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 of Molasses Based Distillery from

40.0 KLD to 100.0 KLD (AA/ENA/RS) & Power : 1.0 MW to 3.5 MW

At Village: Firozpur Hafiz Tehsil: Mohammedpur Deomal District : Bijnor State: Uttar Pradesh

By: M/s Mohit Private Limited

1 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

To be the leader in the Production of Extra Neutral alcohol, Specially grade alcohols and its allied products in Vision the state of U.P.

The expansion of distillery is highly needed to produce more to blend with petrol for saving of along with reduction in emission of green houses gasses and foreign currency in import of crude oil. It also helps to Mission increase the revenue of this /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 , 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 to life- saving drugs to & 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

2 based products like Acetic Acid, Butanol, Butadine, Acetic Anhydride, PVC, etc. Ethylenes, Ethylene oxide are also produced from a route; however this requires plants of huge scales and thus requires substantially high investments. The drug industry also uses alcohol as a 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 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 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

3 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, , flavours and fragrances  Textile processing  Toiletries and perfumeries  Paints and surface coatings  Electroplating  Synthetic  Plastics and polymers  Solvents for and lacquer finishes  Food preservatives  Oilfield chemicals  chemicals

4 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 HIGHLIGHTS Sr No. ITEM DETAILS 1. Name of the Project M/s Mohit Petrochemicals Private Limited 2. Location of the Project Village: Firozpur Hafiz Tehsil: Mohammedpur Deomal District : Bijnor State: Uttar Pradesh 3. Total Project Area 22 Acre Existing 4. Proposed Capacity Expansion from 40 KLPD to 100 KLPD of Distillery / Extra Neutral alcohol / Absolute Alcohol 4.1 Number of working days 350 days/ annum 5. Proposed capacity of Expansion from 1.0 MW to 3.5 MW Power Generation Co- Generation. 6. Total Project Cost 4750.00 Lakhs 7. Category of Project Category “A “ and Schedule - 5 (g) 8. Raw Material Molasses 9. Quantity of Molasses For Existing 40 KLD For Proposed 100 KLD capacity capacity 130 KLD 320 KLD (@ 4.5 MT/ KL of product) 10. Steam Requirement 28.00 TPH 11. 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 Treatment Proposed Treatment for existing 40 KLD strategy for proposed 100 capacity KLD capacity

5 Biomethanation + For Spent Wash Reverse Osmosis MEE + Incineration followed by (Slop fired Boiler) Bio Composting. For Other effluent (Condensate, Leese , Floor washing , Blow downs) Secondary Treatment Plant shall be installed to achieve the ZERO DISCHARGE. 15. Evaporation Plant Capacity 1000 m3/day proposed 16. Incineration Boiler 01 No Slop fired Boiler Capacity 30 TPH. Note: The existing Boiler of capacity 08 TPH will be dismantled after installation of new 30 TPH incineration boiler 17. Waste Water Discharge Zero Liquid Discharge Based Unit 18. Fuel Quality & Quantity For Existing 40 KLD For Proposed 100 KLD capacity capacity Bagasse/ wood chips Bagasse = 220 TPD 100 TPD + Slop =200 m3/day 19. Air Pollution Control Device ESP 20. Nos. of Stack 1 No of Stack is proposed with 55 Meters Height. 21. Solid Waste Generation Total Ash Generated : 40.0 TPD Ash from Boiler Fermenter sludge: 15.0 TPD Use– Use– Total Ash & sludge shall be used as manure. 22. Power Generation Power generation from 1.0 MW to 3.5 MW 23. Power requirement 2.5 MW 24. Green belt development 33 % of total Proposed Project Area (7.26 Acre) 25. Cost towards Rs. 2900.00 Lakhs Environmental protection measures ( Capital cost) 26. Recurring cost towards Rs – 100.00 Lakhs Environmental control measures. 27. Corporate Social 2% of total annual Profit as per the CSR act Responsibility (By Ministry of corporate affairs) Notification GSR 129 (E).

6 4.0 PRE-FEASIBILITY REPORT AS PER MOEF&CC

Contents Details

M/s Mohit Petrochemicals Private Limited Village: Firozpur Hafiz Tehsil: Mohammedpur Deomal District : Bijnor State: Uttar Pradesh Location Co-ordinates: Latitude : 29°23’55.05’’N Longitude: 78° 12.35.44’’E Elevation : 796 ft 1. Executive Summary Total project cost :- Rs 4750.00 Lakhs M/s Mohit Petrochemicals Private Limited is proposing Expansion of Distillery Plant is 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). The proposed Expansion of Distillery Plant is from 40 KLPD to 100 KLPD and power from 1.0 MW to 3.5 MW. It is Green field project. Ethyl alcohol is agriculture based product which is recognized globally by different name like Rectified Spirit, Denatured Spirit, Extra Neutral Alcohol, Absolute Alcohol etc. with multiple uses, like chemical industries, pharmaceutical Solvents, potable purposes and as other alternative source of energy world wise. Alcohol can be produced either synthetically from petroleum 2. Introduction of the substances or by fermentation from Sugar or starchy project Background substrates using yeast. information Industrial Use Of Alcohol Important feed stock for manufacture of various Carbon Based chemicals 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 energy sector. August 13, 2002 was a historic day for the Indian Ethanol programme as on this day the Government of India finally announced that from January 1, 2003 blending of 5% of Ethanol were be made mandatory in Nine States and Four

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Union Territories of India i.e. 70% of consumed in India has to doped with 5% of Ethanol. To ensure that 350 million Litres of Ethanol of right quality will have to be made available in adequate quantities to various oil depot throughout the Country. In future when India has to reduce the dependence on petroleum imports due to very high world market prices the doping of gasoline by ethanol may go as high as 10% to 20%. In that case the requirement of ethanol will be still higher as shown below- The present supply and future projection in terms of ethanol use in India -

Ethanol Required per 450 Million Annum @ 5% blending Litres

Ethanol Required per 900 Million Annum @ 10% blending Litres

Average production of 1600 Million Alcohol per Annum Litres

The projection of fuel ethanol required with the @5% blending is about 31% of total alcohol production in India. Considering the possibility of blending of petrol @ 10% in near future the requirement will increase substantially and therefore installation of more ethanol plants also becomes necessary in order 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 been a source of larger amount of revenue by way of excise duty levied by state government on alcoholic . It has potential as fuel in the form of power alcohol for blending of gasoline in ratio 20: 80. Fermentation alcohol is in great demand in countries like Japan, USA, Canada, Sri Lanka etc. The synthetic alcohol produced from Neptha of petroleum crude is not useful for beverages. These countries import large quantities of alcohol and India is one main supplier.

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India produced 25% of the world cane molasses production. Uttar Pradesh has enough potential to develop cane production to increase the capacity of existing sugar factories and produce as much molasses as possible to increase alcohol production and earn revenue for Uttar Pradesh and India on the whole and can also help in industrial growth of Uttar Pradesh. The main process involved in production of Alcohol from cane molasses are fermentation in which sugars are broken down in alcohol and Carbon-di- Oxide (CO2) and then pumped to section in which alcohol is stripped off from fermented wash in form of Vapour and then condensed to have Alcohol. These days many are available for fermentation process like Batch Fermentation, Bio Still Process, Hiform- Continuous Fermentation etc. The same way the various technologies of distillation process range from -  Conventional direct steam Heating &Rectifier columns.  Multi pressure distillation heating for Stripping off alcohol under vacuum in flubex heat exchanger known as MPR technology.

i. Identification of project and project proponent. In case of N/A project, a copy of mining /letter of intent should be given. The proposed Expansion of Distillery Plant is from 40 KLPD to ii. Brief description of 100 KLPD and power from 1.0 MW to 3.5 MW. nature of the project. It is Green field project.

Besides the technical and environmental benefits fuel ethanol offers, it makes tremendous economic sense in India as India's iii. Need for the project Import bill of crude petroleum is increasing every year. and its importance to the country and or India is number two in the world in Sugarcane production. The region. number of sugar factories is 416 and 295 distilleries in the country. Large number of sugar factories co-produce ethanol. The introduction of ethanol fuel will give big boost to Indian

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economy by following ways:  The efficiency and commercial viability of sugar factories will improve.  Farmers will get higher price for sugarcane which will improve the socio-economic status of farmers.  Agriculture will get boost because of additional production of sorghum, jawar and sugarcane.  Mixing of ethanol to petrol will save foreign exchange worth Rs. 4000 crores every year.  Less dependence on imports and cheaper cost o production of ethanol will bring down the prices of fuels.  Overall it is "Ecofriendly Project". In view of the above positive results, it is recommended without any reservation that the establishment of this factory be granted.

Ethanol Required per 450 Million Annum @ 5% blending Litres

70% of Ethanol Required per 900 Million Annum @ 10% Litres blending Average production of 1600 Million Alcohol per Annum Litres

iv. Demand-Supply Gap. Gasoline consumed in India has to doped with 5% of Ethanol. To ensure that 350 million Litres of Ethanol of right quality will have to be made available in adequate quantities to various oil depot through out the Country. In future when India has to reduce the dependence on petroleum imports due to very high world market prices the doping of gasoline by ethanol may go as high as 10% to 20%. In that case the requirement of ethanol will be still higher as shown below- The present supply and future projection in terms of ethanol use in India -The projection of fuel ethanol required with the @5% blending is about 31% of total alcohol production in India. Considering the possibility of blending of petrol @ 10%

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in near future the requirement will increase substantially and therefore installation of more ethanol plants also becomes necessary in order to cope up with the requirement.

v. Imports vs. Indigenous Only indigenous production. production. vi. Export Possibility. No vii. Domestic/export Domestic Only Markets. viii. Employment Generation (Direct and Direct employment :- approx 35 persons Indirect) due to the Indirect employment :- approx 45 persons project. 3. Project Description i. Type of project including interlinked Expansion of Distillery Unit along with power and interdependent projects, if any. ii. Location (map showing general location, specific location, and Location map Enclosed (Google EARTH MAP/ TOPOSHEET) project boundary & project site layout) with coordinates. iii. Details of alternate sites considered and the basis of selecting the proposed site, Proposed site is within distillery unit so it is convenient to particularly the operate by our common officer/staffs. Proposed Expansion environmental will be Done in Existing Distillery unit. considerations gone into should be highlighted. iv. Size or magnitude of 100 KLPD Distillery along with 3.5 MW power operation.

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v. Project description with process details (a schematic diagram flow chart showing the project layout, Distillation And Fermentation flow diagram enclosed with components of the Project report. project etc. should be given)

vi. Raw material required Molasses For Molasses For along with estimated Existing 40 KLD Proposed 100 KLD quantity, likely source, capacity capacity area of final products, Mode of 130 KLD 320 KLD of raw Material and Finished Product. vii. Resource optimization/ Waste Water (Spent Wash) shall be used in boiler as a fuel. and reuse envisaged in Bagasse Ash used as manure. the project, if any, Slop used as a Manure should be briefly outlined.

Total Water Requirement- viii. Availability of water its Industrial - 800 KL/ Day source, Energy/power (@ 8.0 KL/ KL of Product) requirement and Domestic – 10 KLPD source should be given. Total Water Requirement - 810 KLPD

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Spent wash : 700 KLPD (@ 7.0 KL/ KL of Product)  Other Effluent (Evaporator Condensate, Spent Leese, ix. Quantity of wastes to Blow downs and Floor washing ) be generated (liquid =904 KLPD and solid) and scheme  Domestic – 8 KLPD for their / disposal. Solid Waste- Total Ash Generated : 40.0 TPD Fermenter sludge: 15.0 TPD Bagasse/slop Ash, Fermenter sludge will be used as manure due to high value of .

x. Schematic representations of the feasibility It will be enclosed in EIA report. which give information of EIA purpose.

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

ii. Land Form, Land use Plain land , Industrial Land is registered under M/s Mohit and Land . Petrochemicals Private Limited

iii. Topography (along with Location Map (Google Earth map) enclosed map). iv. Existing land use pattern (agriculture, non-agriculture, forest, water bodies (including area under CRZ)), shortest distances from Land use pattern will be incorporated in EIA Study report. the periphery of the project to periphery of sanctuary, eco from the HFL industrial area, be given. 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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secondary sources. Mini. Temp: 3.8 ° C Ave Temp: 27 °C Relative Humidity: 47 – 85 % viii. Social Infrastructure , School & electricity. available. 5.Planning Brief i. Planning Concept (type of industries, transportation etc) Transportation by Road. Town and Planning/ Development authority Classification ii. Population Projection 80 approx (direct + indirect) iii. Land use planning 67% for Plant establishment and other Facilities and Green (breakup along with belt development: 33% of total area of land. green belt etc). iv. Assessment of Infrastructure Demand Local labours & material. (Physical & Social). v. Amenities/Facilities. Companies employees and consumer shall be provided. 6. Proposed Infrastructure

i. Industrial Area Industrial land (Processing Area).

ii. Residential Area (Non Available with existing Sugar mill. Processing Area). iii. Green Belt. Green belt development: 33% of total area of existing land. Proposed expansion will lead to the development of certain local ancillary facilities and consequent employment iv. Social Infrastructure. opportunities. Further the proposed expansion will also lead to the development of market, trade centres, banking activities etc. v. Connectivity (Traffic Railway Station: and Rail/Metro/Water Bijnor - (Broad gauge)- 9.0 Km -N. Railway ways etc) Airport: IGI New Delhi Air Port, 180 Km vi. Drinking Water Management (Source Ground water. water)

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vii. Sewerage System. Septic tank / Sock pit for domestic effluent treatment. For Spent Wash MEE + Incineration (Slop fired Boiler) viii. Industrial Waste For Other effluent Management. (Condensate, Leese , Floor washing , Blow downs) Secondary Treatment Plant shall be installed to achieve the ZERO DISCHARGE. ix. Solid Waste Bagasse Ash/fermenter sludge will be used as manure due to Management. high value of potash. Power generation 3.5MW (total) x. Power Requirement & Supply / source.

7. Rehabilitation and Resettlement (R&R) Plan i. Policy to be adopted (Central/State) in rESPect Of the project The proposed plant is within the existing distillery unit. The affected persons land is already under the possession of M/s Mohit including home Petrochemicals Private Limited. Therefore, there will not be oustees, land oustees any displacement of people and hence, Rehabilitation & and landless laborers (a Resettlement is not applicable. brief outline to be given). 8. Project Schedule & Cost Estimates ii. Likely date of start of construction and likely date of completion After receipt of NOC & Environmental Clearance. (Time schedule for the project to be given). iii. Estimated project cost along with analysis in terms of economic viability of the project. Rs 4750.00 lacs

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9. Analysis of proposal (Final Recommendations) Financial Benefits: Benefits and advantages of bagasse/biomass cogeneration include: a) Increasing the viability of sugar mills b) Increased fuel efficiency

Social Benefits:

Greater employment for local populations i. Financial and social benefits with special Environmental benefits: emphasis on the benefit to the local people a) Low emission of particulates,SO2,NOx and CO2 including tribal compared to and other fossils fuels population, if any, in the b) It is a Green field project. area. c) Own generation of power.

Other Benefits:

Revenues to the State and Central ex-chequers.

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

16 Project Description & Zero Liquid Discharge Based Treatment Strategy

By: M/s Mohit Petrochemicals Private Limited

17 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:

18 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 Nil(within 15 kms of study area ) important places 9 Area which are NIL(within 15 kms of study area ) important or sensitive for ecological reasons- Wetlands, watercourses or other water bodies, coastal zone, biospheres, mountains, forests.

19 10 Reserved Forest Nil (within 15 kms of study area ) 11 Nearest Major city with Bijnor 200000 population 12 Village within 2 km Firozpur Hafiz Radius surrounding the project 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

20 Location of Distillery Site

River Chhoiya at distance of 300 meters in South Direction

River Ganga the closest distance from site to River Ganga is 13.40 km approx

River Chhoiya connecting to River Ganga at a distance of 35 km (Aerial Distance)

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

21 Source- Google Earth Image1: Location of distillery site M/s Mohit Petrochemicals At Village Firozpur Hafiz, District Bijnor

22 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 - 1 1 LOCATION CORNER 1 North Village Firozpur Hafiz District Bijnor Latitude 29⁰23’57.85”N Longitude 78⁰12’37.89”E 2 LOCATION CORNER 2 East Village Firozpur Hafiz District Bijnor Latitude 29⁰23’56.19”N Longitude 78⁰12’38.92”E 3 LOCATION CORNER 3 South Village Firozpur Hafiz District Bijnor Latitude 29⁰23’53.86”N Longitude 78⁰12’35.37”E 4 LOCATION CORNER 4 West Village Firozpur Hafiz District Bijnor Latitude 29⁰23’55.86”N Longitude 78⁰12’35.12”E 5 LOCATION (CENTRE OF THE SITE) Village Firozpur Hafiz District Bijnor Latitude 29⁰23’55.05”N Longitude 78⁰12’35.44”E

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

-SITE -5 KMS RADIUS

PROJECT NAME: M/s Mohit Petrochemicals Private Limited Village: Firozpur Hafiz Tehsil: Mohammedpur Deomal

Project Location Coordinates: Latitude 29°23’55.05”N Longitude 78°12’35.44”E SCALE: 1:50000

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

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

-SITE -10 KMS RADIUS

PROJECT NAME: M/s Mohit Petrochemicals Private Limited Village: Firozpur Hafiz Tehsil: Mohammedpur Deomal

Project Location Coordinates: Latitude 29°23’55.05”N Longitude 78°12’35.44”E SCALE: 1:50000

Image 3: Toposheet of study area (10.0 km radius) 25 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.

26 5.1 Water Balance: Distillery of 100 KLPD & 3.5 MW Power

Total Water Input for Proposed 100.0 KLD Distillery S.No Section Water required 1 Lees recycle for Dilution 100.0 2 Steam Condensate recycle 620.0 3 Cooling Tower recycle 770.0 4 Floor Wash 10.0 5 Vacuum pump water recirculation 200.0 6. CIP Cleaning 30.0 Total recycling and Utilizing 1730.0 Fresh water requirement 800.0 Domestic Use 10.0 Total Water requirement for First Run 2540.0

Total Water Output for Proposed 100.0 KLD Distillery S.No Section Water required 1 Steam condensate 620.0 2 Spent wash 700.0 3 Spent leese 160.0 4 Cooling tower Evaporation 670.0 5 Blow down (Boiler Blow down) 14.0 6 Vaccum pump & sealing water 200.0 7 Miscellaneous 136.0 8 CIP Cleaning 30.0 9 Washing 10.0 Total 2540.0

Total Water Recycle for Proposed 100.0 KLD Distillery S.No Section Water required 1 Lees recycle for Dilution 100.0 2 Steam Condensate recycle 620.0 3 CPU treated Water to CT 770.0 4 Floor Wash 10.0 5 Vacuum pump water recirculation 200.0 6 CIP Cleaning 30.0 Total recycling and Utilizing 1730.0 Fresh water requirement 810.0

27 Fig 1 28 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: 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

29 Distillery Unit: 100 KLD

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

MEE CAPACITY: 1000 m3

MEE CONDENSATE: 620 KLD SLOP 200 KLD

Other Effluents: 284 KLD Boiler 30 TPH Lees, Boiler Blow Down, DM Plant Reject, Cooling Tower Blow Down, Washing, RO Reject STEAM requirement 28 tph for process , MEE and co gen of power

Condensate Treatment Unit with RO of capacity 1000 m3/day

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

Fig 3.Zero Discharge Based Treatment Strategy

30