Pre Feasibility Report

For

PRODUCTION OF ACID SLURRY (LABSA 100%)

At

Plot No.70, Village-Kajipalasiya (khudel)

Tehsil-Indore, Dist.- Indore (M.P.)

Proposed By

M/s Bhaskar Venkatesh Products Pvt. Ltd. (Unit-II)

Indore (M.P.)

1. Identification of project and project proponent

The Proposed Acid Slurry (LABSA 100%) project is proposed within the existing Premises Detergent unit

with capacity of 9000 TPA and By product Spent Acid 7500TPA at, Village-Kajipalasiya Tehsil-Indore Dist.-

Indore (MP). The project is proposed by M/s Bhaskar Venkatesh Products Pvt. Ltd. which is occupied by Shri

Akash Goyel having 15 years experience in business and industry. He is also Managing Director of the

Company.

BHASKAR VENKATESH PRODUCTS PVT. LTD. is a joint venture company of DAINIK BHASKAR GROUP and

ANANT GROUP.

BHASKAR VENKATESH - a customer-focused company, dedicated to produce enriched quality products and

services to the customers that meet their essential needs. The company is committed in better value to its

consumers by offering them the quality products and services at affordable prices.

BHASKAR VENKATESH PRODUCTS PVT. LTD came into existence on 12th May 2006 and entered into edible

SALT market with the brand name BHASKAR. During its expansion period, we have launched the FMCG items

i.e. ATTA and DETERGENT under the brand name of TAN MAN.

2. Brief Description of Nature of The Project

The Proposed Acid Slurry (LABSA 100%) project is proposed within the existing Premises Detergent Unit

area. 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 100%) 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 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 fulfill 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 150 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 (Labsa 100%) Manufacturing Unit

2. Location of the Project

District/ State Taluka Village Khasra no.

Indore( MP) Indore Kajipalasia (Khudel) 32 (New-70)

The area lies at the cross section of longitude 76 deg. 01’ 30.12” E East & Latitude 22 deg. 41’ 11.93” N North and Topo sheet No-55 B/2. The area is fully developed and all infrastructure facilities including Transportation, communication, proximity to market etc. conductive to growth of an industry are abundantly available.

Site Address Village-Kajipalasiya, Tehsil-Indore,Dist.-Indore (M.P.)

Production Capacity Linear Alkaline Sulfonic Acid(LABSA)-9000 MTPA Spent Acid(By Product)- 7500 MTPA

Cost of Project 17 Crore

Raw Material Requirement Linear Alkaline benzene (LAB)-6000 MTPA Sulphuric Acid(H2SO4)-9000 MTPA Water -1500 MTPA

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

Net fresh Water Requirement The water requirement for proposed unit will be 04 KLD and total requirement for existing and proposed unit will be 12 KLD, whereas domestic requirement will be about 15 KLD. The water is/will be supplied by the tankers.

Power Requirement 350 HP

Capital Cost for Environmental measures ( proposed )

15 Lacs

Proposed area for plantation 18426 Sq.mt.

Existing area of plantation 1535 Sq.mt.

Alternative Source of Power DG set of 100 KVA

Land acquired The Total land area available with the unit is 37452.1 sq.mt. Out of that 9254 sq.mt. Land is required for the proposed LABSA plant.

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

Nearest Highway Nemawar Road (NH-59) -0.14 km

Nearest Railway Station Indore- 17 km

Nearest Airport Indore -23 km

Nearest Forest/ Sanctuary/Eco- sensitive zone.

No Such Areas within 10 km raidus

22°41'12.86"N - 76°01'31.79"E 22°41'9.96"N - 76°01'32.79"E 22°41'8.82"N - 76°01'28.63"E 22°41'11.91"N - 76°01'27.43"E

Proposed Unit Layout Plan

The features of the layout are as follows: Process plants will be consolidated into comprehensive production unit requiring short conveying distances

and lengths of gas ducts; Sufficient space will be provided for ease of operation and maintenance; The lengths of power cables will be minimized by suitably locating load distribution centers in respect of process departments; toward movements of materials from customers/suppliers will be segregated from internal plant traffic; and Safety requirements will be kept in mind while locating the workshops and vehicular movement inside the plant.

3. Details of alternate site:

Detergent Plant has already been established at same plot. Proposed LABSA Plant is interlinked with Existing unit. Hence No alternative sites are considered as the proposed activities.

4. Size or magnitude of operation: The proposed capacity of the plant is 9000 TPA.

5. Project description with process details: List of Product (MT/Month) S.No.

Product

Quantity, MT/Month Existing Product Addition Total After proposed

Addition 1. Detergent Powder

(Non EC Product) 6000 - 6000

2. Detergent cake (Non EC product)

3000 - 3000

3. LABSA (EC Product) - 750 750 4. By Product(Spent Acid) - 625 625

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

Product -1: Detergent Powder (Existing Product)-

For Manufacturing of the Detergent powder it is required to mix soda ash, Dolomite powder, vacuum salt,

SIPP, and Perfume in standard proposition and simultaneously required to add/mix acid slurry in standard

propitiation. Therefore color and water solution to be mixed fro decorating the product which further

required the process of dry, grind and filtration through fine mesh net. After all process of dry, grind and

filtration through fine mesh net. After all process it result in to finished product in loose form. Lastly loose

finished product is to be weighed, filled and packed in polythene bag of 1 kg, 500 gms and 250 gms etc .and it

is also to be packed in 50 kg.25 Kg. Jute/Polythene bags for transportation purpose.

Product-2: Detergent Powder (Existing Product)-

Soda ash, China clay, soap stone, Acid Slurry, Calcide, STPP, Starch, Lime stone and other minerals and items

will be added in standard proportion along with water this mix will be kept in mixer for half an hour therefore

by machine cakes will be available for sale.

Product-3: Proposed Product Addition of LABSA-

For manufacturing lf LABSA first of all Lab(Linear Alkyl Benzene) will be pumped from its storage tank to

dosing tank in which we can measure to required quantity and then after measuring the required quantity it

will be dropped into stirrer and after it we will pump H2SO4 (Sulphuric Acid)into dosing tank to measure its

quantity after measuring it we will drop it in the stirrer which is already mixing LAB, we will mix it for nearly

3-4 hours after completion of mixing we will add little amount of water and the whole batch will be drop in

the separator.

We will allow to separate it for 4-5 hours resulted the bottom part would be of spent Acid9By product) and

the upper part as LABSA (slurry)then both liquids will be transferred to their individual storage tank.

Brief Description Proposed Product LABSA-

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 transferred 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 Block diagram for manufacture of LABSA (100%)-

MASS BALANCE OF LINEAR ALKYL BENZENE SULPHONIC ACID (LABSA)

Raw material Qty. Mt.(300 Days) % stage

Input

Linear Alkaline benzene(LAB) 6000 36.36

Sulphuric Acid (H2SO4) 9000 54.55

Water 1500 9.09

16500 100

Output

Linear Alkyl Benzene Sulphonice Acid 9000 54.55

Spent Acid 7500 45.45

16500 100

Storage Tank Capacity Tank quantity

Reactor (6500 kgs) each with suitable Gearbox and motor 4 no.

Settler(6500 kgs each) 4 no.

Dosing Tank(3500 kgs each) 4 no.

Slurry Storage tank(50 mt each) 3 no.

Lab storage tank(100 mt each) 2 no.

Acid Storage tank(50 mt each) 2 no.

Spent storage tank(50 mt each) 2 no.

Pumps(for transfer of material we are using below given pumps)

Slurry 2 no. (1Gear pump + 1 spare )

LAB 2 no. (1monoblock + 1 spare)

Acid 2 no. (1 SS seal pump + 1 spare)

Spent Acid 2 no.( 1 PP seal pump + 1 Spare)

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.

Plant & machineries-

Plant & Machineries Cake And Powder

Dump Hopper, STP, ETP, Dust Collector, Load Cell, weighing machine, level sensor, various valves, Transfer

pumps, Motors, Gear Box, Hoist, Gear Motor, MS Structure, SS Structure, MS Pipe line, SS Pipe line, SS Sheets,

Mixers, Screening Machines, Vertical Packing Machine, Horizontal Packing Machine, Pouch Sealing Machine,

Tub Detergent Cake Mixer, Roll Mill, Extruder Machine, Cake Cutting Machine, Rotary Cutter, Pneumatic bar

cutter, Pneumatic Cutter, Auto Stamper, Bin Activators, Dump Hoppers, conveyors, Elevators, Transfer

conveyors, Cartooning Machine, Dyes, Multi screw mill, cage mill, Crutches, Big MS / SS Tubs, Kadav, Multi

Discharge, ETP, Laboratory Accessories and Equipments, Ink Jet Printer, Printing Machines, Offset Machines,

ROTO Gravure, Sleeting machine, Pouching machine, Various Sealing machine, tape machine, VFD, electrical

panel, transformer, compressor, DG set, cables, wires, other electrical accessories and equipment, welding

transformers, leth machines, drill machines, grinders, pulveriser, Machine, Wrapping Machine, Stamping

Machine, cylinders, workshop accessories and equipment, sewing machine, various belts, chains, coupling,

pulley, nuts and bolts, washer, welding rod, hand sewing machine, Grinder, Flour mill etc.

Plant & Machineries Labsa Plant

Stirrer Vessel, M.S. Settler, Storage Tanks, Reactor, Load Cell, weighing machine, level sensor, various valves,

Transfer pumps, Motors, Gear Box, Hoist, Gear Motor, MS Structure, SS Structure, MS Pipe line, SS Pipe line, SS

Sheets

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.

List of Raw material-

Soda, Alluminium sulphate, Bleaching powder, magnesium, L.A.B., China Clay, Coco, Diaethinol amide,

SCMC,T.S.P.,T.C.C.,Conditior,C.P.A.B.,S.L.E.S.,Silica,E.G.M.S.,S.M.P.,E.D.T.A.,SulphuricAcid,AminoAside,Flaim,Pro

tin,Hydro lysate, Olium,Acid slury, Ficldspar powder, filtrocin, A.O.S. potine, S.T.P.P., Sodium chloride, Lauric

Acid, Sodium salphates, Dolomite, Parafide, calcite, Citric Acid, calcium carbonate, Caustic, Urea, Zeolire,

optical brightner, perfume, Precipitated Silica, Sodium Silicate, Enzyme, Lime, Starch, Tale powder, Soap

Stone, global salt, common salt, magnesium carbonate, colour, polymers, Optical brightness etc.

Packing Materials-

Polythen Bags, Plastic Bory, cartoons, thread, wrapper, Plastic rope, Gum, tape, laminates, corrogaiced box, etc.

List of Raw materials for Proposed Product-

Sr.No. Name of Raw Material Consumption Per Month

1. Linear Alkyl Benzene 500 MT

2. Sulphuric Acid 100 % 750 MT

3. Water 125 Lit

• 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

500MT TANKERS By Road M/s Reliance Industries M/s TIPL M/s IOCL

M/s IPCL

2. Sulphuric Acid (100%)

750 MT TANKERS By Road

3. Water 125 Liter Tank Through Pipe line

Water Tankers

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. Solvents used during the manufacturing process if

Detergent Powder, Detergent cake process are water and Sulphuric Acid. Water and acid are completely used

up during the manufacturing process of Detergent cake and powder. By product spent acid sell to nearest SSP

unit

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 The water requirement for proposed unit will be 04 KLD and total requirement for existing and proposed unit will be 12 KLD, whereas domestic requirement will be about 15 KLD. The water is/will be supplied by the tankers Item Water Consumption In KLD Waste Water Generation In KLD Detergent Unit LABSA Unit Detergent Unit LABSA Unit Process 1 Nil Nil Nil Boiler Nil Nil Nil Nil Cooling Tower 2 1 Nil Nil Industrial 5 3 Nil Total 08 04 12 Domestic 15 Nil 12 Nil • Power Requirements and its source:

Sr. No.

Particulars

Proposed

Source

1 Power Electricity requirement 560 kVA 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:

The proposed project would be based on Zero Effluent Discharge. The sludge from the water treatment plant

is dried and sent to TSDF. Spent oil will be sold to authorized venders. Biodegradable food waste will be given

to Municipal collection point and recyclable plastic waste will be disposed through authorized vender.

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 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/Authorized vendor.

No waste water is generated in the plant operation. Only domestic waste water is generated. Treatment plant

for domestic waste water has already been installed. Details are as follows :

The Process of Treatment Primary Treatment (before COMPACT)

In primary treatment, floating and suspended solids are settled and removed from Sewage. Following this,

discharge from the sewers enters a screen/bar rack to remove large, floating material such as rags and sticks.

Secondary Treatment

This is the next level treatment where the bacteria in Sewage are used for further purification of the Sewage.

It’s a biological process that removes about 85% or more of the organic matter in Sewage compared with

primary treatment, where the purification level is about 50%. These processes are variations of what is called

the "Activated Sludge" process, which provide a mechanism for bacteria, with air added for oxygen, to come

in contact with the wastewater to purify it.

In the activated sludge process, flow from the sewer goes into the reactor, where compressed air is mixed

with sludge in the presence of synthetic media on which the purifying organisms grow and contact the

wastewater, removing contaminants in the process. The activated sludge allows bacteria to feed on the "food"

provided by the new wastewater in the reactor, thus purifying it.

The flow, along with excess organisms that build up on the media during the purification, then goes to a

secondary clarifier. Air flows up through the media in the filters, to provide necessary oxygen for the bacteria

organisms. Clarified effluent flows to the receiving water, typically a river or bog, after disinfection. Excess

sludge is produced by the process and after collection from the bottom of the secondary clarifiers it is

dewatered, sometimes after mixing with primary sludge, for use as fertilizer, disposed of in a landfill, or

incinerated.

Tertiary Treatment

Advanced level of water treatment is called tertiary treatment of water - where heavy metals, toxic chemicals

and other pollutants are removed from wastewater to an altering degree. The tertiary treatment methods

include microfiltration, carbon adsorption, evaporation/distillation, and chemical precipitation.

Raw Water Parameters (Inlet) Assume

S.No.

Parameters

Value

Unit

1 Colour Light Brown 2 pH 6-9 3 T.S.S. 1200 mg/l 4 B.O.D.(3 Days 21 C) 450 mg/l 5 C.O.D. 800 mg/l

Product Water Parameters (Outlet) S.No.

Parameters

Value

Unit

1 Colour Colorless 2 pH 6-9 3 T.S.S. 10 mg/l 4 B.O.D.(3 Days 21 C) 10 mg/l 5 C.O.D. 50 mg/l

Components Involved

Components Description Units Make

Bio Reactor Twin Chambered with SAFF media and Fine Bubble Diffusion Grid

1 No. EEPL

Clarifier Slanted Chamber with Tube Pac media and appropriate launder.

1 No. EEPL

Feed Pump sludge Pump to feed the system with incoming sewage

1W+1S Kriloskar/Crompton

Air Blower Twin/Tri Lobe blower with complete accessories to aerate the reactor

1W+1S Airvac/SGNDI

Treated Water

Pump

Mono block Pump to feed the Polishing Unit, i.e. DMF and ACF

1W+1S Kriloskar/Crompton

Recycling Sludge

Pump

Sludge Pump to recycle the system with incoming sludge

1 No. Kriloskar/Crompton

Dual Media Filter Pressure Vessels with multilayered filtering media

1 No. Aventura

Activated Carbon Filter

Pressure Vessels with multilayered filtering media with Activated Carbon

1 No. Aventura

Electric Panel With starters, level controller switches and required digital meters

1 No. Shivam Controls/

L&T

Filter Press Plates 18, Size– 18’x 18” with filter Press Pump

1 No.

Make-Sahil Filter

UV Size – 36W x 2 Nos. 2 No. Alfa

Steps Involved in the Treatment of Sewage

Bar Screen-The floating objects which may arise choking in the pumps and other machineries are barred

from entering the plant as the sewage is passed through the MS/SS grill fixed in the Bar Screen Chamber.

Equalization Tank-As the original flow of the sewage may vary time to time, the Equalization tank stores the

influent as to avoid shock load and help the plant to operate while in low flow condition.

Sewage Lifting Pump-The sewage is transferred from Equalization Tank to the Aeration Tank through

Submersible pumps for a controlled flow. Using Submersible avoid choking as they have an excellent solid

handling capacity.

Aeration Tank-The aeration process takes place in Biological Reactors which convert the finely divided and

dissolved organic matter in wastewater into flocculent settle able solids. The sewage is mixed with air round

the clock to build up necessary environment within the reactor. The sewage flows by gravity to the adjoining

Settling tanks.

Fixed Media-To enhance the contact surface area for proper oxidation FUDISED AEROBIC BIO REACTOR

(FAB) is inserted in the aeration tank. These are optimally designed made by continuous forming to achieve

high surface area for given volume and offer minimum resistance to airflow, providing more air contacts less

power consumption.

Diffusers-The Equalization and the Aeration tanks are equipped with non clog diffusers to transfer diffused

air. This allows maximum oxygen transfer having the Oxygen Transfer Efficiency up to about 3%-6%.

Root Air Blowers-These are Positive Displacement Blowers. They have higher efficiency at moderate

compression ratio and provide constant flow rates at varying discharge pressures in Equalization ns Aeration

Tanks.

Settling Tank-It minimizes the flow and the carrying capacity of sewage and thus the flowing organic matters

settles down here. To achieve proper MLSS growth in the aeration tank the settled

Tube Settler Media-The most efficient sedimentation systems have high settling surface area whilst

maintaining a small structure. The Tube settler media provides a large settling surface area within the

specified volume thus giving high flow rates. They have a chevron shaped self-supporting structure in a

tubular form with six sides.

Sludge Transfer Pumps-These are Centrifugal pumps efficient in handling sludge. These transfer sludge from

the clarifier’s hopper to the Sludge Holding tank and the Aeration tank as recirculation.

Clear Water Tank-The clear overflow from the clarifier is collected in a sump and either used for gardening

or disposed off in the drain after proper chlorination which disinfects treated sewage.

Filter Feed Pump-These are high pressure Centrifugal Pumps that pusses the clear water in the sand filter

and adsorption vessels.

Dual Media filter-These are pressure vessels with multi layered filtering media. Here the suspended solid

from the water is filtered.

Activated Carbon Filter-The Activated Carbon filled vessel removes the color and the odor of the water. So

that it can be reused for washing, flushing and etc.

Electrical Panel-The starters of all the Electrical equipments are connected to a single panel to facilitate the

operator in handling the process. Additionally, it have energy meter, level switches and flow totalizer.

4.0 Site Analysis: i. Connectivity

Location : Kajipalasiya (Khudel)

Place : Indore

District : Indore(M.P.)

S. No.

Particulars Details

1 Co-ordinate 22°41'12.86"N - 76°01'31.79"E 22°41'9.96"N - 76°01'32.79"E 22°41'8.82"N - 76°01'28.63"E 22°41'11.91"N - 76°01'27.43"E

2 Height above mean sea level 552 mRL

3 Nearest Town Indore -17 km

4 Nearest Railway Station/Town Indore -17 km

5 Nearest Airport Indore – 23 km

6 Nearest Highway/Road Nemawar Road (NH-59) – 0.14 km -N

7 Hills/Valley None

8 Ecological Sensitive Zone None

9 Reserve Forest Renuka RF- 5.46 km Rambhawar RF-6.40 km Ralamandal Sanctury-11 km

10 Nearest Village Khudel– 0.20 km- E Kajipalasia -0.30 km - S

11 Nearest River/ Nalla Jaljaiwanti Nadi – 0.47 km

12 Surrounding Features North : Namawar road (NH-59) South : Open Land East : Open land West : Open Land

ii. Land Form, Land use and Land Ownership

Project Proponent is procured 9254 Sq.mt of land for the proposed project which is in possession and

diverted for industrial purposes.

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.

Land use Break-Up for Proposed unit

Particulars Total Area (Sq.mt.)

Total Land Area 37452.1

Shed Area 5400

Slurry plant area 732

Office area 2600

Toilet 50

Labour 472

Land Required for Proposed Unit 9254

Open Space 1 Area 18,426

Open Space 2 Area 1490

Open Space 3 Area 45

Open Space 4 Area 1,000

Total 22,556 Sq.mt. (60.2%)

v. Existing Infrastructure

We have not started any activity pertaining to proposed project. Land is converted into Industrial use. The

total land area available with the unit is 10 acre out of that 3.0 acre land is required for the proposed

Detergent plant. Naational Highway is passing at 0.14 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 1st

March to 31st

March, 2017

Date

Temperature OC Relative Humidity

% Morning (8.00)

Evening (17.00) Cloudiness

%

Max Avg Mi

n Max Avg Min

Wind

Directi

on

Wind

Speed

km/h

Wind

Directi

on

Wind

Speed

km/h

Mor. Eve.

1 32 24 16 68 40 17 E 4 N 9 0 2

2 33 24 15 52 36 19 ESE 5 NNE 5 0 3

3 35 26 18 65 38 19 SSE 4 N 7 5 2

4 36 27 18 52 36 18 S 5 NW 8 4 5

5 34 28 21 55 36 18 S 6 W 7 4 5

6 29 24 19 74 58 35 NE 10 ESE 2 10 50

7 32 25 18 76 59 33 SSW 6 WSW

7 16 14

8 33 26 18 83 53 16 SW 5 NNW 7 9 13

9 33 26 19 78 50 25 NNE 6 NNW 6 6 46

10 34 26 19 71 39 19 NE 6 NW 8 6 27

11 36 27 18 55 34 15 SE 4 WNW 5 0 7

12 26 23 20 75 57 44 SSE 7 NNW 15 3 9

13 25 22 19 85 72 60 ESE 7 S 13 30 25

14 29 23 17 94 72 45 SSE 9 WNW 7 8 66

15 30 24 17 87 58 25 ENE 8 NNW 6 6 50

16 31 23 15 77 38 8 NNW 8 NW 10 0 0

17 33 24 15 50 27 12 NW 2 NNW 8 6 5

18 36 28 19 47 33 18 S 11 WNW 12 7 9

19 36 28 20 57 38 20 ESE 2 NE 6 22 8

20 36 28 20 56 34 13 SW 6 WNW 11 3 0

21 35 27 19 55 31 15 NNW 7 NW 14 0 0

22 33 26 18 44 25 13 NW 13 WNW 14 0 0

23 34 24 15 37 25 13 NW 12 NW 9 0 0

24 36 26 16 48 27 12 WSW 2 NNW 8 0 0

25 38 28 18 48 29 14 SSW 4 N 7 1 5

26 39 29 19 46 29 16 S 8 NNE 6 41 16

27 27 24 21 82 53 38 NNE 7 NW 8 5 48

28 35 26 18 86 53 29 W 1 NW 10 0 2

29 36 28 19 64 39 20 NE 1 NW 12 1 2

30 37 28 19 51 34 22 NE 2 NW 11 5 11

31 38 28 19 43 26 15 SSE 6 NE 10 13 0

METEOROLOGICAL DATA FOR MONTH OF 1st April to 30th April, 2017

Date

Temperature OC Relative

Humidity % Morning (8.00)

Evening (17.00) Cloudiness

%

Max Avg Min Max Avg Mi

n

Wind

Directio

n

Wind

Speed

km/h

Wind

Directio

n

Wind

Speed

km/h

Mor. Eve.

1 40 30 21 39 27 13 WNW 6 NNW 11 2 0

2 40 30 21 34 20 6 S 3 NNW 11 3 0

3 41 32 23 40 25 7 SSW 6 NNW 11 2 19

4 42 33 24 40 20 7 SSW 4 NW 11 4 3

5 40 32 25 36 19 6 NW 9 WNW 14 2 8

6 39 32 25 29 18 7 WNW 5 WNW 13 7 6

7 38 30 23 28 20 9 ENE 5 WNW 13 10 16

8 40 32 24 32 19 10 SW 8 WNW 13 4 3

9 40 32 24 37 20 9 SSW 3 W 15 3 6

10 41 32 24 33 20 8 N 3 W 15 3 0

11 41 32 24 29 18 8 W 9 WNW 16 4 0

12 38 31 24 32 24 14 NNW 15 WNW 19 3 2

13 38 30 22 34 23 14 NW 14 WNW 16 0 0

14 40 31 22 30 23 14 W 4 WNW 12 0 0

15 42 32 23 36 26 17 NW 12 NW 12 0 0

16 44 34 24 39 25 6 WNW 7 WNW 12 33 16

17 41 34 27 35 28 24 WNW 15 W 15 27 22

18 41 32 24 37 31 27 NW 16 W 15 15 39

19 43 34 25 38 30 23 WSW 9 WNW 13 3 21

20 42 34 26 33 30 27 W 11 WNW 17 4 24

21 41 34 26 34 26 14 NW 17 WNW 19 3 0

22 42 33 24 24 13 4 W 13 W 15 6 6

23 40 34 28 14 10 6 WNW 21 WNW 20 0 0

24 40 32 23 23 14 7 NNW 3 NW 12 0 0

25 40 31 22 27 16 10 ENE 7 N 7 0 0

26 41 34 26 23 16 10 E 3 NNW 5 22 46

27 40 32 25 27 20 13 WNW 4 W 14 3 45

28 42 34 25 30 17 10 SSW 4 NW 13 7 17

29 44 34 25 29 16 8 N 5 NW 12 0 15

30 43 34 25 23 14 7 ENE 6 NNW 10 13 26

METEOROLOGICAL DATA FOR MONTH OF 1st May to 31st May, 2017

Temperature OC Relative Humidity

% Morning (8.00)

Evening (17.00) Cloudiness %

Date

Max Avg Min Max Avg Min Wind

Dir.

Wind

Speed

km/h

Wind

Dir.

Wind

Speed

km/h

Mor. Eve.

1 42 33 24 5 23 13 NW 9 NNW 12 0 0

2 45 34 24 5 20 12 SW 10 NNW 11 0 16

3 43 36 27 10 56 21 W 13 WNW 10 44 21

4 41 33 25 10 65 27 SSW 11 WNW 9 6 0

5 40 34 27 14 39 24 WSW 2 W 7 7 45

6 38 32 25 15 50 34 SW 17 WSW 7 2 74

7 38 30 23 11 56 33 WSW 6 NW 4 17 15

8 40 32 24 10 50 28 WSW 9 WNW 6 5 4

9 40 34 27 15 34 24 SSW 11 SW 3 4 3

10 40 34 28 12 33 23 WSW 9 N 7 9 5

11 42 34 27 15 34 25 W 12 N 8 13 7

12 42 36 29 11 47 24 SW 8 WNW 7 4 3

13 44 35 26 12 51 25 WSW 5 N 13 3 2

14 45 36 28 5 40 20 WSW 9 NW 11 0 2

15 45 37 29 11 38 21 SW 2 NNW 11 0 4

16 44 36 28 13 46 24 WSW 6 SSW 9 10 15

17 45 38 30 11 25 17 NNW 15 NNW 7 44 2

18 44 36 29 6 32 17 SW 16 N 10 0 0

19 43 36 29 12 36 23 S 17 ESE 4 0 2

20 42 36 30 18 54 32 SSW 13 SE 6 0 6

21 44 36 29 14 47 30 SSW 12 NNW 14 0 2

22 43 36 28 16 85 35 WNW 26 W 14 0 18

23 42 36 28 14 56 35 WNW 24 NNW 11 2 4

24 39 31 23 18 74 41 WNW 14 NNW 23 6 13

25 38 31 24 12 57 37 WNW 17 WSW 7 5 10

26 39 30 22 19 84 47 WNW 22 WNW 17 5 7

27 40 34 28 16 49 30 WNW 19 NW 11 3 17

28 41 34 28 16 46 31 NW 18 WSW 17 8 7

29 39 32 24 17 54 37 WNW 19 NW 13 7 5

30 38 32 27 16 47 31 WNW 4 NNW 10 45 66

31 41 34 27 15 49 30 SSW 5 NW 5 3 4S

viii. Social Infrastructure available

Social infrastructure like community center, hospital and electricity is available in Khudal village as well as in Indore Dist.

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 Indore dist. the entire facility 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 National Highway In NH-59 Nemawar Road.

vi Drinking water management

Drinking water has been supplied through bore well with proper RO system.

vii Sewerage System

Septic tanks and soak pit system shall be provided for treatment of domestic waste water.

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

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.

The Total Cost of Project(Amount in Lacs)

Sr. No. Purpose Proposed Cost (Lacs)

1. Land 200.00

2. Civil Construction 660.00

3. P & M Slurry Plant 100.00 4. P & M Cake Plant 350.00

5. P & M Powder Plant 250.00

6. Electrical Installation 100.00

7. Miscellaneous expenses 40.00

TOTAL : 1700.00/-

Means Of Finance (Amount In lacs)

Sr. No. Purpose Proposed Cost (Lacs)

1. Promoters Contribution 425.00

2. Term Loan 1275.00

TOTAL : 1700.00/-

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.