Empee Distilleries Ltd. Contents
Total Page：16
File Type：pdf, Size：1020Kb
PRE – FEASIBILITY REPORT Of EXPANSION OF GRAIN BASED DISTILLERY PLANT CAPACITY FROM 60 KLD TO 80 KLD AT CHOUTKUR VILLAGE, PULKAL MANDAL MEDAK DISTRICT,TELANGANA STATE By EMPEE DISTILLERIES LTD. CONTENTS CHAPTERS 1. Executive Summary 2. Introduction of the Project / Background information 3. Project Description 4. Site Analysis 5. Planning Brief 6. Proposed infrastructure 7. Rehabilitation and resettlement (R & R) Plan 8. Project schedule & Cost Estimates 9. Analysis of proposal (Final Recommendations) CHAPTER – 1 EXECUTIVE SUMMARY EXECUTIVE SUMMARY Empee Distilleries Limited (EDL) is operating a 60 klpd Grain based Distillery unit at Choutkur Village,Pulkal Mandal, Medak District, Telanagana State EDL proposes to increase the production capacity of the plant from 60 to 80 klpd. The capacity enhancement will be achieved by optimising the existing process leading to increase of alcohol concentration from 9.5 % v/v to 12.5 % v/v. The project will use additional grain of 50 t/day . There is no additional requirement of land. Water consumption will increase by 120 m3/day which will be met by borewells. At present project is using 125 t/day coal and after expansion the project will use additional coal of 10 t/day in the boiler as fuel. The summary of the plant before and after expansion is given below EXPANSION OF GRAIN BASED DISTILLERY PLANT CAPACITY FROM 60 KLD TO 80 KLD OPERATING PLANT AFTER 60 KLD EXPANSION TO 80 KLD Raw Material 160 TPD 210 TPD Enzymes 0.25 TPD 0.35 TPD Alcohol Content 9.5 % V/V 12.5 % V/V 7.60 % W/W 10.10 % W/W Water Requirement, m3/day 1428.5 1593.3 Waste Water generation,m3/day 543.4 593.3 Water/wastewater Recycled, m3/day 843.4 918.3 Net Fresh Water Requirement, m3/day 1428-843 1593-918 =585 = 675 COMPARISION (units - kl/kl of alcohol produced Water Consumption without recycling 22.67 19.91 Water consumption with recycling of 9.28 8.43 treated and untreated wastewater into the OPERATING PLANT AFTER 60 KLD EXPANSION TO 80 KLD process Wastewater generation 8.62 7.41 Spentwash generation 5.87 5.38 Raw material required is given below. RAW MATERIAL OPERATING PLANT AFTER 60 KLD EXPANSION TO 80 KLD Raw Material 160 TPD 210TPD Enzymes 0.25 TPD 0.35 TPD Fuel – Coal 125 t/day 135 t/day Ethanol production is consumed by the industrial sector for production of ethanol-based chemicals like acetaldehyde, acetic acid, esters, butanol, glycol, pentaerythritol, vinyl acetate etc. and also is utilized by the potable sector. Transport of the raw material i.e grain is by trucks in gunny bags and finished product is transported by tankers. The proposed expansion will result in the following resource optimisation a. No increase in area of project b. Reduction in fresh water consumption from 9.28 to 8.43 m3/kl of alcohol production c. There will be reduction in wastewater generation as shown below in the table OPERATING PLANT AFTER 60 KLPD EXPANSION TO 80 KLPD Wastewater generation 8.62 7.41 Spentwash generation 5.87 5.38 The project is based on zero liquid discharge. No additional land is required for expansion. The present land occupied for plant is 49 acres and is under the ownership of EDL. No major construction activity is involved except the following in the expansion phase a. An integrated evaporator for concentration of spent wash will be installed b. Wet cake drier will be installed . c. An additional Fermentor will be installed d. Two Additional Distillation columns will be installed Greenbelt is existing in an area of 17.0 Acres No additional greenbelt is proposed. Present water consumption of the plant is 585 m3/day and after expansion 90 cum additional water is required , which will be met with the borewells. The project is based on zero discharge. The solid waste generation from the plant before expansion is 140 t/day and after expansion is 176 t/day. At present the wet cake that is being generated is dried in drier to make it DDGS and packed in HDPE bags. Similarly the unit has proposed additional drier to handle additional generation of cake after expansion. The entire solid waste after drying is sold as cattle feed The expansion will be implemented within 6 months after obtaining the environmental clearance The estimated project cost of expansion is 18.0 Crores. CHAPTER – 2 INTRODUCTION OF THE PROJECT / BACKGROUND INFORMATION 2.1 IDENTIFICATION OF PROJECT AND PROJECT PROPONENT. IN CASE OF MINING PROJECT, A COPY OF MINING LEASE / LETTER OF INTENT SHOULD BE GIVEN. PROJECT : Empee Distilleries Ltd; (EDL) is operating a 60 klpd Grain based Distillery unit at Choutkur Village, Pulkal Mandal, Medak District, Telangana State. EDL proposes to increase the production capacity of the plant from 60 to 80 klpd. The capacity enhancement will be achieved by optimising the existing process leading to increase of alcohol concentration from 9.5 % v/v to 12.5 % v/v. The project will use additional grain of 50 t/day. There is no additional requirement of land. The project after expansion will use 135 t/day of coal in boiler as fuel. There will be no increase in wastewater generation rather per unit consumption of water will decrease on increasing the alcohol concentration . The summary of the plant before and after expansion is given below EXPANSION OF GRAIN BASED DISTILLERY PLANT CAPACITY FROM 60 KLD TO 80 KLD OPERATING PLANT AFTER 60 KLD EXPANSION TO 80 KLD Raw Material 160 TPD 210 TPD Enzymes 0.25 TPD 0.35 TPD Alcohol Content 9.5 % V/V 12.5 % V/V 6.76 % W/W 11.38 % W/W Water Requirement, m3/day 1428.5 1593.3 Waste Water Generation, m3/day 543.4 593.3 Water/wastewater Recycled, m3/day 843.4 918.3 Net Fresh Water Requirement, m3/day 1428-843 1593-918 =585 = 675 OPERATING PLANT AFTER 60 KLD EXPANSION TO 80 KLD COMPARISION (units - kl/kl of alcohol produced Water Consumption without recycling 22.67 19.91 Water consumption with recycling of 9.28 8.43 treated and untreated wastewater into the process Wastewater generation 8.62 7.41 Spentwash generation 5.87 5.38 PROJECT PROPONENT : DIRECTORS: Mr.M.P.Purushothaman He has been a promoter Director of the company since inception. He has 40 years of experience with over 35 years of business in the liquor industry. He has promoted over 20 companies in the Empee Group with diversified activity such as sugars, hotels, education property development, transport and power including alternative sources and generation of power. He is honorary president of South India Hotels and Restaurants Association and Executive Committee Member of the Federation of Hotel and Restaurants Association of India. Ms. Nisha Purushothaman She is presently joint Managing Director of the company. She was appointed as a Director of the Company on 2.12.1994. She was thereafter appointed as Joint managing Director of the company. She holds a degree in Masters in Business Administration from London Business School. She has around 22 years of experience in liquor industry in field of operations, finance, administration and human resource management. Mr.Shaji Purushothaman He is an Arts graduate and completed Oxford A level from Oxford University,U.K. He has been actively associated with the company for the last 20 years and has rich administration experience. Mr.Shankar Menon Mr. Shankar menon holds a degree B.Sc. from Madras University ,M.B.A from Indiana University USA. Masters degree in Hotel & Restaurant Administration from Cornell University and Hilton School of Hotel Management at University of Houston. He had over 40 Years of Experience in National and International Hotels. TECHNICAL TEAM: Promoters would be assisted by in house technical and financial team of professionals: 1. Susheel Kumar (Technical Head) 2. Rajinder Kumar Dogra (General Manager) 3. Nishant Jha (Production Head) 4. Manoj Srivastava (Mechanical Head) GROUP COMPANIES 1.Empee Distilleries Limited 2.Empee Sugar & Chemicals Limited 3.Appollo Distilleries Pvt.Ltd; ( Associate concern of Empee Distilleries Limited) 4.Empee Power & Infrastructure Pvt. Ltd; 5.Empee Power Company ( India) Limited 6.Empee Hotels Limited 7.Empee International Hotels & Resorts Limited 8Empee Holdings Limited 9.Empee Institute of Hotel Management 10.EDL Properties Limited 2.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT EDL proposes to increase the production capacity of the plant from 60 to 80 klpd. Enhancement of production will be achieved by optimising the existing process leading to increase of alcohol concentration from 9.5 % v/v to 12.5 % v/v. 2.3 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE COUNTRY AND OR REGION. Ethyl Alcohol, Alcohol, Spirit, Denatured Spirit, there are myriad descriptions for this agriculture-based product. A globally traded commodity, Ethanol fires combustible engines in Brazil, slakes the thirst of many in Europe and finds its way in pharmaceutical and chemical industries, across the world. Ethanol is made by two routes: either by synthetic one from petroleum substances or by fermentation from sugar-bearing or starchy substrates using yeast. Alcohol finds its use in diverse applications ranging from potable liquor to life-saving drugs to paints & perfumery to renewable source of energy. Ethyl Alcohol is an important feedstock for the manufacture of various chemicals. These chemicals are primarily the basic carbon based products like Acetic Acid, Butanol, Butadine, Acetic Anhydride, PVC, etc. Ethylenes, Ethylene oxide are also produced from a petrochemical route, however this requires plants of huge scales and thus require substantially high investments. The drug industry also uses alcohol as a raw material for production of Insulin, Antibiotics, tonics and several other essential bulk drugs & formulations.