For Proposed Expansion Project of Molasses Based ...environmentclearance.nic.in/.../TOR/09_Sep_2017... · It is Green field project. Ethyl alcohol is agriculture based product which

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Pre-feasibility report as per MoEF &CC Guidelines

for obtaining prior Environmental Clearance in terms

of the provisions of EIA Notification,2006

For Proposed Expansion Project ofMolasses Based Distillery from

40.0 KLD to 100.0 KLD (AA/ENA/RS)&

Power : 1.0 MW to 3.5 MW

At Village: Firozpur HafizTehsil: Mohammedpur Deomal

District : BijnorState: Uttar Pradesh

By:M/s Mohit Petrochemicals Private Limited

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Pre-Feasibility Report as per Ministry of Environment and Forests:

1. Vision, Mission & Goals

The vision and mission of the company are as follows:

Vision, Mission & Goals

Vision

To be the leader in the Production of Extra Neutral

alcohol, Specially grade alcohols and its allied products in

the state of U.P.

Mission

The expansion of distillery is highly needed to produce more

Ethanol to blend with petrol for saving of fossil fuel along

with reduction in emission of green houses gasses and

foreign currency in import of crude oil. It also helps to

increase the revenue of this agriculture industry/state/nation

and fulfill the social responsibility of the rural neighbors

Goal To complete the present project on time

2.0 THE ALCOHOL INDUSTRY

Ethyl Alcohol, Alcohol, Spirit, Denatured Spirit, there are myriad descriptions for this

agriculture-based product. A globally traded commodity, Ethanol fires combustible

engines in Brazil, slakes the thirst of many in Europe and finds its way in

pharmaceutical and chemical industries, across the world. Ethanol is made by two

routes: either by synthetic one from petroleum substances or by fermentation from

sugar-bearing or starchy substrates using yeast.

2.1 Market Potential: Uses of Alcohol Alcohol finds its use in diverse applications

ranging from potable liquor to life- saving drugs to paints & perfumery to renewable

source of energy.

Industrial Alcohol / Solvents Ethyl Alcohol is an important feedstock for the

manufacture of various chemicals. These chemicals are primarily the basic carbon

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based products like Acetic Acid, Butanol, Butadine, Acetic Anhydride, PVC, etc.

Ethylenes, Ethylene oxide are also produced from a petrochemical route; however

this requires plants of huge scales and thus requires substantially high investments.

The drug industry also uses alcohol as a raw material for production of Insulin,

Antibiotics, tonics and several other essential bulk drugs & formulations.

The following table shows the projected demand for Alcohol for production of

chemical in India:

2.2 Alcohol-based chemical industry

2.2.1: Overview

The alcohol-based chemical industry began in India in the early 1950s mainly with

ethyl alcohol as feedstock in the absence of sufficient petroleum feed stocks. Ethyl

alcohol is produced from molasses, which is a byproduct in sugar production.

Molasses is a severe pollution hazard, which resulted in the evolution of downstream

alcohol-based chemical units. The alcohol-based chemical industry saw rapid growth

as the products were not only import substitutes but also available at economical

and competitive prices in the country.

2.2.2: Growth and present status of the industry

The size of the alcohol-based chemical industry is estimated to be in the region of Rs

50 bn. Through licensing and price controls on feedstock, Central and State

governments encouraged the alcohol-based chemicals industry. In June 1993, the

Union government decontrolled molasses/alcohol to encourage this industry.

Presently, there are over 200 alcohol-based products manufactured in India, the

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single largest alcohol-based chemical being acetic acid. Acetic acid itself is the raw

material for the manufacture of several other alcohol-chemicals like ethyl acetate

(EA), butyl acetate (BA) acetic anhydride, etc. Ethyl alcohol is also used to produce

acetaldehyde and ethylene.

2.2.3: Major end use of alcohol-based chemical industries

The following are the major end uses of alcohol- based chemical industries in the

country:

Synthetic fibres and synthetic yarn

Drugs and pharmaceuticals

Agrochemicals

Personal care products

Dyestuffs, pigments, flavours and fragrances

Textile processing

Toiletries and perfumeries

Paints and surface coatings

Electroplating

Synthetic adhesives

Plastics and polymers

Solvents for inks and lacquer finishes

Food preservatives

Oilfield chemicals

Leather chemicals

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3.0 Project summary:

M/s Mohit Petrochemicals Private Limited is proposing Expansion of Distillery Plant

from 40 KLPD to 100 KLPD and Power from 1.0 MW to 3.5 MW.at Village : Firozpur

Hafiz, Block & Tehsil: Mohammedpur Deomal , District : Bijnor, Uttar Pradesh.

As per EIA Notification dated 14th Sep., 2006 and as amended from time to time;

the project falls in Category ‘A’, Project or Activity - 5(g).

PROJECT HIGHLIGHTSSr No. ITEM DETAILS1. Name of the Project M/s Mohit Petrochemicals Private Limited2. Location of the Project Village: Firozpur Hafiz

Tehsil: Mohammedpur DeomalDistrict : BijnorState: Uttar Pradesh

3. Total Project Area 22 Acre Existing4. Proposed Capacity

of DistilleryExpansion from 40 KLPD to 100 KLPDRectified Spirit / Extra Neutral alcohol /Absolute Alcohol

4.1 Number of working days 350 days/ annum

5. Proposed capacity ofPower Generation

Expansion from 1.0 MW to 3.5 MWCo- Generation.

6. Total Project Cost 4750.00 Lakhs7. Category of Project Category “A “ and Schedule - 5 (g)

8. Raw Material Molasses

9. Quantity of Molasses For Existing 40 KLDcapacity

For Proposed 100 KLDcapacity

130 KLD 320 KLD (@ 4.5 MT/ KL ofproduct)

10. Steam Requirement 28.00 TPH11. Water Requirement Industrial - 800 KL/ Day

(@ 8.0 KL/ KL of Product)Domestic – 10 KLPD

Total Water Requirement - 810 KLPD

12. Waste Water Generation Spent wash : 700 KLPD (@ 7.0 KL/ KL of Product) Other Effluent (Evaporator Condensate, Spent

Leese, Blow downs and Floor washing )=904 KLPD

Domestic – 8 KLPD

13. Waste Water Treatment Existing Treatmentfor existing 40 KLDcapacity

Proposed Treatmentstrategy for proposed 100KLD capacity

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Biomethanation +Reverse Osmosisfollowed byBio Composting.

For Spent WashMEE + Incineration(Slop fired Boiler)For Other effluent

(Condensate, Leese , Floorwashing , Blow downs)Secondary Treatment Plantshall be installed toachieve the ZERODISCHARGE.

15. Evaporation Plant Capacity 1000 m3/day proposed16. Incineration Boiler 01 No Slop fired Boiler Capacity 30 TPH.

Note: The existing Boiler of capacity 08 TPH will bedismantled after installation of new 30 TPHincineration boiler

17. Waste Water Discharge Zero Liquid Discharge Based Unit

18. Fuel Quality & Quantity For Existing 40 KLDcapacity

For Proposed 100 KLDcapacity

Bagasse/ wood chips100 TPD

Bagasse = 220 TPD+

Slop =200 m3/day19. Air Pollution Control Device ESP20. Nos. of Stack 1 No of Stack is proposed with 55 Meters

Height.21. Solid Waste Generation

Ash from BoilerUse–

Total Ash Generated : 40.0 TPDFermenter sludge: 15.0 TPDUse– Total Ash & sludge shall be used as manure.

22. Power Generation Power generation from 1.0 MW to 3.5 MW23. Power requirement 2.5 MW24. Green belt development 33 % of total Proposed Project Area (7.26 Acre)25. Cost towards

Environmentalprotection measures( Capital cost)

Rs. 2900.00 Lakhs

26. Recurring cost towardsEnvironmentalcontrol measures.

Rs – 100.00 Lakhs

27. Corporate SocialResponsibility

2% of total annual Profit as per the CSR act(By Ministry of corporate affairs) NotificationGSR 129 (E).

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4.0 PRE-FEASIBILITY REPORT AS PER MOEF&CC

Contents Details

1. Executive Summary

M/s Mohit Petrochemicals Private LimitedVillage: Firozpur HafizTehsil: Mohammedpur DeomalDistrict : BijnorState: Uttar PradeshLocation Co-ordinates:Latitude : 29°23’55.05’’NLongitude: 78° 12.35.44’’EElevation : 796 ft

Total project cost :- Rs 4750.00 LakhsM/s Mohit Petrochemicals Private Limited is proposingExpansion of Distillery Plant is from 40 KLPD to 100 KLPD andpower from 1.0 MW to 3.5 MW.at Village : Firozpur Hafiz,Block & Tehsil: Mohammedpur Deomal , District : Bijnor, UttarPradesh.As per EIA Notification dated 14th Sep., 2006 and as amendedfrom time to time; the project falls inCategory ‘A’, Project or Activity - 5(g).

2. Introduction of theproject Backgroundinformation

The proposed Expansion of Distillery Plant is from 40 KLPD to100 KLPD and power from 1.0 MW to 3.5 MW.It is Green field project.Ethyl alcohol is agriculture based product which is recognizedglobally by different name like Rectified Spirit, DenaturedSpirit, Extra Neutral Alcohol, Absolute Alcohol etc. withmultiple uses, like chemical industries, pharmaceuticalSolvents, potable purposes and as other alternative source ofenergy world wise.

Alcohol can be produced either synthetically from petroleumsubstances or by fermentation from Sugar or starchysubstrates using yeast.

Industrial Use Of Alcohol

Important feed stock for manufacture of various Carbon Basedchemicals like Acetic Acid, Butanol, Butadine, PVC etc.

Alcohol is also used in essential drugs and formulations.

FUEL ETHANOL- Alcohol has a great future in the energysector. August 13, 2002 was a historic day for the IndianEthanol programme as on this day the Government of Indiafinally announced that from January 1, 2003 blending of 5% ofEthanol were be made mandatory in Nine States and Four

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Contents Details

Union Territories of India i.e. 70% of Gasoline consumed inIndia has to doped with 5% of Ethanol. To ensure that 350million Litres of Ethanol of right quality will have to be madeavailable in adequate quantities to various oil depotthroughout the Country.

In future when India has to reduce the dependence onpetroleum imports due to very high world market prices thedoping of gasoline by ethanol may go as high as 10% to 20%.In that case the requirement of ethanol will be still higher asshown below-

The present supply and future projection in terms of ethanoluse in India -

Ethanol Required perAnnum @ 5% blending

450 MillionLitres


900 MillionLitres

Average production ofAlcohol per Annum

1600 MillionLitres

The projection of fuel ethanol required with the @5% blendingis about 31% of total alcohol production in India. Consideringthe possibility of blending of petrol @ 10% in near future therequirement will increase substantially and thereforeinstallation of more ethanol plants also becomes necessary inorder to cope up with the requirement.

Alcohol has a very important place in the country's economy.This a vital raw material for a number of chemicals. It has beena source of larger amount of revenue by way of excise dutylevied by state government on alcoholic liquors. It haspotential as fuel in the form of power alcohol for blending ofgasoline in ratio 20: 80.

Fermentation alcohol is in great demand in countries likeJapan, USA, Canada, Sri Lanka etc. The synthetic alcoholproduced from Neptha of petroleum crude is not useful forbeverages. These countries import large quantities of alcoholand India is one main supplier.

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Contents Details

India produced 25% of the world cane molasses production.Uttar Pradesh has enough potential to develop caneproduction to increase the capacity of existing sugar factoriesand produce as much molasses as possible to increase alcoholproduction and earn revenue for Uttar Pradesh and India onthe whole and can also help in industrial growth of UttarPradesh.

The main process involved in production of Alcohol from canemolasses are fermentation in which sugars are broken down inalcohol and Carbon-di- Oxide (CO2) and then pumped todistillation section in which alcohol is stripped off fromfermented wash in form of Vapour and then condensed tohave Alcohol.

These days many Technologies are available for fermentationprocess like Batch Fermentation, Bio Still Process, Hiform-Continuous Fermentation etc.

The same way the various technologies of distillation processrange from -

Conventional direct steam Heating &Rectifier columns.

Multi pressure distillation technology heating forStripping off alcohol under vacuum in flubex heatexchanger known as MPR technology.

i. Identification of projectand project proponent.In case of miningproject, a copy ofmining lease/letter ofintent should be given.

N/A

ii. Brief description ofnature of the project.

The proposed Expansion of Distillery Plant is from 40 KLPD to100 KLPD and power from 1.0 MW to 3.5 MW.It is Green field project.

iii. Need for the projectand its importance tothe country and orregion.

Besides the technical and environmental benefits fuel ethanoloffers, it makes tremendous economic sense in India as India'sImport bill of crude petroleum is increasing every year.

India is number two in the world in Sugarcane production. Thenumber of sugar factories is 416 and 295 distilleries in thecountry. Large number of sugar factories co-produce ethanol.The introduction of ethanol fuel will give big boost to Indian

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Contents Details

economy by following ways:

The efficiency and commercial viability of sugarfactories will improve.

Farmers will get higher price for sugarcane which willimprove the socio-economic status of farmers.

Agriculture will get boost because of additionalproduction of sorghum, jawar and sugarcane.

Mixing of ethanol to petrol will save foreign exchangeworth Rs. 4000 crores every year.

Less dependence on imports and cheaper cost oproduction of ethanol will bring down the prices offuels.

Overall it is "Ecofriendly Project".In view of the above positive results, it is recommendedwithout any reservation that the establishment of thisfactory be granted.

iv. Demand-Supply Gap.

70% of

Gasoline consumed in India has to doped with 5% of Ethanol.To ensure that 350 million Litres of Ethanol of right quality willhave to be made available in adequate quantities to variousoil depot through out the Country.

In future when India has to reduce the dependence onpetroleum imports due to very high world market prices thedoping of gasoline by ethanol may go as high as 10% to 20%.In that case the requirement of ethanol will be still higher asshown below-

The present supply and future projection in terms of ethanoluse in India -The projection of fuel ethanol required with the@5% blending is about 31% of total alcohol production inIndia. Considering the possibility of blending of petrol @ 10%


450 MillionLitres

Ethanol Required perAnnum @ 10%blending

900 MillionLitres

Average production ofAlcohol per Annum

1600 MillionLitres

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Contents Details

in near future the requirement will increase substantially andtherefore installation of more ethanol plants also becomesnecessary in order to cope up with the requirement.

v. Imports vs. Indigenousproduction. Only indigenous production.

vi. Export Possibility. No

vii. Domestic/exportMarkets. Domestic Only

viii. EmploymentGeneration (Direct andIndirect) due to theproject.

Direct employment :- approx 35 personsIndirect employment :- approx 45 persons

3. Project Description

i. Type of projectincluding interlinkedand interdependentprojects, if any.

Expansion of Distillery Unit along with power

ii. Location (map showinggeneral location,specific location, andproject boundary &project site layout) withcoordinates.

Location map Enclosed (Google EARTH MAP/ TOPOSHEET)

iii. Details of alternatesites considered andthe basis of selectingthe proposed site,particularly theenvironmentalconsiderations goneinto should behighlighted.

Proposed site is within distillery unit so it is convenient tooperate by our common officer/staffs. Proposed Expansionwill be Done in Existing Distillery unit.

iv. Size or magnitude ofoperation. 100 KLPD Distillery along with 3.5 MW power

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Contents Details

v. Project description withprocess details (aschematic diagram flowchart showing theproject layout,components of theproject etc. should begiven)

Distillation And Fermentation flow diagram enclosed withProject report.

vi. Raw material requiredalong with estimatedquantity, likely source,marketing area of finalproducts, Mode oftransport of rawMaterial and FinishedProduct.

vii. Resourceoptimization/recyclingand reuse envisaged inthe project, if any,should be brieflyoutlined.

Waste Water (Spent Wash) shall be used in boiler as a fuel.Bagasse Ash used as manure.Slop used as a Manure

viii. Availability of water itssource, Energy/powerrequirement andsource should be given.

Total Water Requirement-Industrial - 800 KL/ Day

(@ 8.0 KL/ KL of Product)Domestic – 10 KLPDTotal Water Requirement - 810 KLPD

Molasses ForExisting 40 KLDcapacity

Molasses ForProposed 100 KLDcapacity

130 KLD 320 KLD

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Contents Details

ix. Quantity of wastes tobe generated (liquidand solid) and schemefor their Management/disposal.

Spent wash : 700 KLPD (@ 7.0 KL/ KL of Product) Other Effluent (Evaporator Condensate, Spent Leese,

Blow downs and Floor washing )=904 KLPD

Domestic – 8 KLPD

Solid Waste- Total Ash Generated : 40.0 TPDFermenter sludge: 15.0 TPDBagasse/slop Ash, Fermenter sludge will be used as manuredue to high value of potash.

x. Schematicrepresentations of thefeasibility drawingwhich give informationof EIA purpose.

It will be enclosed in EIA report.

4. Site Analysis

i. Connectivity.Railway Station:Bijnor - (Broad gauge)- 9.0 Km -N. RailwayAirport: New Delhi Air Port, 180 Km

ii. Land Form, Land useand Land ownership.

Plain land , Industrial Land is registered under M/s MohitPetrochemicals Private Limited

iii. Topography (along withmap). Location Map (Google Earth map) enclosed

iv. Existing land usepattern (agriculture,non-agriculture, forest,water bodies (includingarea under CRZ)),shortest distances fromthe periphery of theproject to periphery ofsanctuary, eco from theHFL industrial area, begiven.

Land use pattern will be incorporated in EIA Study report.

v. Existing Infrastructure. Existing Distillery Unit

vi. Soil classification Silty/Clay/Sand

vii. Climatic data from Max. Temp:45.2°C

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Contents Details

secondary sources. Mini. Temp: 3.8 ° CAve Temp: 27 °CRelative Humidity: 47 – 85 %

viii. Social Infrastructureavailable. Road, School & electricity.

5.Planning Brief

i. Planning Concept (typeof industries,transportation etc)Town and Planning/Development authorityClassification

Transportation by Road.

ii. Population Projection 80 approx (direct + indirect)

iii. Land use planning(breakup along withgreen belt etc).

67% for Plant establishment and other Facilities and Greenbelt development: 33% of total area of land.

iv. Assessment ofInfrastructure Demand(Physical & Social).

Local labours & construction material.

v. Amenities/Facilities. Companies employees and consumer shall be provided.

6. Proposed Infrastructure

i. Industrial Area(Processing Area). Industrial land

ii. Residential Area (NonProcessing Area). Available with existing Sugar mill.

iii. Green Belt. Green belt development: 33% of total area of existing land.

iv. Social Infrastructure.

Proposed expansion will lead to the development of certainlocal ancillary facilities and consequent employmentopportunities. Further the proposed expansion will also leadto the development of market, trade centres, bankingactivities etc.

v. Connectivity (Trafficand Rail/Metro/Waterways etc)

Railway Station:Bijnor - (Broad gauge)- 9.0 Km -N. RailwayAirport: IGI New Delhi Air Port, 180 Km

vi. Drinking WaterManagement (Sourcewater)

Ground water.

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Contents Details

vii. Sewerage System. Septic tank / Sock pit for domestic effluent treatment.

viii. Industrial WasteManagement.

For Spent WashMEE + Incineration(Slop fired Boiler)For Other effluent(Condensate, Leese , Floor washing , Blow downs)Secondary Treatment Plant shall be installed to achievethe ZERO DISCHARGE.

ix. Solid WasteManagement.

Bagasse Ash/fermenter sludge will be used as manure due tohigh value of potash.

x. Power Requirement &Supply / source.

Power generation 3.5MW (total)

7. Rehabilitation andResettlement (R&R) Plan

i. Policy to be adopted(Central/State) inrESPect Of the projectaffected personsincluding homeoustees, land ousteesand landless laborers (abrief outline to begiven).

The proposed plant is within the existing distillery unit. Theland is already under the possession of M/s MohitPetrochemicals Private Limited. Therefore, there will not beany displacement of people and hence, Rehabilitation &Resettlement is not applicable.

8. Project Schedule & CostEstimates

ii. Likely date of start ofconstruction and likelydate of completion(Time schedule for theproject to be given).

After receipt of NOC & Environmental Clearance.

iii. Estimated project costalong with analysis interms of economicviability of the project. Rs 4750.00 lacs

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Contents Details

9. Analysis of proposal(Final Recommendations)

i. Financial and socialbenefits with specialemphasis on the benefitto the local peopleincluding tribalpopulation, if any, in thearea.

Financial Benefits:Benefits and advantages of bagasse/biomass cogenerationinclude:

a) Increasing the viability of sugar millsb) Increased fuel efficiency

Social Benefits:

Greater employment for local populations

Environmental benefits:

a) Low emission of particulates,SO2,NOx and CO2

compared to coal and other fossils fuelsb) It is a Green field project.c) Own generation of power.

Other Benefits:

Revenues to the State and Central ex-chequers.

Over all development of Bijnor District in particular and UttarPradesh State in general.

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Project Description &Zero Liquid Discharge Based

Treatment Strategy

By:M/s Mohit Petrochemicals Private Limited

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1.0 Project Brief:

M/s Mohit Petrochemicals Private Limited has decided to adopt the latest technology

to achieve Zero Liquid Discharge (ZLD) for the proposed expansion project,

from 40.0 KLPD to 100.0 KLPD distillery unit along with 3.5 MW co gen power;

Resource optimization / recycling and reuse envisaged in the project

Optimum utilization of the available resources is strived by the management.

These resources include land, water, steam, molasses and power. Press-mud is a by-

product of sugar factory that will be used for making manure by mixing fermenter

sludge and potash rich fly ash generated in the distillery. Thereby, nutrients will be

recycled.

The process flow chart is as follows:

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2.0 Environmental Settings

The environment setting of the project around 15 km radius is as follows:

Sr. No. Particulars Details

1 Location

Village Firozpur Hafiz

District Bijnor

State Uttar Pradesh

Latitude 29⁰23’55.05”N

Longitude 78⁰12’35.44”E

2 Elevation 796 ft

3 Climatic condition

Temperature Max. Temp:45.2 °C

Mini. Temp: 3.8 °C

Ave Temp: 27 ° C

Relative humidity Relative Humidity: 47 – 85 %

4 State highway SH-12 (adjacent to unit in North direction)

National highway NH-74

(in East direction at a distance of 14.21 km)

5 Nearest Railway Station Bijnor - (Broad Gauge)- 9.0 Km -N. Railway

6 Nearest Airport IGI New Delhi Air Port, 180 Km

7 Tourist Places Nil(within 15 kms of study area )

8 Archaeological

important places

Nil(within 15 kms of study area )

9 Area which are

important or sensitive

for ecological reasons-

Wetlands, watercourses

or other water bodies,

coastal zone,

biospheres, mountains,

forests.

NIL(within 15 kms of study area )

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10 Reserved Forest Nil (within 15 kms of study area )

11 Nearest Major city with

200000 population

Bijnor

12 Village within 2 km

Radius surrounding the

project

Firozpur Hafiz

13 Nearest River River Chhoiya – *300 Meters in South

direction

River Ganga -*13.40 km in West South

direction

Note: river chhoiya is connecting to river

ganga at a distance of about 16.8 kms*

(*Aerial distance)

14 Nearest Hill Range Nil

15 Soil Type Sandy loam, clay loam

16 Seismic Zone IV as per IS- 1893(Part- 1)-2002

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Image 3: Image showing the Rivers around the project site and their connectivitySource: Google Earth

Location of Distillery Site

River Chhoiya at distance of 300 meters in South Direction

River Ganga the closest distancefrom site to River Ganga is 13.40 km

approx

River Chhoiya connecting to River Gangaat a distance of 35 km

(Aerial Distance)

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approx


(Aerial Distance)

21





approx


(Aerial Distance)

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Source- Google EarthImage1: Location of distillery site M/s Mohit Petrochemicals At Village Firozpur Hafiz, District Bijnor

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3.0 Coordinates of Corners of Plot:The coordinates of all four corners of the proposed project along with centre is given here under in table 1

TABLE - 11 LOCATION CORNER 1 North

Village Firozpur HafizDistrict BijnorLatitude 29⁰23’57.85”NLongitude 78⁰12’37.89”E

2 LOCATION CORNER 2 EastVillage Firozpur HafizDistrict BijnorLatitude 29⁰23’56.19”NLongitude 78⁰12’38.92”E

3 LOCATION CORNER 3 SouthVillage Firozpur HafizDistrict BijnorLatitude 29⁰23’53.86”NLongitude 78⁰12’35.37”E

4 LOCATION CORNER 4 WestVillage Firozpur HafizDistrict BijnorLatitude 29⁰23’55.86”NLongitude 78⁰12’35.12”E

5 LOCATION (CENTRE OF THE SITE)Village Firozpur HafizDistrict BijnorLatitude 29⁰23’55.05”NLongitude 78⁰12’35.44”E

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5 KM RADIUS BUFFER MAPTOPO SHEET NO.53K/3,53 K/7(GEOLOGICAL SURVEY OF INDIA)LEGEND:

-SITE-5 KMS RADIUS

PROJECT NAME:M/s Mohit Petrochemicals PrivateLimitedVillage: Firozpur HafizTehsil: Mohammedpur Deomal

Project Location Coordinates:Latitude 29°23’55.05”NLongitude 78°12’35.44”ESCALE: 1:50000

Image 2: Toposheet of study area (5.0 km radius)

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-SITE-5 KMS RADIUS




24


-SITE-5 KMS RADIUS




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10 KM RADIUS TOPO MAPTOPO SHEET NO.53K/3,53 K/7(GEOLOGICAL SURVEY OF INDIA)LEGEND:

-SITE-10 KMS RADIUS




25


-SITE-10 KMS RADIUS




25


-SITE-10 KMS RADIUS




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4.0 Availability of water and its source

Necessary water requirement for the proposed project will be met from bore well.

Water will be required for domestic, process and utility purpose. Daily fresh water

requirement for the proposed distillery unit will be around 810.0 m3⁄d.

5.0 Waste Generation & Treatment Scheme

Estimated daily total water requirement of distillery will be (input) 2540.0 m3/d.

However, during day-to- day operations 1730.0 m3/day water will be recycled and

thus fresh water requirement will be restricted to 810.0 m3/day. Effluent in the form

of spent wash will be 700.0 m3 /day. It will be treated concentrated in Multi effect

evaporation (1000 m3/day capacity/ 7 stage) and then concentrate from MEE will be

utilised in Incineration fired boiler as a fuel along with bagasse.

At secondary stage, its volume will be reduced to 200.0 m3/day using multi effect

evaporation (MEE). This effluent will be safely disposed through incineration in boiler

to achieve “Zero Liquid Discharge” as per CPCB norms. The remaining moderately

polluted effluent due to spent lees and evaporating condensate will be treated in

polishing unit and recycled in the same unit. Estimated domestic effluent will be 7.0

m3/d, which will be treated separately in septic tank and soak pit. Quantity of waste

to be generated & scheme for their disposal is given in the following tables.

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5.1 Water Balance: Distillery of 100 KLPD & 3.5 MW Power

Total Water Input for Proposed 100.0 KLD DistilleryS.No Section Water required

1 Lees recycle for Dilution 100.02 Steam Condensate recycle 620.03 Cooling Tower recycle 770.04 Floor Wash 10.05 Vacuum pump water recirculation 200.06. CIP Cleaning 30.0

Total recycling and Utilizing 1730.0Fresh water requirement 800.0

Domestic Use 10.0Total Water requirement for First Run 2540.0

Total Water Output for Proposed 100.0 KLD Distillery

S.No Section Water required1 Steam condensate 620.02 Spent wash 700.03 Spent leese 160.04 Cooling tower Evaporation 670.05 Blow down (Boiler Blow down) 14.06 Vaccum pump & sealing water 200.07 Miscellaneous 136.08 CIP Cleaning 30.09 Washing 10.0

Total 2540.0

Total Water Recycle for Proposed 100.0 KLD Distillery

S.No Section Water required1 Lees recycle for Dilution 100.02 Steam Condensate recycle 620.03 CPU treated Water to CT 770.04 Floor Wash 10.05 Vacuum pump water recirculation 200.06 CIP Cleaning 30.0

Total recycling and Utilizing 1730.0Fresh water requirement 810.0

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Fig 1

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5.2 Other Effluent:

Approx 904 KLD of other effluent will be generated in proposed distillery which will

be treated in condensate treatment plant (secondary effluent treatment plant).

Treatment scheme is as under fig below

I: Design Basis

CPU will treat 904m3 per day of Evaporation Condensate (spent wash condensate),

cooling tower blow down, boiler blow down, miscellaneous washing, etc from

Distillery along with Spent Leese. The Combined effluent shall first be treated in

diffused aeration system comprises of activated sludge process. The Pretreatment in

the form of Equalization, Neutralization and Solids removal shall be provided. The

treated Effluent after Biological Treatment can be discharged on land for Irrigation /

Surface water streams. However, the treated effluent shall then be subjected to

tertiary treatment consists of carbon filter and sand filter. The treated water can be

used for Process / Cooling Towers. Flow diagram of waste water treatment system

(CPU) is given fig 2

Figure – 2. Condensate treatment unit

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Fig 3.Zero Discharge Based Treatment Strategy

Distillery Unit: 100 KLD

SPENT WASH: 700 KLD @7.0KL/KL OF PRODUCT

MEE CAPACITY: 1000 m3

MEE CONDENSATE: 620 KLD

Other Effluents: 284 KLDLees, Boiler Blow Down, DM PlantReject, Cooling Tower Blow Down,Washing, RO Reject

Condensate Treatment Unit with ROof capacity 1000 m3/day

Treated water will be recycled back inCooling tower makeup , Floor Washing etc

SLOP 200 KLD

Boiler 30 TPH

STEAM requirement 28 tph forprocess , MEE and co gen of

power

Documents

For Proposed Expansion Project of Molasses Based ...environmentclearance.nic.in/.../TOR/09_Sep_2017... · It is Green field project. Ethyl alcohol is agriculture based product which