project Schedule 378.2 Project Cost 39

CHAPTER-9 ANALYSIS OF PROPOSAL9.1 Financial & Social Benefits 409.2 Other benefits 41

LIST OF TABLES

Sr.No PARTICULARS PAGENo.

1.0 Product Profile 31.1 Requirement of Raw Materials 31.2 Solid Waste Generation & Management 42.0 Project Profile 82.1 Category wise manpower breakup 113.0 Production capacity of the Company 153.1 Requirements of Raw Materials 213.2 Water Requirement & Source 243.3 Solid waste generation and management 253.4 Domestic solid waste generation and management 253.5 Hazardous waste generation and management 265.0 Land Use Break-Up 316.0 Solid Waste Generation & Management 358.0 Project Cost Break- Up 39

LIST OF FIGURES

Fig. No. Particulars Page no.3.0 Plant Location 133.1 TOPO Map(10 Km Radius) 143.2 Process Flow Diagram (Coal Tar Pitch) 183.3 Process Flow Diagram (Heavy Creosote Oil/

Anthracite Oil)18

3.4 Plant Layout 233.5 Water Balance 243.6 Schematic Representation 27

M/s Shobha Chemical Industries Private LimitedPre- Feasibility Report on Proposed Coal Tar distillation project to manufacture 84,000 MT/ AnnumCoal tar Pitch and its By- products At- Village Jammal, P.O- Godigaon, Kolabira, Jharsuguda district,Odisha

Visiontek Consultancy Services Private Limited Page 1

CHAPTER - I

EXECUTIVE SUMMARY

1 Name of the project Proposed Coal Tar Distillation Project to Manufacture

84,000 MT/Annum Coal tar Pitch and its By- products.

2 Sl. No. in the schedule 4(b)

3 Registered Office C-302, lumbini palace, Tejpal Road, Velle Parle (East),

Mumbai- 400057, maharastra

4 Name of the promoters Shri Danmal Porwal( Director)

Smt. Shobha Porwal( managing Director)

5 Present Business Coal Tar & its By- Products

6 Area of Plant 4.76 Acres

7 Topo Sheet No. 73C/1

8 Latitude

Longitude

210 50’ 10.42”N

840 07’ 07.17”E

9 Proposed Capacity 84,000 MT/ Month Coal Tar Pitch and its By- Products

10 Cost of Project 398.00Lakhs

11 Manpower Requirement 25 People

12 Power Requirement Total power requirement for the project is 250 KVA,

which will be met from 11 KV H.T. line from WESCO

13 Nearest Railway Station/airport along

with distance in kms.

Nearest railway station – Jharsuguda at- 9 Km W

Bhubaneswar Airport-248 km.

14 Nearest town, City, District Head

quarters along with distance in kms.

Jharsuguda 9.0 Km W

15 Village Panchayats, Zilla Paris

had,Municipal corporation, Local

telephone nos. to be given) body

(complete postal addresses

with telephone no.s to be given)

At- Jammal

P.O-Godigaon

Block & Tehsil-Kolabira

Village Panchayat-Kelendamal

District-Jharsuguda, Odisha



1.0 INTRODUCTION

1.1 Identification of Project and Project Proponent

M/s Shobha Chemical Industries Pvt. Ltd. had proposed to setup a coal tar distillation

unit to produce 84,000 MT/Annum coal tar pitch and its by- product At-Jammal, P.O-

Gadigaon, Kolabira, District- Jharsuguda, Odisha. As per the EIA notification ammendmnent

on dtd 25th June 2014 Coal Tar distillation projects are enlisted under serial number 4(b) and

will be appraised at SEIAA, Odisha for Environmental Clearance. Here it can be mentioned

that Consent to Establish for the proposed project has been obtained from SPCB, Odisha vide

letter no3044/III-CON(NOC) dtd24.08.2013 and accordingly construction has been done.

Shobha Chemical Industries Private Ltd. A Company registered under company’s Act

1956 having its registered office at C-302, Lumbini Palace, Tejpal Road, Ville Parle (East)

Mumbai-Maharastra, Pin Code-400057 was incorporated on 11/10/1993 at Mumbai.

Since Inception compancy’s whole time director Shri Danmal Porwal & Managing

Director Smt. Shobha Porwal has got the vision of setting up Coal tar and its By- Products

manufacturing unit in Odisha but looking to Economic and financial constraints, project got

delayed but now the company’s directors and share holders have decided to move forward in

this direction with full determination and strength.

The company whole time director Shri Danmal Porwal has got an experience of 50 years

in the Coal tar manufacturing line and is the chairman of Porwal Group of Industries with its

various Units located Chhattisgarh and Andhra Pradesh.

1.2 Employment GenerationIt is estimated that the total employment generation due to the proposed project will be 25.

3.0 PROJECT DESCRIPTION2.1 Location

The proposed Project will be located at Jammal Village, P.O- Gadigaon, Kolabira

,Jharsuguda District of Odisha State (Ref: Topo sheet 73C/1). The Latitude and Longitude of

the proposed site 21⁰ 50’ 10.42”N and 84⁰ 07’ 07.17”E respectively.

2.2 Site SelectionSite is located at Jammal Village, P.O- Gadigaon, Kolabira ,Jharsuguda District of Odisha

State. The site has following facilities:



Proximity to the sources of base raw material,

Availability of common Infrastructure facilities / utilities (water / power etc.),

2.3 Technology SelectionTechnology selection involves an analysis of past achievements, present status and future

prospects of each technology under consideration keeping in view the following criteria.

Availability of project plant capacity/module.

Suiting to selected product mix & raw materials

Conservation of scarce inputs such as power & water.

Considerations of capital cost & maintenance cost.

Plant is going to utilize blended Crude Coal tar to produce Coal tar pitch and its by-products

by using Horizontal distillation technology.

2.4 Product ProfileM/s Shobha Chemical Industries Pvt. Ltd. intends to set up Coal tar distillation plant to

produce 84,000 MT per Annum Coal Tar Pitch & its by-products at Jammal Village, P.O-

Gadigaon, Kolabira ,Jharsuguda District of Odisha State.

Table 1.0 Product Profile

SI. No. Units Product Capacity1 Coal Tar Distillation

Plant(1 X 233 TPD)Coal Tar Pitch 24,000 TPA

2 Creosote Oil 24,000 TPA3 Coal tar of various grade 10,000 TPA4 Naphthalene of various grade 1200 TPA5 Melting Pitch 24,000 TPA6 Carbolic Products 800 TPA

2.5 Raw material RequirementTable 1.1 Requirements of Raw Materials

Sl. No. Particulars Quantity in TPA Source Mode oftransportation

1 Anthracene Oil 990 Open Market By Road2 Carbolic Oil 165 Open Market By Road3 Clear Tar 8250 Open Market By Road4 Coal Tar Wash Oil 165 Open Market By Road5 Coal Tar Fuel 1650 Open Market By Road6 Crude Coal Tar/coal 11550 Open Market By Road7 Crude Napthalene 360 Open Market By Road8 Crude Tar Acid 360 Open Market By Road



9 Depitched Tar Acid 990 Open Market By Road10 Dephenolised Coal Tar Oil 3960 Open Market By Road11 Drained Napthalene Oil 330 Open Market By Road12 Heavy Benzol 360 Open Market By Road13 Heavy & Light Creosote Oil 5400 Open Market By Road14 H.P.Napthalene 720 Open Market By Road15 Musk from Benzol 50 Open Market By Road16 Naptha Varius grade 360 Open Market By Road17 Napthalene various grade 3600 Open Market By Road18 Phenol Fraction 3000 Open Market By Road19 Pitch/Coaltar pitch various

grade18000 Open Market By Road

20 Pitch creosote Mix variousgrade

4200 Open Market By Road

21 Spent Solar Oil 350 Open Market By Road22 Still Bottom Oil 350 Open Market By Road23 Tar Pitch 18000 Open Market By Road24 Xylene 5 Open Market By Road25 N.G. tolune 6 Open Market By Road26 Benzene 120 Open Market By Road

2.6 Water & power RequirementThe total water requirement of proposed plant will be 0.68 m³/day, Out of which 0.2

m³/day will be sourced from borewell and 0.48 m³/day will be sourced from rainwater

harvesting pond. Power requirement of proposed plant will be 250 KVA, which will be met

from 11 KV H.T. line from WESCO.

2.7 Waste Water Generation & ManagementWaste water of 100 m³/ month generated from plant will be stored in storage tank and after

treatment in ETP shall used in dust suppression and green belt.

Table 1.2 Solid Waste Generation and Management

Sl. No. Units Solid Wastes Qty In TPA Disposal practice1 Coal Tar distillation Plant Dust from APC devices 1.6 Reused in process

4.0 SITE ANALYSIS3.1 Connectivity

The site is well connected with road. NH – 200 is at distance of 1.53 km from the project

site. Nearest railway station is Jharsuguda at a distance of 9 Km W direction from the project

site. Nearest airport is at Bhubaneswar, 248 Km from proposed project site in its SE side.

Nearest seaport is Paradeep at a distance of 315.0 km SE from the project site.



3.2 Topography and existing Land Use PatternThe topography of the land is generally flat and well suited for development of industrial

projects. Project / Plant is coming under the non- forest category land.

3.3 Climate DataThe climate of the Jharsuguda district is characterized by hot summer with low humidity.

During the summer maximum temperature is 48.0 ⁰C. The temperature in the month of

December is lowest i.e. 7 ⁰C. The average annual rainfall is 1527 mm.

4.0 LAND USE PLANNINGTotal land requirement for the proposed unit is about 4.76 acres which is already identified

and acquired.

5.0 PROPOSED INFRASTRUCTURE5.1 Industrial Area

The setting up of the Main Plant Facilities, Raw Material Storage, Ash Storage, Raw

Water Storage Reservoir & Treatment, Auxiliary facilities, viz. Administrative Building,

Technical Building, Workshop, QC Lab, Switch Yard, etc. & Green belt required is 1.57

Acres land out of which 4.76 acres. Company uses nearest road for goods transportation and

equipped with all other required facilities.

5.2 Green BeltA greenbelt development plan will be prepared and implemented along with the project.

Total green belt area shall be 33% (1.57 Ac) of total area (i.e.4.76 Ac). The main objective of

the greenbelt is to provide a barrier between the plant and the surrounding areas.

5.3 Others A garland drain around the plant along boundary is envisaged to collect surface run-off

during rainy season.

Additional drinking water facilities will be provided for employees as well as nearby

villagers.

6.0 REHABILITATION & RESETTLEMENTS (R & R) PLANThe proposed project is going to setting up on 4.76 acres area. Total land has already

been identified and acquired. There is no existence of displaced habitants in the identified

land. Land is also devoid of any vegetation. Local people will be engaged for construction



and operation activities and the local area have all the infrastructure facilities. Here no

housing colony/township is envisaged.

7.0 PROJECT SCHEDULE & COST ESTIMATES7.1 Project Schedule

The proposed project has already been constructed on the basis of Consent to Establish

from SPCB, Odisha vide letter no. 3044/III-CON (NOC) dtd 24.08.2013.

7.2 Project CostAn indicative estimated capital cost of the proposed Plant is Rs. 398.0 Lakhs, including

the pre-operative expenses, contingency and interest during construction.

8.0 ANALYSIS OF PROPOSALThe socio-economic benefits of the proposed project are as follows:

Improvement and construction of road network in the nearby villages.

Extension & renovation of Local School buildings with playgrounds.

Social awareness programme will further improve the quality of life and standard of

living such as sanitation and hygiene, HIV Prevention Programme etc.

Implementation of adult education and female education programmes in the villages

surrounding the project area.

Financial assistance to tale nted and poor students for higher

studies.(Management/Engineering/Medical science)

Expected to employment are 25 persons.



CHAPTER – 02

INTRODUCTION

2.1 Introduction

M/s Shobha Chemical Industries Pvt. Ltd. had proposed to setup a coal tar distillation

unit to produce 84,000 MT/Annum coal tar pitch and its by- product At-Jammal, P.O-

Gadigaon, Kolabira, District- Jharsuguda, odisha. As per the EIA notification ammendmnent

on dtd 25th June 2014 Coal Tar distillation projects are enlisted under serial number 4(b) and

will be appraised at SEIAA, Odisha for Environmental Clearance. Here it can be mentioned

that Consent to Establish for the proposed project has been obtained from SPCB, Odisha vide

letter no3044/III-CON(NOC) dtd24.08.2013 and accordingly construction has been done.


1956 having its registered office at C-302, Lumbani Palace, Tejpal Rpad, Ville Parle (East)


2.2 Identification of Project and Project Proponent


1956 having its registered office at C-302, Lumbani Palace, Tejpal Rpad, Ville Parle (East)


Since Inception compancy’s whole time director Shri Danmal Porwal & Managing

Director Smt. Shobha Porwal has got the vision of setting up Coal tar and its By- Products

manufacturing unit in Odisha but looking to Economic and financial constraints, project got

delayed but now the company’s directors and share holders have decided to move forward in

this direction with full determination and strength.

The company whole time director Shri Danmal Porwal has got an experience of 50 years

in the Coal tar manufacturing line and is the chairman of Porwal Group of Industries with its

various Units located Chhattisgarh and Andhra Pradesh.

2.3 Description of Nature of the project

M/s Shobha Chemical Industries Pvt. Ltd. intends to set up Coal tar distillation plant to

produce 84,000 MT per Annum Coal Tar Pitch & its bi-products at Jammal Village, P.O-




Table 2.0 Project Profile




Crude Coaltar is stored in storage tanks and from there Coaltar will go to process tank

through pipe lines. In process tank Blending will be done and then processed feedstock will

go to Horizontal distillation units and there the distillation process is carried out either under

Vacuum or atmospheric pressure and by products which are obtained will be collected and

stored which will be further processed or sold as such. The end product is Coal tar Pitch

which will be loaded in specified Insulated Road tankers or in solid state in bags and will be

sent to the customers.

2.4 Need of the Project and its Importance to the Country and/or Region

Coal Tar Pitch is primarily used as a binding agent in the production of carbon electrodes

and graphite electrodes which are used in the production of aluminium and steel respectively.

The aluminium industry is the largest Coal tar Pitch consumer segment. Binder grade coal tar

pitch is a key ingredient in the manufacture of carbon anodes in aluminium smelters.

Graphite electrode industry is the second- largest Coal Tar Pitch consumer segment.

Impregnated Coal tar Pitch is used in the manufacture of graphite electrodes, which is used in

EAF for production of steel.

Current market potential for Coal Tar Pitch in India is about 3, 00,000 TPA is mainly

used in making green carbon anodes for electrolyte pots in smelters and manufacture of

graphite electrodes. The specific requirement of Coal Tar Pitch in Aluminium smelters

ranges from 90 to 110 kg per ton of aluminium metal.

2.5 Supply – Demand gap

India’s consumption pattern of Coal tar Pitch by industry clearly reveals that aluminium

industry I s the major user segment accounting for 73 % of the Coal Tar Pitch consumption,



followed by graphite accounting for 22 % and 5 % for other applications. The analysis of the

domestic Coal Tar pitch industry shows the following facts-

Coal Tar Pitch is primarily used as binding agent in the production of carbon anodes and

electrodes and graphite electrodes which are used in the production of aluminium and steel

respectively.

The aluminium industry is the largest Coal tar Pitch consumer segment. Binder grade Coal

Tar Pitch is a key ingredient in the manufacture of carbon anodes in aluminium smelters.

Graphite electrodes industry is the second- largest CT Pitch consumer segment.

Impregnated CT Pitch is used in the manufacture of graphite electrodes, which is used in

EAF for production of steel.

Aluminium Industry

Aluminium industry across the globe is growing at faster pace. At present scenario,

aluminium production in the year 2013 was 50.1 Million tonnes and considered the progress

of installation plants in various countries, the total installed capacity of aluminium metal will

be around 66.8 Million Tonnes by the end of 2017. In India, present production capacity till

2013 was 1.90 Million tonnes per annum which will reach to the level of 3.9 million tones by

2017.

With increasing production capacities of Aluminium smelters, the demand of Coal Tar pitch(

binder grade) will grow because of the facts elaborated here under:-

Although India possesses world’s fifth largest bauxite reserves of over 3000 million tones,

it stands at the sixth position in terms of region- wise primary aluminium production in the

world as shown above.

For every tone(t) of aluminium metal production from Calcined alumina, there is a need for

around 0:100 t of Coal tar Pitch(Binder Grade).

2.6 Employment Generation (Direct and Indirect) Due to the Project

The manpower estimates have been made taking into consideration the following aspects:

a. The proposed organization structure, production processes involved, layout, equipment

with its degree of automation and mode of operation.



b. Additional manpower over and above the daily requirement at the rate of twenty-five

(25) per cent is provided to cater weekly off, holidays, leave, absenteeism etc. for

departments/sections working seven days a week.

c. The operation staff will be required to carry out routine checking of their own plant and

equipment as well as minor repairs and adjustments in addition to plant operation.

Moreover, during equipment shutdown for maintenance, the operation personnel will

assist the maintenance personnel in carrying out the maintenance tasks to maximize the

utilization of manpower.

d. The maintenance personnel will have multi-disciplinary skills; for example, mechanic

will be able to perform simple machining, welding and gas cutting. Implementation of

such concept will optimize the utilization of human resources and thereby will increase

labour productivity of the plant which, in turn, will reduce the cost of production.

e. Implementation of computer systems including local area network (LAN) with standard

user friendly software's in the field of financial management, human resource

management, personnel management, materials management, order scheduling,

sales and marketing management, management information systems (MIS),

production planning and control, maintenance and spares planning, etc. has been

considered to increase work efficiency and to reduce manpower requirement.

f. For security services, canteen and catering services, horticulture and landscaping

services, sanitary services, personnel transport, heavy maintenance and capital repairs,

plant civil maintenance, general cleaning and up-keep of the plant, loading and unloading

of materials, product handling, stores handling, and other miscellaneous semi-skilled and

unskilled job, appropriate external agencies will be employed under management

supervision.

Total manpower requirement

Based on the above, it is estimated that the manpower requirement for the proposed plant

will be about 25 persons. The details of manpower estimate for administration and works

departments are presented in Table 2.1.

Category-wise breakup of manpower



Category of personnel required in each job position for all departments is indicated in Table

2.1. The category-wise breakdown of manpower for administration and works departments

of the plant is given in Table 2.1.

Table 2.1 Category-Wise Breakup of Manpower

Sl.No.

Category Total

1 Manager 32 Supervisor 63 Skilled Workers 64 Semi-skilled

Workers10

TOTAL 25Training

It is presumed that the personnel in the administration departments having requisite

qualification and experience will be available from the local market and they do not normally

require any specific training. It is expected that their recruitment will be progressive

depending upon the requirement during the construction period and will be completed before

commissioning of the plant.

For works departments, most of the key positions in operation and maintenance of the

proposed plant at different categories will be manned by the qualified persons having

experience in the similar field in metallurgical industries and attitude to learn new

technologies. However, depending on the type of equipment/facilities along with the degree

of automation contemplated, the operation and maintenance personnel of the plant so

recruited will require specific need based training which is proposed to be carried out on-site

by the respective equipment supplier during equipment erection, start up and commissioning

of different plant units.



CHAPTER - 3

PROJECT DESCRIPTION


produce 84,000 MT per Annum Coal Tar Pitch & its by-products at Jammal Village, P.O-


3.1 Type of Project

The proposed project is envisaged to produce Coal Tar Pitch and its by-product from raw

Coal Tar through Horizontal distillation technology. Plant shall be based on Advanced

Process technology. The plant will also be equipped with the most efficient auxiliary sub

systems, material handling facilities and pollution control equipment.

3.2 Location & Accessibility

The proposed Project will be located at Jammal Village in Jharsuguda District of Odisha

State (Ref: Topo sheet No. 73C/1. The Latitude and Longitude of the proposed site 20° 50’

10.4”N and 84° 07’ 07.2”E respectively.

a. Road Connectivity

The site is well connected with road. NH – 200(Raipur- Chandikhol) is at distance of 1.53

km from the project site.

b. Rail Connectivity

The railway facility is also available near to the site. Nearest is Jharsuguda at a distance of 9

Km W direction from the project site.

c. Airport

Nearest airport is at Bhubaneswar, 248 Km from proposed project site in its SE side.

d. Sea Port




Fig 3.0 Plant Location







M/s Shobha Chemical Industries Private LimitedPre- Feasibility Report on Proposed Coal Tar distillation project to manufacture 84,000 MT/ Annum Coal tar Pitch and its By- productsAt- Village Jammal, P.O- Godigaon, Kolabira, Jharsuguda district, Odisha


Figure 3.1 TOPO Map



Figure 3.1 TOPO Map



Figure 3.1 TOPO Map



3.3 Site Selection

Based on following site selection, the site was selected to set up the proposed plant:

Proximity to the source of raw material.

Availability of water & power.

Availability of land, approach roads & accessibility.

Topography of land & geological aspects.

Nearness to rail head, transport logistics.

3.4 Size or Magnitude of Operation

Table 3.0 Production capacity of the company




3.5 Project Description

3.5.1 Process Description

The process of production involves charging various grades of Coaltar in pre

determined ratio from storage/charging tank and melting tank into the distillation vessel

and given heating charge through arrangement of submerged flue tube. After attaining

certain temperature, moisture content in the tar / various light aromatics and tar oil get

evaporated and is condensed and collected through an arrangement of bunch type

water cooled condenser. Extent of oil extracted depends on the softening point and

various specification of pitch as desired by customer as final product.

Major equipment for distillation is distillation and melting vessel of different size &

capacity as per requirement, fitted with column, condenser with cold water circulation

system and with provision for oil firing through burner (size 3A & 4A) the unit fitted with

air blower the minimum ratio of air and fuel oil of combustion is (600 CFM), through

seamless “U” size pipe which is spread on bottom of distillation vessel to generate heat to



inside materials for distillation and melting through the heat given by burner unit’s all

the distillation and melting vessels of both shed smoke exhort system connected to

main chimney (H-33m x B-Ø 3m x T-Ø 1m). Digital thermometers fit in all

distillation vessels, receiver & condenser for indicating temperature of boiling

range/cooling on a separate indicator penal board. “U” tubes fitted on top of all distillation

vessels which act as pressure relief value as salient safety features, Condensers are

water-cooled type of adequate capacity so that all types of vapors get condensed and

stored in separate mild steel receiver, like oil-water mixture, light oil, Heavy oil,

Anthracene oil. Firstly Coaltar & Hard pitch is melting on melting tank and after melting

on the semi liquid condition fed to the distillation vessel through vacuum unit. After a certain

temperature is attained in vessel, moisture & mild oil separated from Coaltar, then range of

firing is extended in stage, and above mentioned liquids come out and stored on separate

receivers made from mild steel. After minimum inside temperature attained as per quality

control parameters, then for gradation propose compressed air is fed to the vessel through air

tube fitted on the top of distillation vessel to extract extra oil to maintain the specific grade as

per customer. The gas exhaust from distill is stored on gas catcher made from mild steel

vertical tank and the gas condensed through oil, which acts as the interim distribution line

of pressure & gas. After extraction, the same semi liquid form of Coaltar pitch on same

temperature is sent to column and there it is given specific gradation by decrease of heat

and oil by several times through compressed air, and testing by quality control expert. At last

the desired liquid pitch is sent to dehydrator as finish product and loaded into insulated road

tanker and sent to the customer directly or to pitch cooling tray for cooling to prepare pitch

lumps. The essence of the process of production is heat treatment of charge in combination

with vacuum suction to achieve the best in various physical and chemical properties.

The right temperature and suction condition are determined depending on the product

specification.

Unit is also fitted with a brine chilling plant for cooling crystallization of suffixes and to

separate solids. For Crystallization of light oil, which is out on fractional at distillation of

coal tar on distill is push to Chilling plant crystallization tank from distill receiver, The



Chilling plant consists of compressor & Water cooler to maintain (100 °C) to separate

Naphthalene from light oil, after getting cooled Naphthalene becomes hard and then it

removed from tank and stored in the gunny bags to separate excess oil. On distill, it is again

charged and when mild temperature distillation begins, vapor formation start in condenser

and then cold water circulated on condenser to bring vapor to liquid form. The liquid

collected on open tank carefully & allowed to cool and hard. When the distilled naphthalene

gets hard, it is cut and bagged and again sent to hydraulic press for press and to release

excess oil. Steam coal, is used as solid fuel is a small boiler to generate steam for heating of

hydraulic press outer part cylinder to extract excess oil from distilled Naphthalene blocks.

Then the dry naphthalene blocks are broken in to lumps and packed in HDPE Bags as Finish

products. The extract oil from all process of naphthalene is treated as the final product

like light creosote oil of various grades. Process flow chart of route-I & route-II process

enclosed here with as annexure D/1 & D-2.

Fuel oil used in distill firing propose on all unit is stored in mild steel vertical tank

situated away from all distillation shed, Fuel oil used is non-dangerous “C” class petroleum

type.

For all Storage, Distillation, Cutting, Bagging, Hard press, Powder working area water

washing unit are provided with stirrer for emergency handling of staff.



Figure 3.2 Process Flow Diagram (Coal Tar Pitch)

Figure 3.3 Process Flow Diagram (Heavy Creosote Oil/ Anthracite Oil)



3.5.2 Infrastructure

The Main process area of the plant is divided in to two part Shed I & Shed II each shed

measuring area is (W-23M x L-40.0M x H-11.5M) 920 sqmt. On shed no. I of process unit is

proposed to install 5 distillation vessels each (2.50mØ x L-7m of charging capacity of 35

mts), 1- melting tank (2.50mØ x L-7m) having 50 mts capacity with condenser and swan

neck fitted, 1-Dehydrator (2.50mØ x L-7m)/ 1- Vertical Column (2.50mØ x L-7m)/ 1-

charging tank / 1- Vertical fuel tank (1.50mØ x H- 4.00m). On shed no. II of process unit is

proposed to install 4 distillation vessels each(2.50mØ x L-7m of charging capacity of

35 mts), with condenser and swan neck fitted, 1-Horizontal Dehydrator(2.50mØ x L-7m) /

1- Vertical Column(2.50mØ x L-7m) / 1- charging tank / 2 no’s - Naphthalene

distillation Vertical vessels (2.00mØ x H - 3.00m) / 4 no’s of M.S.Open Tank (L-5.0m x

W-1.5m x H-1.4m) with Equipment platform consisting of electric & Heat Control Panel /

Burner unit and controller / Common vacuum / blower and Compressor of suitable capacity

has been provided both of the distillation shed separately. Each process shed measuring area

(Length 40 meter x width 23 meter x height 11.5mtr). Two no’s of lento shed, each lento

shed measuring area (L-35mtr x W-8mtr x 5mtr) consist of independent 12 no’s of receiver

tank on Lento shed no.I and 8 no’s of receiver tank on Lento shed no., apart from that 2-

No’s of Oil-water tank (1.5mØ x L-5.0m) / 2 No’s of Gas catcher (1.5mØ x H- 5.0m),

with 1- Vertical fuel tank (1.50mØ x H- 4.00m) on each lento shed.

Apart from that Crystallization & chilling plant measuring area( L-35.0m x W-10.0m x

H-6.0m) 350sqmt consisting of 1- Brain Chilling Plant / 2 no’s of M.S. Insulated cooling

processing tank (L-5.0m x W-2.0m x H-1.0m) with insulated top cover & 11 no’s of open

M.S. Tank (L-5.0m x W-2.0m x H-1.0m) for storage. Press Machine & crystallization area is

(L-35m x W-10.0m x H- 6.0m) 350sqmt consist of 1-Baby boiler (1.0mØ x H-3.0m of M.S.

Plate) and 11 no’s of open M.S. Tank (L-5.0m x W-2.0m x H-1.0m) for storage purpose.

Pitch cooling tray and Pitch powder machine area (L-35.0m x W-10.0m) 350 sqmt

consist of Pitch powder machine & powder storage area (L-9.66m x W-9.64 x H-6.0m) under

cover shed and pitch cooling M.S.tray 4 no’s (L-25.0m x W-2.5m x H-0.3m) on



open separately. The Main Chimney of the plant (H-33.0m x Bottom Ø 3 mtr x Top Ø 1 mtr)

made from M.S. Plate with ladder support and platform on two stage.

3.5.3Details of plant and machinery

1. Distillation vessels and Columns and over head Tanks.

2. Receiver Tanks.

3. Crystallization Tanks.

4. Baby Boiler

5. Compressor Units

6. Burner Units

7. Vacuum Pump

8. Chilling Plants

9. Cooling Towers

10. Hydraulic press

11. Wash Units

12. Pulverizer Machines

13. Rotary Tablet Machines

14. Chimneys

15. Mettles and Dehydrators

16. Pumps, Motors and other supporting equipments

Others

1. Working / Processing Sheds

2. Laboratory Equipments

3. Weigh Bridge

4. Generator Sets

5. Fire Fighting Equipments

6. Storage Tanks

7. Open Tanks / Trays

8. Settler Tanks

9. Weighing Scales



3.5.4 Raw material Requirement

Table 3.1 raw material Requirement & Source

Sl. No. Particulars Quantity in TPA Source Mode oftransportation

1 Anthracene Oil 990 Open Market By Road2 Carbolic Oil 165 Open Market By Road3 Clear Tar 8250 Open Market By Road4 Coal Tar Wash Oil 165 Open Market By Road5 Coal Tar Fuel 1650 Open Market By Road6 Crude Coal Tar/coal 11550 Open Market By Road7 Crude Napthalene 360 Open Market By Road8 Crude Tar Acid 360 Open Market By Road9 Depitched Tar Acid 990 Open Market By Road

10 Dephenolised Coal Tar Oil 3960 Open Market By Road11 Drained Napthalene Oil 330 Open Market By Road12 Heavy Benzol 360 Open Market By Road13 Heavy & Light Creosote Oil 5400 Open Market By Road14 H.P.Napthalene 720 Open Market By Road15 Musk from Benzol 50 Open Market By Road16 Naptha Varius grade 360 Open Market By Road17 Napthalene various grade 3600 Open Market By Road18 Phenol Fraction 3000 Open Market By Road19 Pitch/Coaltar pitch various

grade18000 Open Market By Road

20 Pitch creosote Mix variousgrade

4200 Open Market By Road

21 Spent Solar Oil 350 Open Market By Road22 Still Bottom Oil 350 Open Market By Road23 Tar Pitch 18000 Open Market By Road24 Xylene 5 Open Market By Road25 N.G. tolune 6 Open Market By Road26 Benzene 120 Open Market By Road

3.6 Plant layout

The layout of the plant will be developed taking into following considerations:

Process departments will be consolidated into comprehensive production units requiring

short conveying distances;

The major utilities and service facilities will be centrally located in respect to points of

high consumption;

Sufficient space will be provided for ease of operation and maintenance;



The lengths of power cables will be minimized by suitably locating load distribution

centres in respect of process departments;

Outward movements of materials from customers/suppliers will be segregated from

internal plant traffic

Sufficient space for storage of raw materials and finished products.

Green belt will be provided.

Rainwater harvesting pond will be provided at lowest elevation to collect surface run-off

to maximum possible extent.

Adequate area will earmark for tailings and ash disposal.

Weigh Bridge and administrative block will be located at the entrance.



Figure 3.4 Plant Layout



3.7 Water & Power Requirement

3.7.1 Water Requirement

The total water requirement of proposed plant will be 0.68 m³/day. 0.2 m³/Day will be sourced from

existing bore well and 0.48 m³/Day will be sourced from Rain Water harvesting pond of total capacity

270 m³.

Table 3.2 Water Requirement & Source

Sl.No. Particular Quantity in m³/Day Source1 Domestic use 0.2 Bore well2 Cooling Process in Condensers 0.48 2,70 m³ capacity Rain Water

Harvesting PondTotal 0.68

Figure 3.5 Water balance

3.7.2 Power Requirement

Power requirement of proposed plant will be 250 KVA, which will be met from 11 KV H.T.

line from WESCO.

3.8 Pollution Control Measures

3.8.1 Air Environment – Mitigation Measures

The plant can cause air pollution due to the following activities:

Dust emission due to movement of vehicles carrying raw materials and finished products.

Dust emission due to finish product bagging system and handling in warehouse.







270 m³.







line from WESCO.












270 m³.







line from WESCO.








Particulate matter, CO₂, NOx, SO₂, PAH and VOC emission from pitch melting, pitch

storage tank, Non condensable from distillation operation, coal firing thermic fluid

heater.

Following Measures to mitigate air pollution causes:

Internal black topped roads shall be provided to minimize dust emission due to

movement of vehicles carrying raw materials.

CO₂, NOx, SO₂ emissions shall be controlled by roviding dust collector, bag filter and

chimney assembly.

3.8.2 Water Pollution

The plant cause can water pollution due to the following activities.

Waste water from the distillation plant due to distillation process.

Sewage generation due to domestic activities.

Following Measures shall be taken

Waste water of 100 m³/month generated due to process will be stored in storage tank and

will be treated in Effluent Treatment Plant and the treated water will be used for dust

suppression and green belt.

Sewage generated due to domestic activities provided with septic tank followed by soak

pit as per the condition stipulated in the SPCB, Odisha.

3.8.3 Solid Waste management

Proposed Plant will generate the following solid wastes from different production processes

and the respective management plans are mentioned against each heads.

Table 3.3 Solid Waste Generation and Management

Sl. No. Units Solid Wastes Qty In TPA Disposal practice1 Coal Tar distillation Plant Dust from APC devices 1.6 Reused in process

Table 3.4 Domestic Solid Wastes

Units Solid Wastes Qty In TPA Disposal practiceCanteen Garbage and food

waste02 Organic and inorganic portion of

waste will be separated, organic



waste will be vermin compostedand used for greenbeltdevelopment. Inorganic portion willbe given to scrap dealer.

Table 3.5 Hazardous waste

Hazardous Wastes Quantity Hazardous Wastes ManagementUsed Oil and Lube Oils 1.0 KL/Annum Reused as fuel oil

3.8.4 Noise Levels

The noise control will be done in four ways, namely by selecting low noise prone equipment

which would have led level below 75 dB (A) at 1 meter distance;

By selecting low noise generating equipment, which would have below 75 dBA at 1m

distance. This will be taken care at the equipment design stage.

By isolating the noise unit from the working personnel’s continuous exposure by

providing acoustic aids for plant personnel.

By administrative & safety measures, providing noise level monitoring, remedial

measures, providing noise safety appliances.

The noise impact on the surrounding environment during the construction phase will be

within acceptable limits. The operation of high noise generating equipment shall be

restricted during the night time.

Various measures proposed to reduce noise pollution include reduction of noise at source,

provision of acoustic lagging for the equipment and suction side silencers, selection of

low noise equipment and isolation of noisy equipment. The plant personnel in noisy area

will be provided with high noise reduction aid such as ear muffler & also the duration of

exposure of the personnel will be limited as per the norms.

Thick green belt development is planned for the attenuation of noise pollution and to

maintain ambient noise quality within the statutory limit.

3.8.5 Green belt development

A greenbelt development plan will be prepared and implemented along with the project.



The main objective of the greenbelt is to provide a barrier between the plant and the

surrounding areas. The greenbelt helps to capture the fugitive emissions and to attenuate the

noise generated in the plant apart from improving the aesthetics of the plant site.

The Greenbelt provided will be 33% (1.57 Ac) of total area 4.76 Ac and will have a suitable

density so as to mitigate the effects of emissions from the plant. The treated effluents from

the plants will be utilized for the greenbelt development.

The landscaping of the plant will be carried out. Roads for vehicular movement will be paved

and adequate mitigation measures will be provided to prevent fugitive emissions.

3.9 Schematic representations of the feasibility drawing which give information of eia

purpose.

Figure 3.6 Schematic Representation












purpose.













purpose.




CHAPTER-04

SITE ANALYSIS

4.1 General

The proposed site is located at Vill-Jammal in Jharsuguda district of Odisha. The site is at

about 9 km away from nearest town Jharsuguda. The national highway NH-200 is runs at

1.53 km from the site respectively. Nearest airport is at Bhubaneswar, 248 Km from

proposed project site in its Southern side.

4.2 Connectivity

a. Road Connectivity

The site is well connected with road. NH – 200(Raipur- Chandikhol) is at distance of 1.53

km from the project site.

b. Rail Connectivity

The railway facility is also available near to the site. Nearest railway station is

Jharsuguda at a distance of 9 Km W direction from the project site.

c. Airport

Nearest airport is at Bhubaneswar, 248 Km from proposed project site in its SE side.

d. Sea Port


4.3 Topography

The topography of the proposed land is generally flat and well suited for development of

industrial projects.

4.4 Existing Land Use Pattern

Land of the proposed project is devoid of any vegetation. Plant is not coming under the

dense forest category land. This area does not form part of any National Park, Wild Life

Sanctuary and Natural/Biosphere reserve.

4.5 Existing infrastructure

Land

Total land requirement for the proposed unit is about 4.76 acres.



Utilities

A. Power

Power requirement of proposed plant will be 250 KVA, which will be met from 11 KV H.T. line from

WESCO.

B. Water

The total water requirement of proposed plant will be 0.68 m³/Day. 0.2 m³/Day will be sourced from


2,70,000 litre.

C. Transport

The site is well connected with road. NH – 200(Raipur- Chandikhol) is at distance of

1.53 km from the project site. The railway facility is also available near to the site. Nearest

railway station is Jharsuguda at a distance of 9 Km W direction from the project site.

4.6 Climate Data

The climate of the Jharsuguda district is characterized by hot summer with low humidity.

During the summer maximum temperature is 48.0 °C. The temperature in the month of

December is lowest i.e. 7 °C. The average annual rainfall is 1527 mm.



CHAPTER – 05

PLANNING BRIEF

5.1 Planning Concept


produce 84,000 MT per Annum Coal Tar Pitch & its bi-products at Jammal Village, P.O-


As the nearest railhead is within 10 kms and NH-200 is within 10km from the site, the

transportation of both raw material as well as product will depend on the roads and rail. As

the site is almost at the confluence of two major national highways, road transportation will

not cause much problem. Existing road connection from the plant site to the NH will be

utilized for material transportation.

Plant should be provided with following facilities:

Transportation facility shall be provided to the executives.

An ambulance shall be provided for the emergency.

Qualified doctor shall be engaged for the regular health check up.

Drinking water and electricity facilities shall be provided.

Greenbelt shall be developed in and around the plant.

Canteen shall be provided with all facilities.

Separate sanitary facilities shall be provided.

5.2 Population Projection

With the set up of proposed project infrastructure and social development will

simultaneously takes place. Project will contribute for raising the population of the locality

as it creates job opportunities and economic upliftment of the area. The company is providing

employment 25 persons during the operation period of the proposed project Plant activities

will also boost the ancillary industries, business and market establishments. The whole set

will invite both skilled and unskilled from outside. This will result in increase in the

population density due to industry.

5.3 Land use planning

Following is the break-up of the land use of the project site/area:



Table 5.0 Land use break-up

Sl. No. Description Area in acre1. Plant Built-up 1.432. Auxiliary facilities 0.183. Admn. Building, Offices, Lab, Canteen & First

Aid 0.054. Roads 0.705. Solid waste Disposal Area 0.236. Raw material & Product Storage Yard 0.377. Water Storage & Rain water harvesting pond 0.238. Greenbelt 1.57

Total 4.765.4 Amenities & Facilities

To render the necessary repair & maintenance, inventory, quality control related and

administrative services for the proposed plant with slime and associated facilities, following

auxiliary facilities have been considered inside the plant boundary.

Repair and maintenance shop: It is proposed to set up a local repair shop equipped with

facilities for machining, fabrication, assembly, electrical repairs, instrument

calibration/repair etc. A mobile crane of 5 ton capacity will also be provided for dismantling

and mounting of component assemblies and sub-assemblies of equipment.

Stores: A single-bay building will keep equipment spares, hardware, wearing parts and

consumables. A strong room for keeping valuable item, offices for inventory control,

material receipt section, toilet etc will be suitably provided.

Plant office: An office building will be constructed inside plant premises. The office

building will be complete with separate toilet, conference rooms, computer room, separate

executive's room and other facilities like record maintenance, printing, scanning etc.

Ancillary buildings: Besides the auxiliary facilities other ancillary buildings with necessary

facilities such as canteen, time office & security offices etc. will also be provided.

Canteen: A canteen building will be set up near the plant office and a suitable external

agency is proposed to be engaged to service snacks and refreshments to the workers,

supervisory and office staff working in the different plants/facilities and other working area.



CHAPTER – 06PROPOSED INFRASTRUCTURE

6.1 Industrial Area

The setting up of the Main Plant Facilities, Raw Material Storage, Raw Water Storage

Reservoir & Treatment, Auxilliary facilities, viz. Admn. Bldg., Tech. Bldg, Workshop, QC

Lab, Switch Yard, etc. & Green belt (33%) required 1.57 Acres land. Company will use

nearest road and rail facility for goods transportation and equipped with all other required

facilities.

6.2 Residential Area

The area around the site is under development with reasonably good communication

facilities.

Around 25 people will be engaged in the plant and Jharsuguda town is very close to the

project site and the area around the site is under development with reasonably good

communication facilities. Other social infrastructure like housing, schooling and medical

facilities has been developed and in some area it is underdeveloped. Hence, no residential

colony/township is envisaged for employees.

6.3 Green Belt

A greenbelt development plan will be prepared and implemented along with the project.

Total green belt area shall be 33% (1.57 Ac) of total area (i.e.4.76 Ac). The main objective of

the greenbelt is to provide a barrier between the plant and the surrounding areas.

Comprehensive greenbelt/plantation program will be undertaken in and around the

project. The species selection will depend upon crown shape, surface of bark and leaves,

flower, color, capacity of growth in the wide variations of ecological conditions etc. A

mixture of soil should be prepared by mixing commercial fertilizer, cow dung, BHC powder

in the topsoil.

6.4 Social Infrastructure

SCIPL will commence a lot of infrastructure developmental works in the periphery area.

Some glimpses of the developmental activities are presented below:



Improving and building road network in the adjoining villages.

Strengthening School buildings with playgrounds.

Social awareness programme will further improve by the local authority such as

sanitation and hygiene, HIV Prevention Program.

Through this project, adult education and female education will be provided to the

illiterate adults and backward females of the villages in the project surrounding area.

The proposed project will set up training centre or tie up with Industrial Technical

Institutes to educate local youth as skilled labour.

6.5 Connectivity

The site is well connected with road. NH – 200(Raipur- Chandikhol) is at distance of

1.53 km from the project site. The railway facility is also available near to the site. Nearest

railway station is Jharsuguda at a distance of 9 Km W direction from the project site.

6.6 Drinking Water Management

Drinking water facilities will be provided for employees.

6.7 Sewerage System

A garland drain around the plant is envisaged to collect surface run-off during rainy

season. Separate Internal drainage system will be constructed to collect domestic and

industrial effluent. A common basin will be constructed for the treatment of effluents the

plant. Sludge from settling tank will be used as manure for greenbelt development.

6.8 Run-Off Management

The rain water collected from the roof of buildings will be channelized through drains

around the buildings and will be recharged into the ground by providing recharging pits.

Overflow, if any, will be discharged to the nearby plant drainage. Also one rain water

collection pond has been considered in the layout. All the plant storm water drains will be

routed to the rain water collection pond and overflow, if any, from the pond will be

discharged to any existing natural outfall outside the plant area. The rain water collection

pond will be unlined.



A Rain Water Harvesting Pond has been contemplated to act as collection basin for

rainwater. The collected water will be 100% reused in the raw water reservoir in dry season.

The pond will be located at the lowest area of the plant so that it can effectively collect all the

rainwater by gravity. The Tank shall be earthen. The pond will be lined at the bottom and

sides with two layers of HDPE lining of appropriate thickness to prevent percolation of the

harvested rainwater in to the ground. Figure below depicts schematically the proposed

rainwater harvesting scheme for the proposed plant. The Rain Water Harvesting Pond is

depicted below:

Garland drain will be provided around raw material stock pile area. The run-off collected

from these areas will be treated in adequate settling pond and will be taken to rain water

harvesting pond.

Suitable pump house will be installed adjacent to the rain water collection pond so that

the settled water from the collection pond can be pumped and supplied to the plant for

meeting some of the daily requirement.

6.9 Industrial Waste Management

Hazardous Wastes

Majority of the wastes (spend oils) will be preferably sold to the potential users with

necessary authorization for reprocess/reuse.



6.10 Solid Waste ManagementThe solid wastes include dust from plant. Dust from plant will be recycled and reused in theprocess.

Table 6.0 Solid Waste Generation and ManagementSl. No. Units Solid Wastes Qty In TPA Disposal practice1 Coal Tar distillation Plant Dust from APC devices 1.6 Reused in process

6.11 Power Requirement & Supply/SourcePower requirement of proposed plant will be 250 KVA, which will be met from 11 KV H.T.

line from WESCO.



CHAPTER – 07

REHABILITATION AND RESETTLEMENT (R & R) PLAN

7.1 Policy to Be Adopted For R & R Plan w.r.t Project

The proposed project is going to come up on 4.76 acres area. Total land has already been

acquired. There is no existence of displaced habitants in the area. Land is also devoid of any

vegetation.

Local people will be engaged for construction and operation activities and the local area

have all the infrastructure facilities. Jharsuguda Town is just 9 Km away from the site and is

well connected with NH-200, thus, no housing colony/township is envisaged.



CHAPTER – 08

PROJECT SCHEDULE & COST ESTIMATES

8.1 Project Schedule

In this industry, any one of the following three alternate modes of project execution is

adopted:

Turnkey

Semi Turnkey

Packaged procurement mode

Planning Of Activities

Careful planning of all the activities is one of the pre-requisite for timely completion of the

project. Following activities will be given special attention.

Pre Project Activities

Management Approvals.

Selection of location

Land acquisitions

Statutory Clearances

Financial Approvals and Tie ups.

Selection of Consultants

Conceptual Design

Preparation of main machinery tender

Evaluation of tenders

Project Activities (Implementation Stage)

Firm up basic design

Main Machinery Order placement

Detailed engineering of the project

Statutory approvals of Building Plans.

Preparation of Tender, Evaluation of tenders received and Order placement for balance

machinery



Completion of procurement activities on time

Release of civil drawing for civil construction

Civil construction

Supply of mechanical & electrical equipment

Inspection of major machinery at supplier’s works

Erection of all plant & machinery

Commissioning of the plant

Statutory Clearances

SCIPL has already obtained Consent to Establish from SPCB, Odisha vide letter

no3044/III-CON(NOC) dtd24.08.2013 and accordingly construction has been done. Other

Clearances required for the proposed project shall be identified in due course and necessary

action will be taken to obtain the same.

Project Schedule

The schedule has been developed on the basis of the estimated quantum of work,

expected delivery and installation periods of plant and equipment and the need to

commission the plant facilities in the shortest possible time. The schedule envisages a total

project implementation period of 18 months from the date of 'Go-ahead'. Schedule

commissioning of the plant can only be achieved if construction, delivery and erection

periods as shown in the bar chart can be met by respective suppliers and contractors.

The 'Go-ahead' date for the project implementation has been considered as a date of 'Go-

ahead' given to the Consulting Engineers for detailed engineering. The schedule has been

prepared based on the assumption that the following activities will be completed prior to the

date of 'Go-ahead'.

i. Freezing of adequate project details to enable preparatory site activities to commence on '

Go-ahead',

ii. Finalizing the arrangement for requisite finance as per projections matching with

implementation schedule,

iii. Acquiring all relevant statutory Govt. clearance (environmental, forest, rehab illation etc)



Strategies for Timely Execution of the Project

The following strategies would be adopted for smooth functioning as well as timely

execution of the project:

The task of implementing the project in time shall be achieved by ensuring a well

coordinated project implementation task force in-house and from external agencies

A well chosen team of experienced personnel for project execution shall coordinate the

implementation of the project from in-house

Experienced engineering consultants with proven track records shall be selected for

detailed engineering of the project.

Reputed and experienced contractors with adequate resources of finance, men, material

and tools and tackles, will be engaged for execution of the construction and erection

work.

Effective project monitoring including project planning schedule and monitoring shall be

employed in this project. Timely execution and resources will be monitored using

computer based project monitoring tools. In case of deviations in project progress, all

possible corrective actions such as crashing of network etc. will be carried out.

8.2 Project Cost

An indicative estimated capital cost of the proposed Plant is Rs. 398.00 Lakhs, including

the pre-operative expenses, contingency and interest during construction.

A broad break-up of the indicative estimate of the Project capital cost is provided below:

Table 8.0 Project Cost Break-Up

Sl. No. Particulars Amount in Lakhs1 Land & Land Development Cost 8.002 Building & Boundary 20.003 Plant and machinery 310.004 Plant & Equipments 110.005 Electrical Equipment 10.006 Storage tanks 50.00

TOTAL 398.00



CHAPTER – 09

ANALYSIS OF PROPOSAL

9.1 Financial and Social Benefits

M/s Shobha Chemical Industries Pvt. Ltd. intends to set up Coal tar distillation plant to produce

84,000 MT per Annum Coal Tar Pitch & its by-products at Jammal Village, P.O- Gadigaon, Kolabira

,Jharsuguda District of Odisha State. The proposed project is envisaged to produce Coal Tar Pitch and its

bi-product from raw Coal Tar through Horizontal distillation technology. Plant shall be based on

Advanced Process technology. The plant will also be equipped with the most efficient auxiliary sub

systems, material handling facilities and pollution control equipment. It will cater the increasing demand

coal tar pitch in aluminum and steel industries.

Besides there will be immense social benefits of the project, to the backward region.

9.1.1 Improvements in the Physical Infrastructure

SCIPL has envisaged a lot of infrastructure developmental works in the periphery area.

Improving and building road network in the adjoining villages.

Strengthening School buildings with playgrounds.

Providing the Drinking Water Facilities.

9.1.2 Improvements in the Social Infrastructure

Employment, direct and indirect for the local predominantly tribal people.

Social awareness programme will further improve by the local authority such as

sanitation and hygiene, health, immunization etc.

Through this project, adult education and female education will be provided to the

illiterate adults and backward females of the villages in the project surrounding area.

Sponsor education to Poor Students of the Proposed Area.

The proposed project will set up training centre or tie up with Industrial Technical

Institutes to educate local youth as skilled labour.

Provide & conduct the Free Eye & Health Check up Programmes.



9.1.3 Employment

It is estimated that the total requirement of manpower for the whole organization will be 25.

There will be much larger indirect employment in transport, ancillary, support facilities and growth in

local trades and business.

9.2 Other Benefits

Development of the local area in terms of an enlarged market.

Besides above, indirect benefits shall also occur to the region by way of increase in industrial

production.

Thus, the proposed project will usher in the social and economic upliftment of the persons living in

the vicinity of the Project i.e. of society at large.

Visiontek Consultancy Services Pvt. Ltd(An Enviro Engineering Consulting Cell)

Plot No.-108, District Centre, Chandrasekharpur, Bhubaneswar-16, Tel.: 91-2744594, 3250790, Fax : 91-6742744594E-mail : [email protected], [email protected], Visit us at : www.vcspl.org

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