Pre Feasibility Report

For

Produce ACID SLURRY (LABSA 90%)

At

Plot No.176, AKVN Industrial Area

Meghnagar, Dist.- Jhabua (M.P.)

Proposed By

Madhya Bharat Phosphate Private Limited

(Unit III) Meghnagar, Jhabua(M.P.)

1. Identification of project and project proponent

The Proposed Acid Slurry (LABSA 90%) project is proposed within the existing SSP unit with capacity

of 40 TPD at Meghanagar Industrial Area, Meghanagar Dist Jhabua (MP). The project is proposed by

Madhya Bharat Phosphate pvt limited which is governed by Shri Pawan Agrawal aged 39 years is

Commerce Graduate having 18 years of experience in business and industry. He is also a director in M/s

API India BioTech (p) Limited which is engaged in the manufacture of NPK.

2. Brief Description of Nature of The Project

The Proposed Acid Slurry (LABSA 90%) project is Inter linked with Existing GSIP/SSP Unit. The

proposed new project involves the production of “Acid Slurry” which are Synthetic Organic Chemicals,

for the proposed project, the company intends to procure the available latest technology for

manufacturing the proposed products.

The industrial sector in the past years has seen a drastic boom and also the keeping in mind the

globalization trend, we have identified the demand for the proposed products and with continuous R&D

found that it can be developed in-house and produce commercially for domestic market as well as an

eye more on export markets.

As per the EIA notification- 2006 as amended the proposed project involves the production of “Acid

Slurry” which falls under item no. “5(f) - Synthetics organic Chemicals industries” hence requires Prior

Environmental Clearance.

This project profile in detail foresees setting up of unit to produce ACID SLURRY (LABSA 90%) LABSA has

been the major surfactant used in detergents for more than thirty five years and continues to represent a

substantial portion of the surfactants market today. Supporting this history of safe usage is a large archive

of environmental research that has been conducted on LABSA. This environmental research, performed by

top environmental scientists and research agencies, has investigated virtually every part of the

environment that could have been exposed to LABSA. The studies have repeatedly proven LABSA's

environmental acceptability and safety. Because of LABSA's environmental safety, cleaning effectiveness

and cost competitiveness, LABSA has experienced 45 years of ever-increasing use around the world.

Linear alkyl benzene (LAB), the material used to produce LABSA, is derived exclusively from petroleum bi-

products--benzene and paraffin derived from kerosene. LAB currently represents one-third of the active

ingredients in detergents worldwide.

Linear alkyl benzene is the raw material used to manufacture linear alkyl benzene sulfonate (LABSA), an

active ingredient in the formulation of detergents. LABSA eliminates dirt by its physicochemical mechanism

and it is one of the surfactants most widely used in liquid cleaners and in powder. LABSA has been used for

more than 45 years in the manufacture of detergents and it is known for its excellent quality/price ratio.

3. Need for the project and its importance to the country and or region

The proposed new project will provide a potential growth opportunity for the company. We identified

the demand for the proposed products and it can be produce commercially for domestic market as

well as an eye more on export markets. Its export and also increase the foreign revenue. The products

are now well established and acceptable in the international markets.

4. Demand –Supply gap

The products have very high demand in Synthetic Detergent Industry and other chemical industries. The

proposed new of unit will to some extent help to meet this consumption indigenously fulfil the demand

supply gap

5. Imports vs. Indigenous production

Proposed products manufacturing in the country will be very much economical compare to Imports of

the same.

6. Export possibility

There is a huge demand of the proposed products in the export market. Our products are widely used and

are in demand in the Synthetic Detergent Industry and other chemical industries etc.

7. Employment generation (direct and indirect) due to the project

During operation skilled, semi-skilled and un-skilled labours approximately 20 numbers will be required

for operation etc.

Indirect employment-

Driver, cleaner for loader & dumper, loading and unloading points where labours are required

8 Project description

1. Types of project: Acid Slurry Manufacturing Unit

2. Location of the Project

District/ State Taluka Village Khasra no.

Jhabua ( MP) Meghnagar Meghnagar Industrial Area Plot No. 176

The area lies at the cross section of longitude 81 deg. 11’ 47” E East & Latitude 24 deg. 11’ 41” N North.

Site Address Plot no.176, AKVN Industrial Area, Meghnagar, Jhabua(M.P.)

Production Capacity Acid Slurry(LABSA 90%)- 12480 MTPA

Cost of Project 2.70 Crore

Raw Material Requirement Linear alkyl benzene - 8100 MTPA Sulphuric acid 98% - 12180 MTPA

Fuel Diesel: 12Lit/Hr for one D.G. Set For Capacity of 100 KVA

Net fresh Water Requirement Water Consumption: 33.00 KL/day (Domestic –05KL/Day, Industrial- 23.00 KL/Day, and Gardening- 5 KL/Day). This will be sourced from AKVN water supply. No waste water is generated in the plant operation. All the water is recycled back in to the process. Only domestic waste water is generated

Power Requirement 25 KW

Capital Cost for Environmental measures ( proposed )

5 Lacs

Proposed area for plantation 751 Sq. mt

Existing area of plantation 10653 Sq.mt

Alternative Source of Power DG set of 100 KVA

Land acquired Total 3592 Sq.mt inclusive of area for new proposal

Land required for plant and building 2840.5 sq.mt

Solid /Hazardous waste Generation No solid waste Generation in our process.

Nearest Highway Meghnagar- Ujjain -0.3 km

Nearest Railway Station Meghnagar- 10 km

Nearest Airport Indore -90 km

Nearest Forest/ Sanctuary/Eco- sensitive zone.

No Such Areas envisages in study area

22°55'.12.04"N - 74°33'45.65"E 22°55'.08.22"N - 74°33'48.05"E

Proposed Unit Layout Plan

3. Details of alternate site: Plant is exiting and running with valid EC and consent to operate.

4. Size or magnitude of operation: The proposed capacity of the plant is 40 mT per day.

5. Project description with process details:

The overall process is shown on the attached Block Flow Diagram, and Process Flow Diagrams.

Raw material consumption per tones of 89+/- 1% acid slurry is Linear alkyl benzene 670-690 kg,

Sulphonating agent 98% Sulphuric acid 1050 +/100kg. LABSA is anionic surfactant with molecules

characterized by a hydrophobic and a hydrophilic group. Alpha-olefin sulfonates (AOS) alkyl sulfates (AS)

are also examples of commercial anionic surfactants. They are nonvolatile compounds produced by

sulfonation.

LABSA is a complex mixtures of homologues of different alkyl chain lengths (C10 to C13 or C14) and phenyl

positional isomers of 2 to 5-phenyl in proportions dictated by the starting materials and reaction

conditions, each containing an aromatic ring sulfonated at the Para position and attached to a linear alkyl

chain at any position with the exception of terminal one (1-phenyl).

The properties of LABSA differ in physical and chemical properties according to the alkyl chain length,

resulting in formulations for various applications in laundry and home care products.

The starting material LAB (linear alkyl benzene) is produced by the alkylation of benzene with n-paraffins

in the presence of hydrogen fluoride (HF) or aluminium chloride (AlCl3) as a catalyst, the latest is DETAL

process by UOP. LABSA is produced by the sulfonation of LAB with sulphuric acid in batch reactors.

Other sulfonation alternative reagents are oleum, diluted sulfur trioxide, chlorosulfonic acid and sulfamic

acid on falling film reactors.

Surfactants are widely used in the industry needed to improve contact between polar and non-polar media

such as between oil and water or between water and minerals.

Linear alkylbenzene sulfonic acid is mainly used to produce household detergents including laundry

powders, laundry liquids, dishwashing liquids and other household cleaners as well as in numerous

industrial applications like as a coupling agent and as an emulsifier for agricultural herbicides and in

emulsion polymerization.

Because they are stable, sulfonic acids can be isolated, stored and shipped as an article of commerce. SO3

is an aggressive electrophilic reagent that rapidly reacts with any organic compound containing an electron

donor group.

Sulfonation is a difficult reaction to perform on an industrial scale because the reaction is rapid and highly

exothermic; releasing approximately 380 kJ/kg SO3 (800 BTUs per pound of SO3) reacted.

Most organic compounds form a black char on contact with pure SO3 due to the rapid reaction and heat

evolution. Additionally, the reactants increase in viscosity between 15 and 300 times as they are converted

from the organic feedstock to the sulfonic acid.This large increase in viscosity makes heat removal difficult.

The high viscosity of the formed products reduces the heat transfer coefficient from the reaction

mass. Effective cooling of the reaction mass is essential because high temperatures promote side reactions

that produce undesirable by-products. Also, precise control of the molar ratio of SO3 to organic is essential

because any excess SO3, due to its reactive nature, contributes to side reactions and by-product formation.

Therefore, commercial scale sulfonation reactions require special equipment and instrumentation that

allows tight control of the mole ratio of SO3 to organic and rapid removal of the heat of reaction.

Sulfuric acid (H2SO4) is widely used as sulfonating agent. It is an equilibrium process, as water is formed

in the reaction and the resultant water dilutes the sulfuric acid. The sulfonation reaction stops when the

sulfuric acid concentration drops to approximately 80%. This process has the dual advantage of low SO3

cost and low capital equipment cost as compared to the gas sulphonation route. However, it has the

disadvantage of being an equilibrium process which leaves large quantities of un-reacted sulfuric acid. This

waste acid must be separated from the reaction mixture and subsequently used in manufacture of SSP and

other fertilizers.

Sulfuric acid can be used to sulfonate aromatics and alcohols in either batch or continuous

equipment. For detergent alkylates, the batch equipment is used which is a Reactor, with a provision for

and cooling to remove the heat of reaction and maintain suitable temperature during the reaction.The

detergent alkylate is first added to the reaction vessel then the Sulphuric acid is slowly added over a period

time.The reaction is highly exothermic and the acid addition rate is determined by the ability to remove the

heat of reaction.The temperature should be maintained below 65°C for optimum product quality.

Frequently the heat of reaction is removed by pumping the reaction mixture through an external heat

exchanger.Because it is an equilibrium reaction, except for the special case of azeotropic sulfonation of

hydrotropes with sulfuric acid, a large surplus of sulfuric acid forms. When the sulfonation reaction is

complete,the sulfuric acid may be separated from the sulfonated detergent alkylate by adding water. The

water addition (typically about 6 to 8% by weight of the reaction mixture) causes a phase separation to

occur between the sulfonic acid and the diluted sulfuric acid called spent acid.

The separation usually takes place in a separate, lined vessel and occurs over a period of about for 1/2

hour.After separation, the sulfonic acid is transfered in to a storage tank from which material is dispatched.

Material is sold either in lorry tankers or in HDPE barrels. An automatic barrel filling machine is used to

make sure that correct weight of material is filled in to each barrel. Road tankers are weighed in

weighbridges before dispatch. Spent acid is likewise transferred to a separate storage tank to be used in

manufacture of SSP .

Process flow diagram for manufacture of LABSA (90%)-

SSP

• INFRASTRUCTURE, MACHINERIES, EQUIPMENT & TECHNOLOGIES

Installation of the plants and machineries and latest technology will be required to manufacturing the

products. To get the best results in terms of quality and quantity, the company will invests in the latest

available plant and machinery and leverages state-of-the-art technologies to get excellent results.

• MANUFACTURING PROCESS

The company shall use the latest available process technology for the production. This section includes the

manufacturing process of the product, chemical reactions, and mass balance of each product.

6. Raw material required along with estimated quantity, likely source, marketing area of final

product/s, mode of transport of raw Material and finished product:

Detailed raw material requirement along with estimated quantity, likely source, marketing are of final

products mode of transport of raw material and finish production.

Manufacture

of SSP

Product-wise list of Raw materials

Sr.No.

Name of Raw Material Consumption MT per month

1. Linear Alkyl Benzene 675

2. Sulphuric Acid 98 % 1015

• Transport of Raw material:

Sr.No Name of Raw Material

Consumption per month

Means of Storage

Mode of Transport

Source of Supply

1. Linear Alkyl Benzene

675 MT TANKERS By Road M/s Reliance Industries M/s TIPL M/s IOCL

M/s IPCL

2. Sulphuric Acid (98%)

1015 MT TANKERS By Road

7. Resource optimization/ recycling and reuse envisaged in the project, if any, should briefly outline:

The raw materials shall be stored in the storage tank. By adoption continuous improvement in technology

and process the reduction in process waste generation will be achieved by proper and efficient handling of

raw materials, wastages of raw materials will be reduced. The spent acid is used in the manufacture of SSP.

8. Availability of water its source, Energy/power requirement and source should be given:

Availability of water its source, Energy/power required and its source.

• Water Requirement

Sr. No.

Particulars

Quantity (KL per day)

1 Domestic 05

2 Gardening 05

3 Industrial 23

Grand Total 33

Source: Fresh water requirement will be catered from AKVN water supply

dept.

• Power Requirements and its source:

Sr. No.

Particulars

Proposed

Source

1 Power – Electricity requirement

25 KW MPEB

2. Power - During power failure 100 KVA D.G. Set

Quantity of waste to be generated (liquid and solid) and scheme for their

Management/disposal:

Domestic effluent passes through septic tank/soak pit of adequate capacity. There will no Industrial

liquid or solid waste generation

Utility Emission & Control Measures:

Sr. No.

Particulars

Fuel / Power & it’s Qty

Probable Pollutants & Limits

Control Measures

1.

D.G. Set 1no. (Capacity:100 KVA)

HSD: 12 Lit/hr PM<150 mg/Nm3 SO2<100 ppm

NO2<50 ppm

Stack Height:7 Dia: 0.10

• Quantity of Solid Waste generation and its management:

Types of Waste & Category

Source of Generation

Quantity (Proposed)

Storage Method

Method of Disposal

Used oil (5.1) D. G. SET 0.020 MT (per annum)

Stored in drum Collection, Storage, Re-use as lubrication of pumps and Gear Box.

4.0 Site Analysis: i. Connectivity

Location : Meghnagar

Place : Meghnagar

District : Jhabua (M.P.)

S. No. Particulars Details

1 Co-ordinate 22°55'12.04"N- 74°33'45.65"E

2 Height above mean sea level 312 mRL

3 Nearest Town Meghnagar -10 km

4 Nearest Railway Station/Town Meghnagar -10 km

5 Nearest Airport Indore – 90 km

6 Nearest Highway/Road Meghnagar- Ujjain – 0.3 km

7 Hills/Valley None

8 Ecological Sensitive Zone None

9 Reserve Forest None

10 Nearest Village Agaral – 4 km

11 Nearest River/ Nalla River Anas - 5 km

12 Surrounding Features North : Thandla-Meghnagar main road South : Land of unit -2

East : Campus of unit -2 West : API India Biotech Pvt.Ltd.

ii. Land Form, Land use and Land Ownership

Project Proponent is procured 3592 Sq.mt of land for the proposed project which is in possession

and diverted for industrial purposes. The unit is proposed to be located within industrial area.

iii. Topography

Topography of the area is almost plain.

iv. Existing Land use pattern

The land use of the project area is pertaining to industrial activity only. Out of project area is

predominantly being used or agricultural purposes.

Land use Break-Up for Proposed unit

Particulars Total Area (Sq.mt.)

Land Required for Proposed Unit 3592

Electric unit area 146

Panel room area 92.71

Office area 80

Store room 160

Workshop area 248

Loading and unloading area 680

Main plant area 296

Greenery area 751.50

Toilet unit area 31.39

v. Existing Infrastructure

The required infrastructure is already in place as proposed site is in operation. State Highway is

passing at 0.3 km from the industry.

vi. Soil Classification

The soils in the area are generally of sedimentary type soil.

vii. Climate data from Secondary Source:

METEOROLOGICAL DATA FOR MONTH OF OCT- 2016

Date

Temperature OC Relative Humidity

%

Morning 8.00 AM

Evening 5.00

PM

Cloudiness

Octas

Max Avg Min Max Avg Min

Wind

Dir.

Wind

Speed

Wind

Dir.

Wind

Speed

Mor Eve.

15 35 27 19 50 31 16 ENE 9 NNE 15 0 2

16 34 28 21 45 31 18 E 14 NE 13 0 2

17 35 26 18 44 31 17 ESE 9 ESE 3 1 2

18 36 28 19 55 33 12 NNW 6 NW 4 1 1

19 34 28 21 57 36 18 W 3 W 5 1 1

20 35 28 20 58 32 16 NW 11 WNW 6 1 2

21 33 28 22 53 37 22 N 9 NNE 7 2 1

22 34 27 20 52 36 18 NNW 7 W 12 2 1

23 34 26 19 57 34 16 NNW 4 W 6 1 0

24 35 26 18 40 30 14 N 7 SW 9 1 1

25 34 26 18 55 40 22 ENE 4 SSW 12 4 5

26 28 24 19 83 64 44 SSW 1 S 9 4 0

27 28 24 19 77 57 38 E 6 S 2 2 3

28 31 24 17 75 56 31 NE 6 WNW 9 1 5

29 28 22 15 78 60 22 NNE 18 N 12 0 0

30 27 21 15 82 57 33 ENE 19 NNE 15 0 0

31 27 21 15 77 47 6 ENE 19 SE 8 0 1

1 29 23 17 71 57 47 E 18 SE 5 1 1

2 30 24 17 73 51 33 ENE 14 SSE 10 1 1

3 32 24 17 66 47 28 NE 18 SE 8 1 5

4 33 26 19 68 45 22 ESE 7 SSE 5 1 5

5 33 26 18 62 42 19 SSE 5 S 5 4 6

6 32 24 17 53 39 22 NNE 8 SSW 8 2 2

7 32 24 16 62 40 21 NNE 8 SSW 6 0 4

8 32 25 18 62 41 22 E 7 N 2 4 4

9 31 24 17 63 47 26 E 13 ESE 9 0 5

10 32 24 17 66 46 26 ESE 7 NE 5 1 4

11 31 24 18 68 46 25 E 6 E 5 5 15

12 31 24 17 66 44 21 ENE 10 SE 1 5 3

13 31 24 17 71 43 20 ENE 6 N 4 4 3

14 32 24 16 62 42 19 E 5 NE 3 0 0

METEOROLOGICAL DATA FOR MONTH OF NOV- 2016

Date

Temperature OC Relative Humidity

% Morning

8.00AM

Evening 5.00

PM

Cloudiness

Octas

Max Avg Min Max Avg Min

Wind

Dirt

Wind

Speed

Wind

Dirt

Wind

Speed

Mor Eve.

15 34 26 17 68 42 16 NNE 14 SSW 3 4 4

16 32 24 16 61 40 20 NNE 7 S 6 0 0

17 31 24 16 64 38 22 NNE 12 NNE 9 0 0

18 29 22 16 60 37 20 ENE 19 E 9 0 0

19 28 22 15 69 36 20 ENE 16 ENE 9 0 0

20 29 22 15 55 38 23 ENE 15 ESE 8 0 0

21 30 22 13 61 36 19 ENE 11 SSE 7 0 1

22 29 22 16 73 42 27 E 11 SSW 3 4 1

23 29 24 20 52 41 30 ENE 8 S 5 4 1

24 29 24 19 56 46 28 ENE 9 S 8 3 3

25 29 24 18 61 36 4 ENE 15 ESE 6 1 1

26 33 24 15 66 41 17 E 10 SSW 10 0 2

27 29 23 17 71 44 25 NNE 14 WSW 9 1 1

28 23 20 16 50 35 22 NE 12 SSW 8 1 1

29 30 23 16 57 39 28 E 12 SSW 3 2 2

30 32 25 18 68 49 27 SE 11 SE 5 2 1

1 32 24 17 74 48 26 SE 7 S 7 1 2

2 30 23 16 72 56 33 NE 7 W 2 1 6

3 26 20 15 67 49 27 NE 15 NNW 1 6 1

4 28 20 12 75 45 19 ENE 10 SE 3 0 0

5 29 20 11 67 43 19 ENE 9 SSE 5 0 0

6 31 21 11 56 39 11 ENE 9 SSE 7 0 0

7 29 20 11 76 41 15 E 7 S 8 0 0

8 31 22 12 68 39 13 E 8 SSE 8 0 0

9 30 22 13 64 42 17 ESE 10 SW 9 0 1

10 30 22 14 68 41 21 SE 7 SW 11 1 1

11 26 20 15 67 48 28 NNW 9 W 11 1 1

12 24 16 9 59 42 25 NNE 14 NNE 2 0 0

13 24 16 8 68 44 25 NE 12 N 4 0 0

14 23 16 9 70 48 27 NE 17 NNE 12 0 0

METEOROLOGICAL DATA FOR MONTH OF DEC - 2016

Date

Temperature OC Relative Humidity

% Morning

8.00AM

Evening

5.00PM

Cloudiness

Octas

Max Avg Min Max Avg Min

Wind

Dirt

Wind

Speed

Wind

Dirt

Wind

Speed

Mor Eve.

15 22 14 7 70 39 20 NE 14 E 7 0 0

16 25 17 9 73 43 18 ENE 8 SW 7 2 0

17 24 16 9 70 46 17 NNE 4 NNW 13 2 0

18 22 15 8 68 40 17 NE 16 NE 12 2 0

19 28 18 8 67 38 17 ENE 17 SSE 6 0 0

20 27 19 11 66 45 31 ESE 6 WSW 10 0 0

21 23 15 9 72 46 26 NE 12 NE 4 0 0

22 23 16 8 74 49 25 ENE 15 E 2 0 0

23 22 14 7 72 45 21 NE 12 NNW 7 0 0

24 21 14 7 63 42 19 NE 17 NNE 14 0 0

25 20 14 7 76 45 19 NE 14 NE 10 0 0

26 23 15 7 77 39 15 E 12 ESE 4 2 2

27 27 18 8 52 31 13 ENE 10 E 7 0 0

28 29 20 11 68 35 9 ENE 8 SE 4 0 0

29 31 22 12 58 36 14 ENE 6 ESE 2 0 2

30 33 23 13 66 38 11 ESE 5 S 9 0 0

31 31 22 14 63 39 17 ENE 8 SSW 7 0 2

1 29 20 12 73 43 19 E 6 WSW 8 0 0

2 27 18 10 60 43 23 NE 7 N 7 0 0

3 27 19 11 84 49 23 ENE 10 SE 4 0 0

4 29 20 11 73 42 15 E 8 SSE 8 0 0

5 30 21 12 80 46 17 E 5 SSW 9 0 0

6 29 21 13 59 40 20 ESE 2 SW 9 0 0

7 29 21 13 73 45 20 NNE 9 SSW 9 0 0

8 28 20 12 60 44 25 NNE 6 WNW 8 0 0

9 27 19 11 71 51 27 NE 9 W 5 0 0

10 28 20 11 69 42 13 E 8 WSW 8 0 0

11 29 20 12 68 43 18 E 8 SW 7 0 0

12 29 20 12 68 43 16 E 7 SW 7 0 0

13 27 20 12 72 48 23 N 10 SW 10 0 0

14 28 20 13 62 44 23 ENE 10 WSW 10 0 0

viii. Social Infrastructure available

Social infrastructure like community center, hospital and electricity is available in Meghnagar as well as in Jhabua.

5.0 Planning Brief:

i. Planning Concept :

There is a cluster of numerous large-scale, medium-scale and small-scale industries, engaged in

manufacture of variety of products in the Madhya Pradesh Audyogik Kendra Vikas Nigam, (MPAKVN)

notified area of Meghnagar. AKVN notified industrial area of Meghnagar has the entire available

infrastructure like water, electricity, roads, rail, and transportation, availability of raw material, CETP, TSDF

Site and drainage system.

Population Projection:

The project is small in magnitude. No influx of population is expected as labour shall be deployed from the

local villages.

iii Land use planning

As above

Amenities / facilities

First aid facility has already been provided at site.

The area shall not being used at all by general public.

A rest shelter is there for workers.

Guards during day & night has already been deputed at site to prevent unauthorized entry.

In case of natural hazards such as earthquake we will take assistance from the local competent

authority of Govt.

ii Residential area (Non Processing area)

As the local people from nearby villages shall be engaged in project activity. Therefore no housing /

building is proposed.

iv Social Infrastructure

Company shall evaluate the need base program under CSR and shall execute as per the given plan.

v Connectivity

Site is well connected with by State Highway In Meghnagar-Ujaain road .

vi Drinking water management

Drinking water will be supplied through bore well with proper RO system.

vii Sewerage System

The domestic waste shall be taken to soak pit and septic tank.

6 Rehabilitation and Resettlement (R&R) Plan:

(i) Policy to be adopted (Central/ State) in respect of the project affected persons including

home oustees, land oustees and landless laborers (a brief outline to be given):

The proposed Industry does not envisage any disturbance to local community or the village since the land

is acquired and fully owned by AKVN the proposed new project will not affect the home oustees, land

oustees and landless laborers. Hence there is no R & R plan required.

8. Project Schedule & Cost Estimates:

(i) Likely date of start of construction and likely date of completion (Time schedule for the project

to be given):

After obtaining Environmental clearance and Consent to Establish from CPCB, the company shall start the

proposed construction and commissioning of the project.

(ii) Estimated project cost along with analysis in terms of economic viability of the project:

Estimated project cost along with the analysis in terms of economic viability of the project Plant &

Machinery, Pipeline & Fittings, Electrical Installation, Safety systems, etc. are the major heads considered

in the Capital Cost Projection for the proposed new project. Environment Protection has also been

considered in planning the Cost Projection, which will include Green belt development, safety systems,

etc.

Capital Cost Projection for Interlinked Unit

Sr. No. Purpose Proposed Cost

1. Plant & Machinery 2,00,00,000/-

2. Building and Civil Works 55,00,000/-

3. Utilities and off sites, roads, storages etc

15,00,000/-

TOTAL : 2,70,00,000/-

The proposed investment will be made by company only. The company will provide budgetary provision

for the recurring expenses for environmental issues while planning the allocation of funds during the

annual budgetary planning.

9.0 Analysis of Proposal (Final Recommendation)

Financial and social benefits with special emphasis on the benefit to the Local people including

tribal population, if any, in the area.

From the foregoing analysis, it is observed that proposal is environmental compatible and will helps to

people improving their financial status, performance and repayment capability. This also helps the

company in venturing into production of niche specialty products which will eventually better their profits

and also their ranking in the industry. CSR Programme shall be executed through the group discussion and

need base Programme will be proposed for the area, by which people of the area will be benefitted.