INDEX

S. NO. CONTENTS PAGENO.

1.0 EXECUTIVE SUMMARY 1

2.0 INTRODUCTION OF THE PROJECT/BACKGROUND INFORMATION 5

3.0 PROJECT DESCRIPTION 7

4.0 SITE ANALYSIS 29

5.0 PLANNING BRIEF 31

6.0 PROPOSED INFRASTRUCTURE 32

7.0 REHABILITATION AND RESETTLEMENT (R & R) PLAN 33

8.0 PROJECT SCHEDULE & COST ESTIMATES 33

9.0 ANALYSIS OF PROPOSAL 33

i Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil , District Karnal, Pre - Feasibility Report

PRE - FEASIBILITY REPORT

1.0 EXECUTIVE SUMMARY (I) Introduction Haryana Liquors Pvt. Ltd. is one of the leading manufacturers in the Alcohol industry in North and is part of the CDB Group. Established in the year 2015, Haryana Liquors Pvt. Ltd. is engaged in manufacturing, marketing and sale of Country Liquor, Indian Made Foreign Liquor (IMFL), Bulk Alcohol and contract bottling for established IMFL brands. The Company has a well-established presence in the Country Liquor segment and is making its mark in the IMFL segment by doing contract bottling to cater to renowned Indian players. CDB Group currently operates three modern and fully integrated Distilleries at Banur & Khasa Punjab and Jundla, Haryana. It has one of the largest and most efficient grain based distilleries in India with highest alcohol recovery per unit of grain. Haryana Liquors Pvt. Ltd. is presently operating 165 KLPD Grain based Distillery along with 7.0 MW Co-generation Power Plant at Village Jundla, Tehsil Karnal, District Karnal, Haryana. Environmental Clearance for the same had been obtained from MoEFCC, New vide Letter No. J-11011/130/2011- 1A II (I) dated 17th October, 2012. The company is now proposing expansion in the capacity of existing distillery from 165 KLPD to 300 KLPD with Co-Generation Power Plant capacity of 7.0 MW to 15.0 MW by installation of Unit II – 135 KLPD Grain / Molasses Based and Co-Generation Power Plant capacity of 8MW; within their existing plant premises at Village Jundla, Tehsil Karnal, District Karnal, Haryana. As per EIA Notification dated 14th September, 2006 and as amended from time to time, the project falls under Category “A”, Project or Activity 5(g) (i) Distillery project & Category “B” , Project or Activity ‘1 (d)’ 15 MW Co-generation Power Plant. TABLE – 1 Salient Features of the Project

S. Particulars Details No. A. Nature & Size of the Units Existing Proposed Total Capacity Project Approved Expansion after Expansion Capacity Distillery 165 KLPD 135 KLPD 300 KLPD Grain Grain based Grain / based Distillery

Haryana Liquors Pvt. Ltd. 1 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Distillery Molasses or 135 KLPD based Molasses based Distillery Distillery Co- 7.0 MW 8.0 MW 15.0 MW generation Power Plant B. Category of the Project As per EIA Notification 14th Sep., 2006, as amended from time to time; the project falls under • Category “A”, Project or Activity ‘5(g)’ and • Category “B”, Project or Activity ‘1 (d)’. C. Location Details Village Jundla Tehsil Karnal State Haryana Latitude 29°39'30.38"N to 29°39'51.22"N Longitude 76°49'53.75"E to 76°50'7.07"E D. Area Details

Total Plant Area o Existing plant area: 34.7 acres (14.04 hectares) o No additional land is required for the expansion, as the same will be done within the existing plant premises. Greenbelt / Plantation 11.4 acres (4.6 ha) i.e. 33% of the plant area Area (ha) E. Environmental Setting Details (with approximate aerial distance & direction from plant site) 1. Nearest Village Katlaheri Village (~1.5 km in SSW direction) 2. Nearest City Karnal (~13.5 km in ENE direction)

3. Nearest National o SH - 12 (~2.0 km in SE direction) Highway/State Highway o SH - 8 (~2.5 km in North direction) o NH 1 (~15.0 km in East direction) 4. Nearest Railway Station Karnal railway station (~13.5 km in ENE direction) 5. Nearest Airport International Airport (~113.0 km in North direction) 6. National Parks/ Wild Life No National Parks/ Wild Life Sanctuaries / Biosphere Reserves, Sanctuaries / Tiger/ Elephant Reserves, Wildlife Corridors, Reserved / Biosphere Reserves, Protected Forest within 10 km radius Tiger/ Elephant Reserves, Wildlife Corridors / Reserved / Protected Forest within 10 km radius

7. Nearest Water Bodies o Indri Drain (Adjacent in West) o Major Distributary (~5.0 km in NW direction) o Western Canal (~8.5 km in SE direction)

Haryana Liquors Pvt. Ltd. 2 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

o Nadi (~9.0 km in West direction) Many agricultural minors are present in 10 km radius. 8. Seismic Zone Seismic Zone - III as per IS: 1893 (Part-I): 2002. F. Cost Details Total Cost of the Rs. 92.0 Crores Expansion Project

Cost for Environment o Capital Cost - Rs. 40.90 Crores Management Plan o Recurring Cost - Rs. 0.70 Crores / annum. G. Basic Requirements for Existing Additional for Capacity Total after the project Expansion Capacity Expansion Water Requirement 825 675 1500 (KLD) Source: Ground Water Power Requirement 3.0 2.5 5.5 (MW) Source: Co-Generation Power Plant Man Power Requirement 110 90 200 Source: Unskilled / Semi-Skilled - Nearby Areas; Skilled – Within or Outside Haryana H. Product Mix Rectified Spirit, Extra Neutral Alcohol & IMFL/CL Bottling

I. By-product DDGS & CO2 J. Working Days 350 Days per Annum

1.1 ENVIRONMENTAL MANAGEMENT PLAN Particulars DETAILS Air Quality Management Ø Bag filter with stack of adequate height has been installed with the existing boiler to control the particulate and gaseous emissions due to combustion of fuel. Ø ESP will be installed with the proposed 45 TPH boiler to keep the emissions below permissible level after expansion. Ø CO2 generated during the fermentation process is being/will be collected by utilizing CO2 scrubbers and sold to authorized vendor. Ø All the roads are being / will be concreted to control the fugitive dust emissions. Ø Online Stack Monitoring system is already in place and operational. Ø Greenbelt is being/will be developed all around the plant boundary and the same will be maintained. Water Management Ø The Grain & Molasses based distillery is being/will be based on “Zero Effluent Discharge”.

Haryana Liquors Pvt. Ltd. 3 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Grain based operation: Ø Grain Slops (Spent Wash) is being/will be taken through Centrifuge Decanters for separation of Suspended Solids separated as Wet Cake and which goes as cattle feed as it contains high protein. (Also known as DWG – Distillers Wet Grains) Ø Thin Slops from the Decanter Centrifuge is being/will be partly recycled back to process and balance portions shall be taken to Thins Slops Evaporation Plant for concentration of remaining solids to form a Syrup. This Syrup is also mixed into the Wet Cake coming out of Centrifuge and forms part of Cattle Feed. (Also known as Soluble - Collectively known as DWGS). Ø DWGS Drier - Wet cake / DWGS is being passed through steam tube bundle drier for drying into cake with 10 - 12% moisture (max.) to give higher shelf life. Solid dry cakes are being obtained finally. Ø The Process condensate is being / will be cooled and sent to CPU. After treatment this process condensate is being / will be recycled into process use.

Molasses Based Operation: Ø The spent wash will be concentrated in MEE and the concentrated spent wash will be mixed with auxiliary fuel and burnt in the incinerator boiler. Ø Process Condensate will be neutralized and treated in state of art Condensate Polishing Unit (CPU) and recycled in Fermentation process and for Cooling Tower makeup. Ø Domestic waste water generated from the plant is being/will be treated in STP. Ø Rain Water harvesting is being done within the existing plant premises. Noise Management Ø Personal Protective Equipment like earplugs and earmuffs is being / will be provided to the workers exposed to high noise level. Ø D.G sets are being /will be provided with acoustic hoods to control the noise level within the prescribed limit. Ø Proper maintenance, oiling and greasing of machines at regular intervals is being / will be done to reduce generation of noise. Ø Greenbelt of appropriate width inside the plant premises and at the plant boundary has been developed. Ø Regular monitoring of noise level is being / will be carried out and corrective measures in concerned machinery are being/will be adapted accordingly to the possible extent.

Haryana Liquors Pvt. Ltd. 4 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Solid Waste Management Ø Solid waste from the grain based operations generally comprises of Fibres and proteins in the form of DDGS, which is ideally used as Cattle Feed. The Yeast sludge is added to the Wet Cake. Ø The concentrated spent wash from molasses based distillery will be burnt in incinerator boiler along with biomass as fuel (15% coal will also be used as auxiliary fuel). Ø Ash from the boiler is being /will be given to nearby brick manufacturers. Ø Used oil generated from the plant machinery/ gear boxes as hazardous waste is being/will be sold out to the CPCB authorized recycler. Odour Management Ø Adequate greenbelt all around the periphery of the plant. Ø Efficient CO2 scrubbing to avoid carryover of alcohol vapours & other fumes. Ø DWGS Dryer is being/will be installed for complete drying of solids. Ø Better housekeeping is being/will be maintained with good hygiene condition by regular steaming of all fermentation equipment. Ø Longer storages of any product/by-products will be avoided & use of efficient biocides to control bacterial contamination. Ø Regular use of bleaching powder/formalin in the drains to avoid generation of putrefying micro-organisms. Greenbelt Development/ Plantation Ø Greenbelt development in and around the plant site helps to attenuate the pollution level. Ø The company has already developed greenbelt/ plantation in 33% of the total plant area and the same will be further maintained. Ø Greenbelt has been developed as per Central Pollution Control Board (CPCB) guidelines. Ø Native species have been planted in consultation with the local DFO.

2.0 INTRODUCTION OF THE PROJECT/ BACKGROUND INFORMATION (i) Identification of Project and Project Proponent Applicant : M/s Haryana Liquors Pvt. Limited. Registered Address : Village Jundla, Tehsil and District Karnal, Haryana. Haryana Liquors Pvt. Ltd. has enjoyed a good track record in the business of manufacture, marketing and sale of Country Liquor, Extra – Neutral Alcohol, Industrial Alcohol comprising Rectified Spirit & contract bottling of Indian Made Foreign Liquor (IMFL) for reputed brands.

Haryana Liquors Pvt. Ltd. 5 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

With headquarters in Chandigarh, the company markets its own Country Liquor in state of Haryana. Company also is selling excellent quality ENA in various other states. Haryana Liquors Pvt. Ltd. is presently having the Environmental Clearance for 165 KLPD Grain based / 55 KLPD Molasses based Distillery along with 7 MW Co-Gen Power Plant at Village Jundla, Tehsil Karnal, District Karnal, Haryana. Environmental Clearance for the same had been obtained from MoEFCC, New Delhi vide Letter No. J-11011/130/2011- 1A II (I) dated 17th October, 2012. (ii) Brief description of nature of the project The company is now proposing Expansion of Existing Distillery capacity 165 KLPD to 300 KLPD with Co-Generation Power Plant capacity of 7.0 MW to 15.0 MW by installation of Unit II – 135 KLPD Grain / Molasses Based and Co-Generation Power Plant capacity of 8 MW; within their existing plant premises at Village Jundla, Tehsil Karnal, District Karnal, Haryana. The Proposed expansion capacity of 135 KLPD will be Grain based and Molasses based alcohol using Grain & Molasses as raw materials which are abundantly available in the state. The Project is based on zero effluent discharge. The distillery has put up the most modern technology for treatment of distillery spent wash which ensures Zero discharge of distillery effluents. The distillery unit will generate its own electricity by proposed additional Co-Generation power plant of 8.0 MW and sell the surplus power to the State Electricity Board. (iii) Need for the project and its importance to the country and or region Advancement in science and technology has created so many products that have enhanced the quality of human life in every passing year. The human race is largely dependent on industrialization for up gradation in quality of life. Progress of the nation is judged through its economic growth which is largely dependent on industrial productivity. In Indian economy (which is agro based) many industries are dependent over agricultural produce for production of luxury and need based commodities. Alcohol has assumed a very important place in the Country’s economy. It is a vital raw material for a number of chemicals. It has been a source of revenue by way of excise duty levied by the State Government on alcohol liquors. It has a potential as fuel in the form of power alcohol for blending with petrol in the ratio of 20:80. The use of alcohol for the purpose of potable liquor is as high as its use for industrial purposes. The Country Liquor is mainly used by the common masses. According to analysts, the Indian alcoholic beverages industry is expected to witness

Haryana Liquors Pvt. Ltd. 6 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

accelerating growth in coming years with the consumer base likely to expand amidst rising disposable income. The domestic alcoholic drinks market is estimated around $13 billion and has been growing at a compounded annual growth rate in excess of 10% in the past few years. The growth rate is higher than other major Asian markets like China and South Korea, etc. In the path of company’s growth and development this project will serve as yet another milestone. (iv) Demand- Supply Gap The total production of ENA from molasses and grain is about 300 crores litres per annum. The total requirement of ENA for IMFL in India is around 120 crores litres (35% ENA from grain & 65 % from molasses). Next five year projection of ENA from grains is 60 % & from molasses is 40 %. Alcohol produced from molasses is also used by oil companies and 111 crores litres has been procured in the year of 2016-17. Post 2017 India will require 6.30 billion litres of alcohol mainly from molasses for the use in petrol by the oil companies. Thus the huge demand of ENA will arise. (v) Import vs. Indigenous Production Indian market could not meet present alcohol demand. So 5-7 % of total demand of alcohol was imported. As far as ENA production is concerned, Indian market plays a vital role at both domestic & international level. So they need to produce more alcohol to meet the demand. (vi) Export Possibility There will be possibility of export of alcohol to African, European & Asian countries. (vii) Domestic / Export Markets Market depends on Excise Department. (viii) Employment Generation (Direct and Indirect) due to the project The total manpower requirement after the expansion & installation project will be 200.

3.0 PROJECT DESCRIPTION (i) Type of Project including interlinked and independent projects, if any. There are no interlinked projects related to this expansion project. (ii) Location (map showing general location, specific location, and project boundary & project site layout) with coordinates

Haryana Liquors Pvt. Ltd. 7 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Figure - 1: Location Map

Haryana Liquors Pvt. Ltd. 8 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

(iii) Key Plan

Figure 2: Environmental Settings of 10 km radius area

Haryana Liquors Pvt. Ltd. 9 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

(iv) Details of alternative sites consideration and basis of selecting the proposed site, particularly the environmental considerations gone into should be highlighted. Since the proposed expansion will be done within the existing plant premises and no additional land will be required; therefore, no alternative site has been considered. (v) Size or magnitude of operation The company is now proposing Expansion of Existing Distillery capacity 165 KLPD to 300 KLPD with Co-Generation Power Plant capacity of 7.0 MW to 15.0 MW by installation of Unit II – 135 KLPD Grain / Molasses Based and Co-Generation Power Plant capacity of 8 MW; within their existing plant premises at Village Jundla, Tehsil Karnal, District Karnal, Haryana. The process includes basic raw material requirement, sizing of equipment, utilities & services, infrastructure facilities & sources of waste generation, their quantity, treatment & safe disposal of the waste.

Units Existing installed Proposed Expansion Total Capacity after Capacity Proposed Expansion Distillery 165 KLPD Grain 135 KLPD Grain / Molasses 300 KLPD Grain based based Distillery based Distillery Distillery or 135 KLPD Molasses based Distillery Co-generation 7.0 MW 8.0 MW 15.0 MW Power Plant IMFL/CL Bottling 48 lac cases per Nil 48 lac cases per annum Plant annum

(vi) Project Description with Process Details Process Description of Grain Based Distillery Operation A) Grain Storage Silos, Cleaning, Handling and Milling Section: Grain is received from various sources and is pre-cleaned off stones, husk, etc. and then stored in specially designed storage silos or in bags in storage yard. Grains are continuously lifted from the bottom of the silos, screened and followed by removal of stones in de-stoner and iron matters in magnetic separators. Cleaned Grains are then milled using dry milling process in Hammer Mills. The flour is fed through the bucket elevator and conveyed to the flour silo.

Haryana Liquors Pvt. Ltd. 10 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

B) Liquefaction Section Grain flour is mixed with recycle streams and water in Pre-masher and slurry is fed to Liquefaction tank. Required temperature is maintained by applying steam through steam sparger in liquefaction tank. The cooking process, accomplished in the above manner, converts the slurry into a hydrated, sterilized suspension (as starch molecule is solubilized) and is therefore susceptible to enzyme attack for liquefaction. The liquefied mash is cooled in slurry cooler and transferred to Fermentation section. C) Fermentation Section The purpose of fermentation is to convert the fermentable substrate into alcohol. To prepare the mash for fermentation, it is diluted with water. Yeast is added in sufficient quantity to complete fermentation to produce alcohol. At the start of the cycle, the Fermenter is charged with mash and contents of the Yeast Activation Vessel (Pre-fermenter). Significant heat release takes place during fermentation. This is removed by passing the mash through heat exchangers to maintain an optimum temperature. The recirculation pumps also serve to empty the Fermenters into Beer Well. CO2 evolved during fermentation carries along with it some entrained alcohol. This CO2 is taken to a CO2 scrubber where it is washed with water to remove the entrained alcohol. The scrubbed CO2 can then be taken to CO2 plant or vented out. After emptying of Fermenter, it is cleaned with CIP using cleaning nozzles. After CIP Fermenter is ready for next batch to be filled. D) MPR Distillation Wash to ENA: Multi-Pressure Distillation system has eight Distillation columns operating at various pressure conditions. Heat energy from columns operating under high pressure is utilized for columns operating under low pressure to optimize the operation for energy consumption. Following Columns will be under operation Ø Analyser Column Ø Degasifying Column Ø Pre-Rectifier Column cum Ø Exhaust Column Ø Extractive Distillation Column Ø Rectifier cum Exhaust Column Ø Recovery Column Ø Simmering Column

Haryana Liquors Pvt. Ltd. 11 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Pre-heated fermented wash is fed at the top of the Degasifying column. Analyser Column is provided with Reboiler. Top vapors of Analyser column containing all the alcohol in the wash are sent to Pre-Rectifier column. Rest of the fermented wash flows down the Analyser column and is taken out as thick slops from Analyser column bottom. Low boiling impurities are concentrated in the Pre-Rectifier column. A draw of impure alcohol is taken out from the top of the Pre-Rectifier column. RS draw is taken from the top of Pre rectifier column, which further is sent to Extractive Distillation column. Dilution water is fed to this column. The Extractive Column operates on the principle of inversion of relative volatility. Low boiling impurities are separated in the Extractive Distillation Column & bottom is sent to Rectifier cum Exhaust column. The Rectifier/Exhaust column concentrates the alcohol to 96% v/v. The spirit is drawn from the upper trays of the Rectification Column. Fusel oil build up is avoided in the Rectifier cum exhaust column by withdrawing side streams (fusel oils). ED condensates, fusel oil draw from R/E column are sent to Recovery column where these fusel oils are concentrated and then sent to decanter where these streams are diluted with water and fusel oil rich layer is separated. Washings are sent back to the column to recover alcohol. The spirit Draw from the Rectifier column is sent to the Simmering column where methanol is separated in the form of a cut from the top and ENA is taken out from the bottom. ENA drawn from the Simmering Column is taken to the receiver after cooling in ENA cooler. E) Decantation Section Excluding Decanter Centrifuges Decantation section comprises of a Centrifuge Decanters for separation of suspended solids from Thick slop coming out of Grain Distillation Plant. Wet cake is removed from bottom of Decanter. Thin slops coming out of Decanter are collected in a tank and partly recycled into the process & balance to Evaporation for further concentration. The concentrated thin slops called as Syrup is mixed with Wet cake and sold in wet form as cattle feed (DWGS) or the entire mixture can be dried in a DWGS Dryer and then sold in dry form as Cattle feed (DDGS). F) Integrated Evaporation The suggested treatment scheme is a Multi Effect Evaporation Plant for Thin Slop Evaporation. Shell & Tube type Evaporators with highly efficient liquid distributor working on the principle of Falling Film and Forced circulation Evaporation are being used.

Haryana Liquors Pvt. Ltd. 12 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

The product at the desired concentration of 30%w/w Total Solid is obtained at the outlet of the final effect. Each effect is provided with recirculation cum transfer pumps. The condensate from surface condensers is collected in a common condensate pot. The condensate is transferred for further treatment by using centrifugal pump. The system operates under vacuum. Water-ring vacuum pumps are used to maintain a desired vacuum. Cooling water from cooling tower is used in the surface condensers for condensing the vapours. G) DWGS Dryer Section Wet distiller’s grains shall be fed into the dryer housing at controlled rate through a suitable feeding system. The Rotary Bundle is enclosed in an insulated dryer housing and on its outer flights are fixed. Dry, saturated steam is to be supplied to the bundle through rotary joint at one end & the condensate is discharged through rotary joint mounted of another end. During the course of rotation, these flights pick up the material and shower them on to the tube bundles. The heat transfer is primarily by conduction. The water vapors are exhausted through an Exhaust Blower & passed through a cyclone separator for separating fines. Dry product partially recycled back to feed conditioner for feed conditioning through Product Screw & Recycle Conveyor. Entire operation of the Dryer is controlled through Local Indication cum Control panel. G) Process Condensate Treatment Section The process condensate from the evaporation section is treated in this unit and this treated condensate is then recycled back to process thus reducing the fresh water consumption.

Haryana Liquors Pvt. Ltd. 13 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Figure 3:- Process flow diagram of Grain based Distillery FOR MOLASSES BASED OPERATION i) Molasses Unloading and Storage Molasses from tankers will be unloaded at unloading point and transferred in to molasses storage tank. ii) Fermentation: Yeast Activation: Yeast seed material is prepared in water-cooled Yeast Activation Vessel by inoculating sterilized mash with Active Dry Yeast. Optimum temperature is maintained by cooling water. The contents of the Yeast Activation Vessel are then transferred to Pre - Fermenter. Fermentation: The Molasses from storage tank is pumped to Dilutor installed in Fermentation section and diluted with water. The diluted Molasses called Wort is fed into Pre Fermenter for activation of Yeast. The activated yeast from the Yeast activation vessel is transferred into pre fermenter. Once the yeast is activated in Pre fermenters it will be transferred in to fermenters and diluted molasses is to be add. The process of fermentation is to convert the fermentable substrate into alcohol. The pH of the wort is adjusted by the addition of

Haryana Liquors Pvt. Ltd. 14 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

acid. Yeast is available in sufficient quantity to initiate fermentation rapidly and complete it within the cycle time. Significant heat release takes place during fermentation. This is removed by passing cooling water through the Fermenter PHE’s to maintain an optimum temperature. The recirculating pumps also serve to empty the fermenters into Beer Well. After the fermenters are emptied, they are cleaned with water and sterilized for the next batch. The carbon dioxide evolved during the process is vented to atmosphere after recovery of alcohol in a scrubber. iii) Distillation: Fermented wash from wash holding tank / beer well is pumped by wash feed pump to the top of degassing column after preheating the same in beer heater and spent wash heat exchanger. The vapours along with non-condensable gases from the top of degassing column are rectified in Heads column, to expel the high volatiles, technically known as heads. Bottom liquid from the degasser flows into analyzer column where alcohol is stripped from the liquid. The liquid from bottom of analyzer column is completely stripped of alcohol and is pumped out by thick slop discharge pump through heat exchanger where it preheats the fermented wash before it enters degassing column. The slop from the analyser column will be feed in to MEE. The dilute alcohol vapours from near the top of analyzer column are condensed first in beer heater while exchanging heat with wash feed and then in analyzer condenser. Degasser and analyzer operate under vacuum. The condensate from beer heater and analyser condenser is collected in Rectifier Feed Tank. The vapours for stripping alcohol are generated from analyzer column bottom liquid in the analyzer column re- boiler by using the rectified column top vapours, as discussed subsequently. Vapours from the top of heads column are condensed in heads column condenser and then in head column vent condenser. Part of the condensate is returned to column as reflux while a small portion is taken out as an impure spirit cut. Liquid from bottom of heads column is also taken into Rectifier feed tank. Dilute alcohol water mixture from rectifier feed tank is pumped by rectifier feed pump through rectifier feed pre-heater in to rectifying column. Rectifier and its associated equipment work under pressure so that these vapours can supply the necessary heat for generating the vapours.

Haryana Liquors Pvt. Ltd. 15 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

The condensate from analyser column reboiler is then pumped as Reflux to rectifying column. Rich alcohol vapors at a concentration of 95.5% v/v from top of rectifying column are condensed first in Analyzer reboiler and then in Reflux Vent Condenser. The liquid is then collected in Rectifier Reflux Tank. Part of the liquid from vent condenser may be drawn off as impure spirit. The impure spirit cut will be maintained as little as possible to maintain aldehyde levels to meet the required limits in Absolute Alcohol. Liquid from the rectifier reflux tank is pumped by Product Pump partly as product and partly as reflux to the top of the Rectifying Column. The necessary rectifying vapours to rectifying column are generated by boiling the bottom liquid in Rectifier Column Re-boiler by using medium pressure steam. Some side streams are drawn from rectifier column as light and heavy fractions of higher alcohols called fusel oils and cooled in fusel oil coolers. These are mixed with water and allowed to separate out in fuel oil separator. All vents from condensers are connected to Vent Gas Absorber where the vent gases are scrubbed with water to recover entrained alcohol. The scrubber water is used for washing the fuel oils in fuel oil separator to recover alcohol from the fuel oil fractions. The absorber vent is connected to vacuum pump which is used to create vacuum in the respective columns. The remaining process is same as mentioned under grain based distillation and the product ENA shall be sent for storage. iv) Alcohol Daily Receivers & Bulk Storage: Alcohol is first taken to Daily receiver storage a tank is thereafter transferred to Bulk Storage Tanks after taking the daily receiver Dip. This is transferred using flameproof pumps. Final dispatch of alcohol is again carried out using special flameproof pumps. EFFLUENT HANDLING SECTION i) Evaporation Section: The spent wash coming from Distillation section will be fed in to first calendria of the evaporator section. The multi effect evaporator (MEE) shall be designed to concentrate the dissolved solids. Suggested treatment scheme is FF + Finisher Evaporation Plant for spent wash Evaporation. The following points will elucidate the basic working principle: v Shell & Tube type Evaporators with highly efficient liquid distributor working on the principle of Falling Film & Forced Evaporation have been used, with

Haryana Liquors Pvt. Ltd. 16 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Preheaters for preheating of FEED stream which serves the purpose of energy conservation. v Vapours generated in 1st effect VLS (Vapour Liquid Separator) are used as heat source in the 2nd effect and from 2nd to third and so on. v The product at the desired concentration of TS is obtained at the outlet from the final effect, v A Shell & tube type Multi-pass Surface condenser is employed for condensing the shell side vapours. v The Pure and the process condensate are collected in receiving vessels. v Highly efficient operating pumps will be provided for pumping the required fluid. v The operation of the plant will be under vacuum. Vacuum is created with the help of a water ring vacuum pump. v The plant will have high level of automation to get consistent output at required concentration. v Cooling water from cooling tower is used in the surface condensers for condensing the vapours. ii) Incinerator boiler: The concentrated molasses based effluent shall be burnt in Incinerator boiler along with other Biomass fuels (15% coal will also be used as auxiliary fuel) to generate high pressure steam.

Figure 4:- Process flow diagram of Molasses based Distillery

Haryana Liquors Pvt. Ltd. 17 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

B) Power Co-Generation (7 MW + 8 MW = 15.0 MW) OPERATIONS Presently, with the approved capacity 7.0 MW, the Co-generation section is operating on various biomasses (15% coal will also be used as auxiliary fuel) such as Rice Husk/ paddy straw/ cow dung/ poultry waste etc. After expansion capacity of co-generation power plant will be 15 MW which will also be based on same fuel as existing. Co-generation plant consists of a high pressure water tube steam boiler with extraction cum condensing steam turbine. Fuel in the steam boiler will be burnt with the help of air in the boiler furnace. Water will be circulated in the boiler drum and tubes thus getting heated by the flame burning in the boiler furnace. Water comes out of the boiler drum located at the top of the boiler as steam. Flue gases rise in the boiler furnace and come in contact with the steam coming out of boiler drum. Steam after coming in contact with flue gases gets heated up further thus getting superheated. Super heated steam leaves the boiler in a pipe. Flue gases after super heating the steam pass through economizer where they pre-heat the boiler feed water before it enters the boiler drum. After economizer, flue gases pass through air pre-heaters where they heat the air which is fed to the boiler furnace for burning the fuel. After air pre heaters flue gases pass through an ESP where the dust particles are collected on charged electrodes. The dust is collected from the bottom of the ESP. High pressure superheated steam from boiler is passed through a steam turbine, which is used for distillery process operations. While passing through the turbine, the high pressure and temperature steam rotates the turbine rotor and an electric alternator mounted on the same shaft. Electric power is generated by the alternator. This electric power generated is consumed in house i.e. for running the distillery and utilities like boilers auxiliaries etc. Surplus power can be exported to Grid.

Haryana Liquors Pvt. Ltd. 18 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Figure 5: Process flow chart for Proposed Co-generation Power Plant vii) Raw material required along with estimated quantity, likely source, marketing area of final products, mode of transport of raw material and finished product. (a) Raw Material Requirement The basic raw material for the manufacturing of ENA/RS will be Grain and Molasses. In the present scenario, grains with different starch content are used like broken Rice, sorghum, bajra, maize etc. The process requires the above grains to be milled into specific flour size. Small quantities of micro-nutrients & other chemicals are required. Molasses from sugar mills containing sugar shall also be used. The raw material for the boiler fuel will be various biomasses (15% coal will also be used as auxiliary fuel) such as Rice Husk/ paddy straw/ cow dung/ poultry waste etc and concentrated spent wash for incineration when the distillery is operated on molasses.

Haryana Liquors Pvt. Ltd. 19 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Table - 2 Raw Material Requirement S. Particulars Requirement Source & Mode of No. Existing Additional for Total after Transportation proposed proposed expansion expansion 1 Grain - Broken Rice, 360 300 MT/day 660 MT/day Through Grain Sorghum, Bajra, MT/day suppliers By Maize etc. road/Rail 2. Molasses 628 MT/day 628 MT/day From suppliers by tankers (road) 3. Chemicals (kg/day) Near-by Markets Sodium Hydroxide 250 200 kg/day 450 kg/day /by road kg/day Liquefying Enzyme 120 100 kg/day 220 kg/day kg/day Saccharifying Enzyme 98 82 kg/day 180 kg/day kg/day Liquor Ammonia 600 480 kg/day 1080 kg/day kg/day Antifoam Agent 65 50 kg/day 115 kg/day kg/day Yeast (Active Dry 120 100 kg/day 220 kg/day Yeast/Distiller’s Yeast kg/day

(b) Fuel Requirement TABLE – 3 Fuel Requirement Name of Raw Requirement Source & Mode of Material Existing Additional for Total Quantity after Transportation Proposed Proposed Expansion Expansion Rice husk & 340 340 TPD 680 TPD From suppliers by other biomasses TPD truck 15% coal will also be used as auxiliary fuel

(viii) Resources optimization/ recycling and reuse envisaged in the project, if any, should be briefly outlined. Water as a resource will be recycled at each possible step of the process and latest technology and methodology will be adopted to conserve and reuse the resources.

Haryana Liquors Pvt. Ltd. 20 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

(ix) Availability of water it’s source, energy /power requirement and source should be given. (a) Water Requirement and Source Existing water requirement for 165 KLPD Grain Based Distillery is 825 KLPD. TABLE – 4 FRESH WATER REQUIREMENT Existing Water Additional water Total water requirement requirement for requirement after Expansion expansion Grain based Distillery & Co- 825 KLPD 675 KLPD 1500 KLPD gen Power Plant & Bottling Plant Molasses based Distillery Nil 1455 KLPD 1455 KLPD & Co-gen Power Plant & Bottling Plant Source of Water: Ground Water.

Water balance for 300 KLPD Grain based Distillery along with 15 MW Co-generation power Plant & Bottling Unit Total fresh water requirement for the after expansion project is 1500 m3/day. Water requirement for first run would be 6210 m3/day when operating on Grain, which will be reduced through recycling of 4710 m3/ day of treated water/ Condensates. Water requirement for the proposed project will be met from ground water as well as recycled water. Permission for ground water extraction has already been granted. Fresh Water Requirement for the Project S. No. Operation Water required 1. 300 KLPD Grain Based Distillery 1500 m3/day with Blending & Bottling and 15 (Net fresh water after recycle) MW co-generation power

The details worked out are given below: WATER REQUIREMENT FOR GRAIN BASED OPERATION S. No. Description Water Consumption (KLD) 1 Process Water In Liqn & Fermentation 1490 2 Water for dilution 900 3 DM water for boiler feed 2160 4 Blending 75 5 Bottle Washings 50 6 Makeup for Cooling Tower 1525 7 Other Domestic Usage 10 Total Water Requirement (A) 6210

Haryana Liquors Pvt. Ltd. 21 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

TOTAL WATER OUTPUT

S. No. Description Water Consumption (KLD) 1 Steam Condensate 2040 2 Spent Lees 1160 3 Water In DWGS/ Syrup/ Product 350 4 Bottle Washing 50 5 MEE condensate 1000 6 CT evaporation & drift losses 1525 7 Blending 75 8 Domestic Consumption 10 Total (B) 6210

RECYCLING & UTILIZATION STREAM

S. No. Recycle& Utilization Streams Water Consumption (KLPD) 1 Lees Recycle 1160 2 Steam Condensate Recycle 2040 3 CPU treated condensates 1000 4 Bottle washing 50 5 Thin Slops Recycle 460 Total Recycling /Re-utilizations of water per day (C) 4710 Total Fresh Water Input (A-C) 1500

Haryana Liquors Pvt. Ltd. 22 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Figure 6: Water Balance 300 KLPD Grain Based Distillery with Blending & Bottling and 15 MW co-generation power

Haryana Liquors Pvt. Ltd. 23 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Water balance for 135 KLPD Molasses based Distillery along with Co-generation power Plant & Bottling Unit Total fresh water requirement for the proposed project is 1455 m3/day. Water requirement for first run would be 4360 m3/day when operating on molasses, which will be reduced through recycling of 2905 m3/ day of treated water/ Condensates. Water requirement for the proposed project will be met from ground water as well as recycled water. Permission for ground water extraction has already been granted. Fresh Water Requirement for the Project

S. Operation Water required No. 1. 135 KLPD Molasses Based Distillery with 1455 m3/day Blending & Bottling and 15 MW co- (Net fresh water after generation power recycle)

The details worked out are given below: WATER REQUIREMENT FOR MOLASSES BASED OPERATION

S. No. Description Water Consumption (KLD) 1 Water In Molasses & Fermentation 1200 2 Water for dilution 405 3 DM water for boiler feed 1340 4 Blending 75 5 Bottle Washings 50 6 Makeup for Cooling Tower 1280 7 Other Domestic Usage 10 Total Water Requirement (A) 4360

TOTAL WATER OUTPUT

S. No. Description Water Consumption (KLD) 1 Steam Condensate 1340 2 Spent Lees 535 3 Water In Conc. Spent wash / Product 90 4 Bottle Washing 50 5 MEE condensate 980 6 CT evaporation & drift losses 1280 7 Blending 75 8 Domestic Consumption 10 Total (B) 4360

Haryana Liquors Pvt. Ltd. 24 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

RECYCLING & UTILIZATION STREAM

S. No. Recycle& Utilization Streams Water Consumption (KLPD) 1 Lees Recycle 535 2 Steam Condensate Recycle 1340 3 CPU treated condensates 980 4 Bottle washing 50 Total Recycling /Re-utilizations of water per day (C) 2905 Total Fresh Water Input (A-C) 1455 * Water requirement for first run would be 4360 KLD Hence, looking to the above for both grain and molasses based operations, the total fresh water requirement is 1500 KLD

Haryana Liquors Pvt. Ltd. 25 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Figure 7: Water Balance 135 KLPD Molasses Based Distillery with Blending & Bottling and 15 MW co-generation power

Haryana Liquors Pvt. Ltd. 26 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

(b) Power Requirement and Source Existing power requirement is 3.0 MW and additional 2.5 MW of power will be required for proposed Expansion. Thus, the total power requirement after proposed expansion & installation project will be 5.5 MW. Source: Existing approval for 7.0 MW and additional proposed 8.0 MW Co-generation Power Plant & D.G Sets (for back-up). Surplus power shall be exported to the State Electricity Board. (c) Steam Requirement Existing steam requirement for 165 KLPD distillery capacity is being met by existing approved boiler capacity of 45 TPH and after proposed expansion additional boiler of 45 TPH capacity shall be installed which be suitable for incineration of molasses spent wash and other biomasses (15% coal will also be used as auxiliary fuel) in a single/ twin furnace. (d) Boiler Details Existing approved and proposed boiler details are mentioned in the table given below: TABLE – 5 Boiler Details S. Boiler Details Existing Proposed No. 1. Boiler Capacity 45 TPH 45 TPH 2. Type of Fuel Biomasses Biomass / Conc. (15% coal will also Molasses spent wash be used as (15% coal will also be auxiliary fuel) used as auxiliary fuel) 3. Stack Height 52 metres 52 meter 4. Pollution Control Equipment Bag Filter ESP Measures

(e) Details regarding the D.G. Sets Two D.G. sets of 1000 KVA have already been installed for the power backup and after proposed expansion additional 1 D.G sets of 1000 KVA will be installed. Details regarding the D.G. Sets are mentioned in the table given below:

Haryana Liquors Pvt. Ltd. 27 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

TABLE – 6 DETAILS REGARDING THE D.G. SETS

S. Details Existing Proposed No. 1. Type of Fuel Diesel Diesel 2. Capacity 2 x 1000 KVA 1 x 1000 KVA 3. Stack Height (above roof As per CPCB As per CPCB level) guidelines guidelines

(x) Quantity of waste to be generated (liquid and solid) and scheme for their management/disposal

o The proposed expansion & installation project is being/will be based on “ZERO EFFLUENT DISCHARGE”.

o Grain Slops (Spent Wash) is being/will be taken through Centrifuge Decanters for separation of Suspended Solids separated as Wet Cake.

o Thin Slops from the Decanter Centrifuge are being/will be partly recycled back to process and balance taken to Thins Slops Evaporation Plant for concentration of remaining solids to form Syrup. This Syrup is mixed with the Wet Cake coming out of Decanter Centrifuge and forms part of Cattle Feed. (Also known as Distillers Wet Grain Solubles - Collectively known as DWGS)

o DWGS is being/will be taken to a dryer operating on steam and is dried to make it DDGS – Distillers Dried Grain Solubles.

o The process condensate is being/will be cooled and taken to CPU. The treated water is then recycled into process and/ or used for greenbelt development within the complex.

o Molasses slops (spent wash) shall be concentrated in evaporators and incinerated in boiler.

o Solid waste from the Grain based operations generally comprises of Fibres and proteins in the form of DDGS, which are being / will be ideally used as Cattle Feed.

o Fly Ash from the Boiler is being / will be sold to brick/cement manufacturers. o Used oil & grease generated from plant machinery / Gear boxes & D.G. Set is being / will be partly used in oiling & greasing as lubrication of external parts of machinery & partly is being / will be sold to the CPCB authorized recycler.

Haryana Liquors Pvt. Ltd. 28 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

4.0 SITE ANALYSIS (i) Connectivity The project site is located at Village Jundla, Tehsil & District Karnal, Haryana and is well connected with state highway SH-12 & SH - 8 and National Highway NH 1 from the project site. Nearest Railway Station is Karnal, which is about 13.5 km in ENE direction from the project site. Nearest Airport is at Chandigarh which is approx. 113 km in North direction. It has an easy access to raw material availability and other infrastructural facilities e.g. land, power, water, transport and communication, approach through road & access distances from the nearest highway, railway station etc. (ii) Land from Land use and Land ownership Total plant area is 34.7 Acres (14.04 ha). Since, the proposed expansion & installation will be done within the existing plant premises, thus, no additional land is required for the same. (iii) Topography The topography of the area is almost flat. (iv) Existing land use pattern (agriculture, non-agriculture, forest, water bodies (including area under CRZ)), shortest distances from the periphery of the project to periphery of the forests, national park, wild life sanctuary, eco sensitive areas, water bodies (distance from the HFL of the river), CRZ. In case of notified industrial area, a copy of the Gazette notification should be given Environmental Settings of the Area

S. PARTICULARS DETAILS NO. 1. Nearest Village Katlaheri Village (~1.5 km in SSW direction) 2. Nearest City Karnal (~13.5 km in ENE direction)

3. Nearest National Highway/State o SH - 12 (~2.0 km in SE direction) Highway o SH - 8 (~2.5 km in North direction) o NH 1 (~15.0 km in East direction) 4. Nearest Railway Station Karnal railway station (~13.5 km in ENE direction) 5. Nearest Airport Chandigarh International Airport (~113.0 km in North direction) 6. National Parks/ Wild Life Sanctuaries No National Parks/ Wild Life Sanctuaries / / Biosphere Reserves, Tiger/ Elephant Reserves, Biosphere Reserves, Tiger/ Elephant Wildlife Corridors, Reserved / Protected Forest Reserves, Wildlife Corridors / within 10 km radius

Haryana Liquors Pvt. Ltd. 29 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Reserved / Protected Forest within 10 km radius

7. Nearest Water Bodies o Indri Drain (Adjacent in West) o Nardak Major Distributary (~5.0 km in NW direction) o (~8.5 km in SE direction) o Chautang Nadi (~9.0 km in West direction) Many agricultural minors are present in 10 km radius. 8. Seismic Zone Seismic Zone - III as per IS: 1893 (Part-I): 2002.

(v) Existing Infrastructure Total plant area is about 34.7 Acres (14.04 ha). Proposed expansion & installation will be done within the existing plant premises. Existing infrastructure comprises of Grain based Distillation & Fermentation unit and basic utilities such as water, power, etc. (vi) Soil classification The Chantang Nala is the other drainage line and flows from north to southwest in the western part of the district and disappears near . The soils in and SE half of Karnal blocks are young, stratified with no profile development. They are sandy to fine sandy loams. The soils in SE half of , SW extremity of Karnal block touching Nilokheri, eastern portion of Nissang, Western half of Gharaunda block are heavily textured varying from sandy loam at the surface to clayey loam at about one meter depth. (vii) Climatic data from secondary sources The climate of the district is characterized by the dryness of the air with an intensely hot summer and a cold winter. The year may be divided in to four seasons. The cold season starts by late November and extends to the middle of March. It is followed by hot season which continues to the end of June when the southwest monsoon arrives over the district. July to September is the southwest monsoon season. The post monsoon season period is from October to December. The normal annual rainfall of the district is 582mm recorded in 32 rainy days in a year. About 82.39% of the annual rainfall is recorded during the southwest monsoon from July to September. August is the wettest month of the year with an average of 9.0 rainy days and 221.5 mm rainfall. Maximum rainfall of 1404mm and minimum rainfall of 255mm were observed in the years 1998 and 1987 respectively.

Haryana Liquors Pvt. Ltd. 30 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

(viii) Social Infrastructure available There are schools, College, dispensaries, hospitals, Post offices, Banks, Market and places of worship in nearby area of the project site.

5.0 PLANNING BRIEF (i) Planning Concept (type of industries, facilities, transportation etc.) Town and country Planning/Development authority classification. The existing unit is Distillery industry and proposed expansion & installation will be done within the existing plant premises. Facilities required for the proposed expansion & installation project will be provided as per requirement. Transportation of raw material and final product is being / will be done by road. (ii) Population Projection Temporary influx of people will be there as the managerial and supervisory staff will generally be from outside the area. (iii) Land use planning (breakup along with greenbelt etc) Total Plant area is 34.7 Acres (14.04 ha). Proposed expansion & installation project will be set up in the existing plant premises. No additional land will be required. About 33 % of the total plant area is being/will be covered under greenbelt & plantation in order to reduce dust & noise pollution levels & to increase aesthetic beauty of the area. (iv) Assessment of infrastructure demand (Physical & Social) Haryana Liquors Pvt. Ltd. has assessed the demand of infrastructure (Physical & Social) in nearby area of the plant site and development activities are being undertaken under corporate social responsibilities program for rural development initiatives for the upliftment of the nearby communities from time to time. (v) Amenities/ Facilities Haryana Liquors Pvt. Ltd. has developed and will further develop the Amenities/Facilities in nearby area of the Plant site as per requirement of local people of the nearby area under corporate social responsibilities programs.

Haryana Liquors Pvt. Ltd. 31 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

6.0 PROPOSED INFRASTRUCTURE (i) Industrial Area (Processing Area) For the proposed expansion of Distillery capacity from 165 to 300 KLPD by installation of 135 KLPD Grain & Molasses based Distillery & Co-generation Power Plant from 7.0 MW to 15.0 MW, additional infrastructure will be built which includes grain milling, starch conversion, fermentation, distillation, boiler, turbine, evaporator & dryer for Unit II – 135 KLPD Grain & Molasses Based & 8.0 MW Co-Generation Power Plant. (ii) Residential area (Non Processing area) No residential area is envisaged. (iii) Greenbelt The company has already developed greenbelt/ plantation in 33% of the total plant area and the same will be further maintained. (iv) Social Infrastructure Proposed expansion & installation project will result in growth of the surrounding areas by ancillary development and supporting infrastructure in the region. (v) Connectivity The site is well connected with communication facilities like telephone, fax, and wireless as such no constraints are envisaged in this aspect. (vi) Drinking Water 5 m3/ day water will be required for drinking purpose after proposed expansion & installation project which will be sourced from Ground Water. (vii) Sewage Treatment System Domestic waste water generated from the plant is being/will be treated in STP. (viii) Industrial Waste management The distillery project is being / will be based on “ZERO DISCHARGE”. (ix) Solid Waste Management

o Solid waste from the Grain based operations generally comprises of Fibres and proteins in the form of DDGS, which are being / will be ideally used as Cattle Feed.

o Ash from the Boiler is being / will be sold to Cement & Brick manufacturers.

Haryana Liquors Pvt. Ltd. 32 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

(x) Power requirement and source Existing power requirement is 3.0 MW and additional 2.5 MW. Thus, the total power requirement after proposed expansion project will be 5.5 MW. Surplus power shall be sold to the State Electricity Board. Source: Co-generation Power Plants & D.G Sets (for Power Back-Up).

7.0 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 labourers (a brief outline to be given). Proposed expansion & installation will be done within the existing plant premises. No additional land is required for the same and hence, Rehabilitation & Resettlement is not applicable.

8.0 PROJECT SCHEDULE AND COST ESTIMATES (i) Likely date of start of construction and likely date of completion (time schedule for the project to be given). The project will start only after obtaining Environmental Clearance and other statutory permissions. Project will be completed in 24 months after getting all the regulatory approvals. (ii) Estimated project cost along with analysis in term of economic viability of the project. Ø Total cost of the Project: Rs. 92.0 Crores Ø Cost for Environment Protection Measures: v Capital Cost: Rs. 40.90 Crores v Recurring Cost/ annum: Rs. 0.70 Crores / annum.

9.0 ANALYSIS OF PROPOSAL (i) Financial and social benefits with special emphasis on the benefit to the local people including tribal population, if any, in the area. Proposed expansion & installation project will result in growth of the surrounding areas by increasing ancillary development and supporting infrastructure. Special emphasis on Financial and Social benefits will be given to the local people including tribal population, if any, in the area.

Haryana Liquors Pvt. Ltd. 33 Expansion of Distillery (165 KLPD to 300 KLPD) & Co-Generation Power Plant (7.0 to 15.0 MW) by installation of Unit II 135 KLPD Grain / Molasses Based Distillery & 8.0 MW Co-Generation Power Plant within Existing Plant Premises At Village Jundla, Tehsil Karnal, District Karnal, Haryana Pre - Feasibility Report

Development of social amenities will be in the form of medical facilities, education to underprivileged and creation of self help groups. Haryana state will get revenues in terms of taxes. Business opportunities for local community will be available like transport of alcohol to market, fly ash transport to Brick manufactures, maintenance & house-keeping contract work etc.

Haryana Liquors Pvt. Ltd. 34