pre feasibility report on proposed production of …...pre feasibility report on proposed production...

Pre Feasibility Report

on

Proposed Production of 4.020 KLD Mahua

Flower Based Country Liquor Manufacturing

Unit, Birmitrapur Main Out Still Shop at

Birmitrapur, Tahasil- Birmitrapur, Dist-

sundargarh

License Holder: M/s Rajesh kumar Sahu

Submitted By:

Sri. Rajesh Kumar Sahu

(License Holder)

At-Main out Still Shop, Birmitrapur, Tahasil- Birmitrapur,

Dist-Sundargarh, State- Odisha

Pre-Feasibility Report of Birmitrapur Out Still Shop Shri Rajesh Kumar Sahu

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CHAPTER - 1

EXECUTIVE SUMMARY

1.0 Introduction

This project of manufacturing and sale by retail of country liquor (spirit) under

Out Still system is proposed by Sri Rajesh kumar Sahu, the Licensee, S/O: Late

Jyoti Prasad Sahu, At Raghunathpad, PO/PS: Titilagarh, Dist: Bolangir, Odisha.

The unit is new and undersigned collector of Sundargarh to work still at

Birmitrapur, in Birmitrapur Tahasil in the district of Sundargarh for manufacture

and open a shop at same place from the date of this license to the 31st march

2019.

Out still system is a system under which certain number of Stills for the

manufacture of liquor made allowed within certain area and the holder of an Out

Still license pay certain sum per month for manufacturing Out Still Liquor in his

Out Still and sell it by retail in his premises.

Country liquor manufacturing with retail sale unit under out still system is a small

scale industry and the said unit is always remained under the control of the State

Excise Department in terms of capacity creation, distribution and taxation. Since

long the industry possesses a dilemma to the State Government, due to

temptation of large revenues, on the one hand, and the other hand to supply

quality liquor to the people of the locality. The State Government has started a

new initiative to check and control of the illegal country liquor production

business and accordingly throughout Odisha state Out Still Country liquor

manufacturing and sale by retail units were established under the full control of

the Excise department.

Sri Rajesh Kumar Sahu has also obtained license for establishing such a unit at a

location namely Birmitrapur in Sundargarh district.

Since 1996 until now the Excise department, Odisha have renewed the said

license each year.

As per Order No. 15889/Ind-I-Con-(M)1204 dtd. 31.10.2016 issued by the

Odisha State Pollution Control Board, Bhubaneswar, Fermentation Industry

including manufacturer of Yeast, Beer, Distillation of Alcohol (extra neutral

alcohol) (waste water discharge up to 100 KLD) is listed under Orange Category.

Further, Hon’ble NGT, EZB, Kolkata has issued an Order in 2017 regarding

requirement of obtaining Prior Environmental Clearance from competent

authority for Fermentation and Distillation units in the matter of number of cases

of Manufacturing of Country Liquor.

Considering the magnitude of the unit and quantity of waste water generation

(less than 25 CUM per day) and fuel consumption (less that 25 TPD) the said

proposal may be considered as B2 Category for appraisal of the project for grant

of Environmental Clearance at SEIAA, Odisha.


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Therefore, the application is being submitted at SEIAA for Environmental

Clearance for the said proposal along with prescribed check list duly signed by

the Excise Superintendent and other documents such as, Form-1, PFR, process

flow sheet, land documents, design and specification of OS (Pot), plant layout,

and copy of excise license and brief description of the project.

1.1 Salient Features of the Project

The salient features of the project are given below in Table No. 1.

Table No. 1: Salient Features of the Project

Name of the Country Liquor Project Proposed Production of 4.020 KLD

Mahua Flower Based Country Liquor

Manufacturing Unit, Birmitrapur Main

Out Still Shop at Birmitrapur, Tahasil-

Birmitrapur, Dist-sundargarh

Name & address of the Applicant Sri Rajesh Kumar Sahu

The Licensee: At : Raghunathpada, PS/PO

: Titilagarh, DIST. : Bolangir, ODISHA

Whether new / existing Unit New

Date and year of commissioning License No 10/2018-19, issued by Dist.

Excise Office, Sundargarh.

Location of unit

Village /Mouza Vill : Birmitrapur,

Tahasil Birmitrapur

District Sundargarh

Khata No. 19/622

Plot No. 919

Co-ordinates of the site (Latitude

and Longitude)

Lat: 22.40278

Long: 84.73891

Land area of the unit (acres) 0.450 Acres

Forest Land Nil

Ownership of land NOC taken for the total Land by the

licensee from the Owner of the Land.

Excise License issued Yes

If yes, whether single/ multiple

license for the same location

Single License with Retail Shop at Same

Location.

Date of issue and validity period 1/04/2018 of the last issued license and

Validity Period is 01/04/2018 to

31/03/2019

Nearest Railway line Nearest Railway line is at Sogra Station is

at a distance of 3 km.

Nearest National Highway Nearest National Highway is NH-23 at

distance of 3 km.

Nearest Densely populated or built-

up area

Nearest Densely populated or built-up

area is Kaurmunda is at a distance of 10


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Km.

Power Requirement Only for lighting from state grid.

Man Power Ten (10 ) Numbers

Water Requirement 22.2 m³/Day, is sourced from Bore well

Air Pollution and Management One no. chimneys of height of 20 ft AGL

attached to rice husk fired bhatti (1 no of

deck still capacity 4020 litres). The

emissions generated will be passed

through air filter before releasing into the

atmosphere through the stack or chimney.

Waste Water Generation and

Management

Process waste water generation is 11.72 KLD- It will be recycled and will be used for cooling purpose. Domestic Waste Water generation is 3.216 KLD – It will be routed through separate septic tank and then to soak pit.

Solid Waste Generation and

Management

Solid Waste Management – Mahua Waste obtained during distillation and cooking process is dried completely and then sold off as cattle feed and also, the mahua waste after drying is again reused as fuel in place of husk, which reduces the quantity of husk required by half. Fly ash from rice husk fired bhatti- The fly ash generated is sold /supplied to brick kilns for making fly ash bricks and also used in filling of low lying areas.


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CHAPTER - 2

INTRODUCTION OF THE PROJECT/BACK GROUND INFORMATION

2.1 Identification of Project and Project Proponent

The license holder has been permitted for production of 4020.0 ltrs (Deck

capacity) per day Mahua Flower based Country Liquor / Spirit at village:

Birmitrapur, Dist: Sundargarh, Odisha.

Nature of license: License issued by the Excise Department, Odisha State as

per their endorsement OS-1 (Main Out Still Liquor Shop). This license is valid for

the manufacture and sale by retail of country spirit / liquor in a shop on the out

still system and the said license is in force for the unit till 31st March, 2019.

No. of license as in original: license No: 10/2018-2019 as per the

endorsement made by Superintendent of Excise, Sundargarh.

Locality of vend: Birmitrapur, Shop of Sundargarh District in the State of

Odisha.

Name of the License Holder: Sri Rajesh kumar Sahu, S/O: Late Jyoti Prasad

Sahu, At: Raghunathpada, PS/PO: Titilagarh, Dist: Bolangir, Odisha.

Operational Status of Unit: The unit is new as per the valid Excise License

granted by State Excise Department of Odisha and being renewed on yearly

basis. The present license of the E.P. holder is valid till 31st March, 2019

2.2 Brief Description of Nature of the Project

It is proposed to produce Mahua Flower based Country Liquor in the unit. The

unit will have the flexibility to produce this type of country liquor through the

process of fermentation and distillation, according to market requirements.

The unit has capability to dispatch the product in sealed pouches. The pouch

packing machine is well equipped to cater the required quantity enough to pack

and dispatch for domestic sale.

Then the concerned in-charge Excise Officer collects the product sample for

chemical examination. If it is found fit for human consumption thereafter the said

Mahua liquor has been transferred to the retail shop of the licensee for sale.

The said country liquor is packaged in an earmarked poly pack for sale. The

packaging is done in the premises of the unit and then taken to the shop for

storage and sale.

2.3 Need for the Project and Its Importance to the Country and or

Region

As for liquor, mahua is a sacred drink for adivasis, and one of the world's best

when distilled properly. Mahua flowers are rich in sugar (68-72%), in addition to

a number of minerals.


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Various local alcoholic drinks meet upto 5-10 % of the daily nutritional

requirements, playing supplementary role in the nutrition of tribal people. The

Mahua alcoholic beverage is also used to treat dysentery by Baiga, Gond, and Kol

tribes.

Mahua (Madhuca indica) has been used for liquor production, for centuries, by

the tribals. The liquor produced from the flowers is largely colorless, with a

whitish tinge and not very strong. The taste is reminiscent of sake with a

distinctive smell of mahua flowers. It is inexpensive and the production is largely

done in home stills.

In 19th century, the British government identified the potential of mahua and

went a step forward to help the Jaiswal family in Ranchi to come up with the first

mahua distillery of the country named Ranchi distillery in 1875. English

anthropologist and visiting professor at Institute of rural management, Anand

(IRMA) Felix Padel a descendant of Charles Darwin during a visit to Jharkhand

had tasted Mahua and expressed his surprise over government not picking it up

to develop as an industry and also expressed his anxiety why people in India

would prefer French wine and English scotch when something fresh and

rejuvenating like mahua and salpo are available.

British administrators interfered with this, alternately making its manufacturing

illegal and placing a heavy tax on it. In effect mahua become a 'low-caste' drink

that respectable people in a town will not drink. With good reason, since you can't

get good quality in a town. Padel also identified it as one of the reasons that

illegal brewing and spiking the drink with battery fluid and other toxic substance

to give a kick has made it worse. The then excise commissioner and secretary to

government of Jharkhand Satyendra Singh agrees that mahua has a great

potential and could be developed into an industry like the Maharashtra

government has used grapes for wine or Goa has used cashew nuts for Feni.

However a legalized framework is needed.

India is one of the major alcohol producing countries. Production of alcohol has

gone up from a meager 100 million liters in the fifties to the current level of more

than 600 million liters. The Russia, USA, Brazil, India, the UK, Japan and West

Germany, are the leading alcohol producing countries. India, has been exporting

alcohol in substantial quantities. According to a survey conducted by a UK-based

trade magazine in liquor, three Indian brands figured in the "TOP 25 Fastest

Growing Brands in the world in 1994". While the survey is for both local as well as

foreign sales, it takes into account only those brands which "export or produce

more than 10 percent of their sales volumes overseas"- in other words, Indian-

made Foreign liquor (IMFL) could actually be well on its way to becoming a

preferred foreign liquor. Indian Consumption of whisky has grown at an average

14% annually for the past eight years, climbing to 30 million cases (of 12 bottles

of 750 ml each) per annum. That makes India the hottest whisky market in the

world.

Mahua based alcohol can fetch a good international market if distilled with

following international standards. So there is definitely the need for proper


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distillation of Mahua under the banner of Make in India project of our Hon’ble

Prime Minister at par of any foreign liquor.

2.4 Demand - Supply Gap

Change in the situation with a sharp increase in demand for alcohol following the

implementation of expansion and new schemes by SM Dyechem and Chemplast,

which were increasing the output of ethylene oxide, specialty chemicals, PVC

resins and Mono ethylene glycol in a big way.

The output of alcohol-based chemicals would increase at a faster rate in future

with the independent units taking up new projects and sugar mills having their

own distilleries establishing downstream projects. The calculations in this regard

have been upset largely by the sharp increase in the cost of molasses and

alcohol.

The present availability of alcohol cannot meet the entire demand. Alcohol

production is directly linked with sugar output and availability of molasses.

To meet the needs of the growing population, sugar production will continue to

maintain this trend and as a result, alcohol availability will improve. However, a

disturbing factor is the diversion of a large proportion of alcohol for potable use.

Further, demand for mahua based liquor at tribal belt has also increased as the

tribals themselves reduced making mahua liquor in-house but their consumption

of the said liquor has increased.

2.5 Imports Vs Indigenous Production

The mahua based liquor is mostly indigenous. Many foreign companies have tried

making mahua based liquor but could not get remarkable success. It is not

imported.

2.6 Export Possibility

Production of country liquor is not meant for export marketing. It is produced for

sale in the local market under the terms and conditions of the license issued and

fixed by the Excise Department, Govt. of Odisha. However, export of said product

can only be thought of once it is of international quality and within the provision

of existing law of the country.

2.7 Domestic / Export Markets

There is a good demand of mahua flower based country liquor in the domestic

market mostly in the tribal belt. However, if the distillation takes place with

international standard then it can fetch a good export market as was commented

by many foreign delegates during their official visit to India.

With the government is planning to showcase “Wines of India” across the globe,

the Agricultural and Processed Food Products Export Development Authority

(APEDA) is working out the strategy. Mahua, being an indigenous tree of high

economic value has vast potential for good quality mahua flower wine which may

find extensive export market.


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2.8 Employment Generation (Direct and Indirect) Due to the Project

The manpower requirement for running this unit is around 10 (ten) numbers including

administrative, managerial and skilled / unskilled staff.


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CHAPTER - 3

PROJECT DESCRIPTION

3.1 Type of the Project Including Interlinked and Interdependent

Project

Mahua flower based country liquor / spirit manufacturing unit with 4020.0 ltrs

(Deck capacity) per day production capacity.

3.2 Location and Accessibility

The country Liquor shop is located at village: Birmitrapur, Tehsil: Birmitrapur,

Dist: Sundargarh, Odisha.

Village: Birmitrapur

Tehsil: Birmitrapur

District: Sundargarh

State: Odisha

Latitude: 22.40278

Longitude: 84.73891

1. Road Connectivity: The Out Still Shop is well connected with State Higheway-

10 which is passing at a distance of 32 km from the project site.

Rail Connectivity: Nearest Railway station is Sogra railway station is at a

distance of 3 km from project site.

Figure No. 1: Google Map of 10 Km Radius


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Figure No. 2: Topo Map of 10 Km Radius

3.3 Details of Alternate Sites Considered and the Basis of Selecting

the Proposed Site

No alternative site is applicable for the unit as it is an existing permitted site

approved by the Excise department.

3.4 Size or Magnitude of Operation

The said project is for production of 4020.0 ltrs (Deck capacity) per day Mahua

Flower based Country Liquor at village: Birmitrapur, Dist: Sundargarh, Odisha.

And approved raw material storage capacity is 700.0 Quintals per month as MGQ.

3.5 Project Description with Process Details

The ripe mahua flowers are first dried in the Sun and then fermented with water

in HDPE drums for 72 hours. The HDPE drums are of 200 litres capacity in which

956.88 kg/day of mahua flower are fermented with 4878.36 litres of water for 3-

5 days.

After completion of fermentation, the fermented liquid is taken for distillation at

110°C in a copper still (pot) that is, in a rice husk fired Bhatti (1 no of deck still

capacity 1080 litres) which is water cooled and the condensation product of

distillation is country liquor.


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Product of Mahua liquor with water is being mixing as per the guideline of the

Excise Department. Then the concerned charge Excise Officer collects the product

sample for chemical examination. If it is found fit for human consumption, then

thereafter the said Mahua liquor is being distributed to the authorized retail

counters i.e. branch shops of the locality for selling. The state Excise department

has tagged different branch shops with this unit in the locality. The product is

being sold in an earmarked poly pack. This pouch is being prepared in the

premises of this unit prior to distribute to the retail counters of the locality.

Basis: For production of 1000 litres liquor

Mahua flower required is = 886 Kg

Rice Husk required is = 768 Kg

Mahua flower residue from process = 284 Kg

Ash generation from rice husk fired bhati = 236 Kg

Water required for process = 4517 Litres

Total water requirement including domestic = 5517 Litres

Waste water generated from process = 2916 Litres

Taking the above basis, For production of 4020 litres liquor

Mahua flower required is = 3561.72 Kg

Rice Husk required is = 3087.36 Kg

Mahua flower residue from process = 1141.68 Kg

Ash generation from rice husk fired bhati = 948.72 Kg

Water required for process = 18158.34 Litres

Total water requirement including domestic = 22178.34 litres ≈ 22200 litres

Waste water generated from process = 11722.32 Litres

The process flow chart of the production process is given in Figure No. 3 and the

schematic diagram of the manufacturing Bhatti is given in Figure No. 4.


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Figure No. 3: Manufacturing Process Flow Chart

Figure No. 4: Design of Country Liquor Manufacturing Bhatti


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Land requirement: The land requirement of the project is Ac 0.450.

Figure No. 5: Layout Map

3.6 Raw Material Requirement

Mahua flower: 3561.72 kg/day

Rick Husk: 3087.36 kg/day

Transportation of Raw Material: The basic raw material Mahua flowers are

being transported to the project site by road. Various local vendors are regularly

supplying the material at site. The Licensee also purchases the flower from

different licensed holders. The NOC endorsement is made in the license of the

State Excise Department Odisha.

Transportation of Finished Product: Vehicular transportation of finish product

Mahua Liquor from bhatti area to OS Shop is not required as the shop and Bhatti

are in the same premises.

3.7 Resource Optimization / Recycling and Reuse Envisaged in the

Project

Management shall envisage optimum utilization, recycling and reuse. These

resources include mahua flower, land, paddy husk, water and electricity.

Optimum use of mahua flower is ensured. It is regularly checked that no disposal

of used flower takes place those having any sugar content or juice left in the


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flower. Waste water generated from distillation process has been collected in a

pond for use in plantation / gardening. Waste water from the cooling area is

recycled in the system for condensation. The land available is used as per design

requirement. No wastage or inappropriate use of land in the project. The paddy

husk as fuel is used as per requirement. Wastage is not permitted. Waste residue

of mahua flower mix is used as manure. Electricity is also used very economically

and as per need.

3.8 Availability of Water, Its Source, Energy / Power Requirement and

its Source

Water Requirement: The source of water is bore well for the present

consumption. Total water consumption for different purpose is 22.2 KLD.

Sl. No. Description Total water Requirement

(m3/day)

1 Process Requirement 18.1

2 Domestic & Misc 4.1

Total 22.2

There will be Process water requirement for the plant as water is required for

fermentation. The process waste water will be stored in concrete made closed pit

and then will be sent to treatment plant. The domestic effluents will be treated in

septic tank and routed to soak pit. The recycled water from settling tank will be

consumed for green belt development and gardening inside the plant. NOC for

water permission is under process.

Water Balance

Power: Electricity consumption is not required for Mahua flower based Country

liquor distillation process. But Electricity is required for domestic/general purpose

of the unit. The required power is taken from State Grid.

3.9 Environment Management Plan


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Waste Water Generation & Management

Process water is required only for fermentation & cooling purposes and hence the

waste water will be generated from the plant. The Unit is using clean and hygienic

water for manufacturing of out still liquor for fermentation. Consumption of water

for fermentation and distillation is 18.2 KLD (approx) waste water generated from

above process is 11.7 KLD (Approx). Effluents generated from the process are

discharged to concrete made closed pit situated inside the premises and then

routed to ETP for treatment. Treated water from ETP will be reused for cooling

purpose and process. Other, wastewater generation will be mainly due to the

sanitary wastewater generated due to domestic uses. There will be ‘zero

discharge’ from the unit and there will not be any contamination of surface water

bodies or ground water due to effluent discharges.

Waste Generation and Management

The manufacturing unit will generate solid waste & liquid effluents and will be

fully equipped to handle its domestic sewage.

The plant will not have any gaseous emissions. All air emissions of the plant

through stack will be through the most efficient pollution control equipments and

will not have any adverse impact on the land or marine environment.

Solid Waste Generation (Other than Mahua Flower) and it’s Management:

No hazardous waste will be generated either in the process or pollution control

facilities. There will be solid wastes from the process. All domestic waste will be

routed to septic tank and then to soak pit.

Waste oil in small quantities will be generated from gear box and other

machineries and will be disposed off to authorized recyclers registered with

Pollution Control Board.

Mahua Flower Residue Generation – 1141.68 kg/day

Waste from rice husk fired Bhatti(Ash) – 948.72 kg/day

Green Belt Development: Greenbelt will be developed along with the project.

The total greenbelt area will be around 0.08 Dec (20 % of total area.). The main

objective of the greenbelt is to provide a barrier between the plant and the

surrounding areas. The greenbelt helps to capture the fugitive emissions and to

attenuate the noise generated in the unit apart from improving the aesthetics of

the plant site. The Greenbelt will be adequately sized and will have a suitable

density so as to mitigate the effects of emissions from the unit. Roads for

vehicular movement will be paved and adequate mitigation measures will be

provided to prevent fugitive emissions.

3.10 Schematic Representations of the Feasibility drawing which give

information of EIA Purpose

The proposed schematic representation with reference to the EIA guidance

manual-Distilleries prepared by IL&FS Ecosmart Limited, Hyderabad and issued


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by Ministry of Environment, Forest and Climate Change, Govt. of India provides

information for preparation of EIA and is depicted in the following Drawing No. 5.

Figure No. 5

Schematic Representation of EIA Process


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CHAPTER - 4

SITE ANALYSIS

4.1 Connectivity

4.1.1 Road

The unit site is located at a distance of 32 km from State Highway-10. And the

national highway-23 is at a distance of 3 km from project site.

4.1.2 Rail

Nearest Railway station is Sogra railway station is at a distance of 3 km from

project site.

4.2 Land Form, Land Use and Land Ownership

Land of the project site is 0.45 Acres is not a part of forest land. The land of the

project vide plot no 919 khata no 199/622 measuring 0.450 Acres. The area does

not form part of any national park, Wildlife Sanctuary and National/Biosphere

reserve.

4.3 Topography

The topography of the land is generally flat and well suited for development of

Industry. There are no ecologically sensitive zones nearby forest within 10 km

from the plant site.

4.4 Existing land use pattern

Land of the proposed project is barren Land. Plant is not coming under the dense

forest category land. The unit’s land vide plot no 919 khata no 199/622

measuring 0.450 Acres. This area does not form part of any National Park, Wild

Life Sanctuary and Natural/Biosphere reserve.

4.5 Existing Infrastructure

The project site is well connected to roads and rail network. Nearest densely

populated area is Kaurmunda is at a distance of 10.0 Km from project site.

Nearest railway station is Sogra is at a distance of 3 km.

4.6 Climate data from secondary sources

The project area experiences tropical and humid climate with three distinct

seasons i.e. the summer season, the Rainy Season and the winter season. The

summer starts from March and extends up to May, the Rainy season starts from

Mid June to Mid October and the Winter Season from November to February. The

south-west monsoon breaks in the middle of June and continues till the end of

October.

Daily maximum temperature is 40.20 C and daily minimum temperature is

13.80C. Where the annual mean temperature is 32.60 C (Max) and 21.00 C


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(Min). The average relative humidity is 75 %. The average annual rainfall is

1287.0 mm.

4.7 Social Infrastructure Available

Dalmia College is at a distance of 28.32.4 km from project site.


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CHAPTER - 5

PLANNING BRIEF

5.1 Planning Concept

Type of industry: Mahua Flower based country liquor manufacturing unit of

capacity 1 X 4020 ltrs (Deck capacity) per day production and it is a small scale

industry. Facilities for drinking water: Drinking water is available in this site and

the source is ground water. Facilities for transportation: National High way no. 23

is passing at a distance of 3 kms from project site. SH 10 passing by at around

32 Kms. Other Village Roads are also there within 1 Kms of Project Site. Sogra

Railway Station is at 3 kms.

5.2 Population Projection

This unit is giving employment opportunity to the 10 number of people. In future

more people will get employment. People of the buffer zone are mostly engaged

in agriculture, business and services. The workers of the project will be from the

nearby villages so there will be no permanent increase in population.

5.3 Assessment of Infrastructure Demand

The infrastructures such as land, roads, power, water, transportation, raw

material and paddy husk are sufficiently available locally. This has been using for

green belt development and other uses in the unit and it is easy and low cost for

the project proponent.

5.4 Amenities/Facilities

The project site is well connected to roads and rail network. National High way

no. 23 is passing at a distance of 3 kms from project site. SH 10 passing by at

around 32 Kms. Other Village Roads are also there within 1 Kms of Project Site.

Sogra Railway Station is at 3 kms.


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CHAPTER - 6

PROPOSED INFRASTRUCTURE

6.1 Industrial Area

The project is for manufacturing of country liquor by the Birmitrapur OS Shop at

village Birmitrapur, District of Sundargarh, Odisha.

The total land of the said project is 0.45 Ac. The total land has already been

taken on lease by the proponent or the licensee. The land available for the

project is sufficient for the said project.

6.2 Residential Area

No residential facilities envisaged in the project.

6.3 Green Belt

About 20% of the total land is and will be developed as plantation area. Mixed

and local species are selected for plantation. New plantation and gap Filling in the

Plantation area is planned to be carried out in each monsoon season.

6.4 Social Infrastructure

Social infrastructure such as road, rail, hospitals, schools, bank, places of

worship, park, market, playground etc. healthcare, community hall, etc. are

available in nearby area of project site.

6.5 Drinking Water Management

The total water requirement for the project is 22.2 KLD (Maximum). The water

will be sourced from Groundwater through deep bore well. Necessary permission

will be obtained from CGWA if required.

6.6 Sewerage System

A garland drain around the plant is envisaged to collect surface run-off during

rainy season. Internal drainage system is constructed to collect domestic and

industrial effluent.

6.6.1 Run-off Management

The rain water collected from the roof of buildings will be channelized through

drains around the buildings and will be recharged into the ground by providing

recharging pits. Overflow, if any, will be discharged to the nearby plant drainage.

Rain Water Harvesting: Proposed Structure for Rain Water Harvesting &

Artificial Recharge Rainwater from roof area will be recharge to ground water

system through recharging structure. Artificial recharging structures (Chamber

with an injection well) will be constructed at suitable locations. The dimension of

the chamber will be 1mX 1m X 1m. The bottom half of the chamber will be filled


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up with filter material (gravel and sand). The wall of the chamber is made up of

bricks. The plan and section of the recharge pit are given in Fig. 1.

Filter Material:

The purpose of the filter media is to clean of the water meant for recharging off

any suspended particles. The bottom 0.5m thick layer is a gravel layer with

2.0mm to 3.0mm size. The gravel layer is overlain by a 0.25m thick medium to

coarse sand layer with sand size 0.5mm to 2.0mm.

Injection Well

An injection well is a 4” dia. PVC Pipe lowered in a 8” diameter bore well

constructed at the centre of the chamber. The depth of the bore well will be

around 80m or the depth will be decided during drilling. Slotted pipe will be given

against fractured formations. The annular space will be filled up with gravel. A

0.5m length slotted pipe (1.0mm slot size) will be put at the top of the injection

well inside the chamber for passage of filtered water in to the injection well. The

number, location and dimension of recharge structures are given in Table No. 1.

Table No. 1: Proposed Structures

Sl Structure No Dimension

1 Recharge Structure

1 Length- 1.0 m Breadth- 1.0 m Height- 1.0 m

Fig. 1: Plan of Recharge Structure


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6.7 Solid Waste Management

No hazardous waste will be generated either in the process or pollution control

facilities. There will be solid wastes from the process. All domestic waste will be

routed to septic tank and then to soak pit.




Mahua Flower Residue Generation – 1141.68 kg/day

Waste from rice husk fired Bhatti(Ash) – 948.72 kg/day.

6.8 Power Requirement

Electricity consumption is not required for Mahua flower based Country liquor

distillation process. But Electricity is required for domestic/general purpose of the

unit. The required power is taken from State Grid.

For emergency operation, there will be one number of 50 KVA capacity DG set,

which will be operated during power failure only.


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CHAPTER - 7

REHABILITATION AND RESETTLEMENT (R & R PLAN)

7.1 Policy to be adopted (Central / State) in respect of the project

affected person including Home Oustees, Land Oustees and Land

Less Labourers

The said project area does not involve any settlement or do not need any

rehabilitation. So, R & R plan is not required as per R & R policy of Central or

State Government. However, in case any such issues arise in future the Licensee

will abide by all rules and regulations thereof.


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Chapter - 8

PROJECT SCHEDULE & COST ESTIMATE

8.1 Project Schedule

8.1.1 Statutory Clearances

The proposed project will require various statutory approvals and clearances from

various authorities of the Government.

The total project is already implemented and all other statutory clearances from

the State / Central Government is under process as per direction passed by

Hon’ble Nation Green Tribunal, Kolkata.

Direction of Hon’ble NGT to obtain EC from the State Authority: The

licensee is entitled to obtain EC having regard to the law of the land. The Hon’ble

Nation Green Tribunal, Eastern Zone bench, Kolkata has passed order on

15.12.2016 vide O.A Case No: 124 of 2015/EZ to obtain EC from the state

authority.

8.2 Estimated Project Cost

The project cost is approximately Rs.6.0 Lacs (Rupees Six Lakh) only inclusive of

environmental pollution control and protection measures. It is from own finance.

Table No. 2: Project Cost

Sl. No. Description Amount (in lakhs)

1 Copper Deck - 1.50

2 Stack 0.50

3 HDPE drums (200 ltrs capacity) 1.50

4 Pouch Making Machine - 0.50

5 Fire extinguisher - 2 Nos. 0.15

6 Road and building 0.15

Total 4.30

Table No. 3: Cost of Pollution Control Equipment

Sl. No. Description Estimated Cost

(in lakhs)

1 Air Pollution Control Devices 0.80

2 Environmental Monitoring & Management 0.50

3 Green Belt Development & Misc 0.40

Total 1.70


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CHAPTER - 9

ANALYSIS OF PROPOSAL (FINAL RECOMMENDATIONS)

9.1 Analysis of Proposal (Final Recommendations)

There will be positive impact due to the project executed. The state govt. shall

earn revenue due to running of unit. Due to this operating unit, there will be

direct & indirect employment to nearby villagers. Further, good number of people

will get ancillary jobs in transport, casual labour for various works. In addition,

the living condition will improve through integrated rural development

programmes, provision of essential facilities like education, health care, drinking

water and all other well-conceived beneficial social welfare activities. Thus, the

project will usher in the social and economic development of the persons living in

the vicinity of the Project i.e. of society at large.

Improvement in Socio-Economic Conditions

Employment: During operation plant is generating direct employment. The

preference is given for local population for employment in the semi-skilled and

unskilled category. Indirect employment is created by the unit for supply of raw

materials and daily domestic goods.

Health and Safety Measures: The workers engaged in pollution generation

area are equipped with appropriate equipment.

Following measures are adopted in the plant to keep check on the safety

measures and health:

A periodic health check-up are arranged for the workers in the plant for

occupational diseases. All the employees will undergo medical check-ups at

regular time interval to determine any impact on the health of employees due

to the distillery operation.

Inspection and maintenance of pollution control systems regularly.

Adequate facilities for drinking water and toilets are provided for the

employees.


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Annexure-1

a) Detail of Effluent Treatment Plant (ETP) for treatment of

waste water generated from the country liquor unit

This report covers the detailed engineering design of the Effluent Treatment Plant

(ETP) with a capacity of 12.0 M3/day for our Mahua Country Liquor Plant.

Mahua is a commaon tree in deciduous forests of India, quite prominent in states

of Andhra Pradesh , Bihar, Gujarat, Karnataka, Madhya Pradesh, Odisha etc.

Mahua flowers are in dense fascicles near end of the branches having 1.5 cm long

fleshly cream corolla tube and are scented. Flowering period of Mahua is from the

month of March to May in East and North india and July to September in south

india. flowers mature time is about 32-35 days . One to two good flowering is

expected every three years, that is ,it has an alternate bearing habit. It is used

for making alcohol, vinegar,syrups and jams. Mahua oil is largely used in the

manufacture of soaps, besides cooking. It is also used for curing various diseases

like Bronchitis, Rheumatism, Diabetes, Piles, Arthritis, and Tonsillitis etc.

Mahua flower is rich in sugar (68-72%) out of which maximum proportion is of

reducing sugars. Apart from sugar, number of minerals components is there.

Sugars identified are sucrose, maltose, glucose, fructose,arabinose and

rhamnose. When flowers are mature and ready to fall, there is maximum total

sugar content in the flowers. It is one of the most important raw materials for

alcohol fermentation. mahua has been used for liquir production, for centuries by

the triabls. Fermentation conditions were standardized for nahua wine

preparation. The liquor produced from the flowers is largely colourless, with a

whitish tinge and not very strong. It is inexpensive and the production is largely

done in home stills.

Mahua flower contains 45-60% ethyl alcohol. The fermentation and steam

distillation processes are adopted by manufacturers to extract ethyl alcohol from

dried mahua flowers. The yield of ethanol is 300-400 ml per kg of dried mahua

flowers. The mahua flower is soaked in water. Around 37-38kg of flower is put up

in the 200 litre capacity plastic drum. The kinetic of fermentation depends on the

dilution of solid in water. It has been reported (given in Table 1 and Fig.2) that

solid and water ratio (1:5) gives better yield of alcohol due to saturation as well

as concentration. Hence around 140-160 litres water is added in the solid. It is

kept 2-4 days by adding some additives like urea or sodium-potassium tartarate

and yeast strain to improve the fermentation kinetics at normal temperature. The

bubbling of carbon dioxide gas from the slurry indicates the status of

fermentation kinetics. After fermentation, the pH of the slurry is around 4-


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5%depending on the water quantity. Then, the slurry is fed to the distillation unit

shown in Fig.3. The vessel with cover was kept on the earth made chulla. The

vessel is made in copper metal for better heat transfer. Based the capacity of the

plant, the volume of vessel varies. The volume of the vessel is same volumetric of

production capacity. The copper vessel is heated by burning of rice husk. The

temperature is maintained around 110°C. It is boiled 4-6 hours to take out total

alcohol along with steam and then the vapour of steam and alcohol are

condensed through copper cooling coil dipped in cooling tower by exchanging the

heat with water. Then the mixture of distilled water and ethanol is collected in the

pot/jar. The concentration of alcohol is maintained around 36-42.5% by volume

depending on the water evaporation along with alcohol by increasing the

residence time.

The effluent treatment plant is based on Activated Sludge technology. The

biological treatment system will consist of an aeration tank with Air Blower. The

treatment scheme will consist of Screening, Oil & Grease trapping, Equalization,

UASB Reactor, Biological Treatment (Aeration), Clarification, Sludge Drying,

Sludge Recirculation, Filtration and Disinfection, Treated water Collection. The

treated water will be low in BOD, COD, TSS, O&G etc.

Process Technology

Activated sludge technology is used in this Effluent Treatment Plant. This scheme

is proven, under a variety of operating conditions, and is highly flexible in

operation. By the concept of Activated sludge technology the requirement of

expensive land is reduced. Basically a conventional treatment requires large

space, and large operating force but the Activated sludge technology based plants

individually occupy much less space, making the plants more manageable.

Activated sludge process is a common method of aerobic wastewater treatment.

The purpose of the process is to reduce amount of dissolved organic matter from

wastewater, using microorganisms growing in aeration tanks. Microorganisms

convert dissolved organic matter into their own biomass, oxidizing carbonaceous

matter, oxidizing nitrogenous matter and removing phosphates.

The system utilizes aeration tank of much smaller size, thereby reducing the

power required in aerating the raw effluent. In Aeration tank moisture free Air is

bubbled for the purpose of aeration.

The treated wastewater runs over the edges of clarifier. A part of the settled

sludge is being returned into aeration tank, where is mixed with fresh primary

treated wastewater and bio-oxidation process goes on.

The treated wastewater from clarifier passes through the Multi Grade filter &

Activated Carbon Filter for removing colour and odour and then stored in treated


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water collection tank. Now this treated water can be permissible to discharge to

inland surface.

Process Description

The Fine Bubble Membrane Diffuser which is designed with the help of best

available modern technology. It has been designed for easy retrofitting of existing

diffused aeration installations to increase performance and decrease utility costs.

The membrane diffusers offer exhibit the following characteristics:

Self cleaning

Back flow Prevention

Flexibility & Durability

Sizes Ø250 mm

Type of bubble Fine Bubble

Bubble size 1mm to 2 mm

MOC of diffuser EPDM / Silicon

MOC of diffuser support ABS

Temperature Tolerance 850C

Operating temperature 350C

Membrane Surface Area 0.05 m²

Shape of Diffuser Disc type

Proposed Treatment Scheme

The treatment consists of Anaerobic Treatment in U.A.S.B Reactor followed by

Treatment in Aeration Tank with the help of Air blower, then Clarifier and Tertiary

Treatment in Multi Grade filter & Activated Carbon Filter.

In this process the effluent will be treated in three stages

• Primary treatment

• Secondary treatment

• Tertiary treatment

Primary treatment:

In the primary treatment the raw effluent will pass through the bar screen

chamber and oil and grease removal unit. In this section suspended matters, oil,

sand, grit and floating material etc. will be removed from the effluent. Then the


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effluent is sent to a collection tank cum equalization tank by gravity.

The effluent will be pumped from equalization tank to UASB reactor. UASB is Up

flow anaerobic sludge blanket technology referred as UASB reactor, is a form of

anaerobic digester that will be used in the treatment of waste water. This system

uses an anaerobic process while forming a blanket of granular sludge which

suspends in the tank. In this reactor the waste water flows through the blanket

and is processed or degraded by the anaerobic microorganisms. The upward flow

combined with the settling action of gravity suspends the blanket with aid of

flocculants. The bio gas will be produced as by product which can be captured or

vented to atmosphere.

Secondary treatment:

In the secondary treatment the effluent from just above the thick sludge blanket

layer of UASB reactor will be pumped to aeration tank where the effluent is

treated by aerobic process followed by clarifier. In aeration tank organic load will

be degraded with the help of aeration.

Mixed liquor Volatile suspended solids (MLVSS) will be maintained in aeration

tank in definite proportion by recycling the bio sludge trapped in the clarifier.

Recycling the bio sludge will be carried out by non clog, centrifugal, semi open

type impeller.

Oxygen is injected into the aeration tank by the help of air blower. The clear

overflow from clarifier will go to the filter feed tank. The excess sludge from the

clarifier shall be withdrawn to sludge drying beds for dewatering. The dried

sludge can be used as good manure or for land filling.

Tertiary treatment:

In the tertiary treatment the clear water from filter feed tank will be filtered by

pumping through the Multi grade filter and Activated carbon filter for removing

colour and odour from it.

The clear treated water will be stored in treated water collection tank. The clear

treated water can be reused for gardening or can be discharged to inland surface.


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Fig No: 1. LAYOUT MAP OF ETP PLAN OF LIQUOR PROJECT


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Annexure-2

b) Details of utilization of treated water to adopted Zero Liquid

Discharge (ZLD) with water balance.

Water Requirement: The source of water is bore well for the present

consumption. Total water consumption for different purpose is 22.2 KLD.

Sl. No. Description Total water Requirement

(m3/day)

1 Process Requirement 18.1

2 Domestic & Misc 4.1

Total 22.2

There will be Process water requirement for the plant as water is required for

fermentation. The process waste water will be stored in concrete made closed pit

and then will be sent to treatment plant. The domestic effluents will be treated in

septic tank and routed to soak pit. The recycled water from settling tank will be

consumed for green belt development and gardening inside the plant. NOC for

water permission is under process.

Water Balance


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Annexure-3

Environment Management Plan

Air Quality Environment & Management

Air Environment – Mitigation Measures

All air emissions of the unit will be through the installed a chimney of height

of 19 feet AGL attached to the rice husk fired Bhatti with deck capacity of

4020 lts. Hence, and will not have any adverse impact on the land or marine

environment.

Table 3.5- Source of Air Pollution and Control Measures.

Sl.

No. SOURCES POLLUTANTS MITIGATIVE MEASURES

PROCESS SECTION (INCLUDING DISTILLATION SECTION) & Raw Material Handling

Section

1 Process Section (husk fired copper pot (Bhatti)

Smog The unit has installed a chimney of height of 19 feet AGL attached to the rice husk fired Bhatti with deck capacity of 4020 lts.

2 Raw Material

Yard (rice husk)

Dust The yard will be covered with tarpaulin.

ROADS

1 Internal Roads

Fugitive Dust • The internal roads will be made of

Concrete/ Black topped.

• Manual sweeping will be carried out

regularly followed by water sprinkling.

Waste Water Generation & Management

Process water is required only for fermentation & cooling purposes and hence

the waste water will be generated from the plant. The Unit is using clean and

hygienic water for manufacturing of out still liquor for fermentation.

Consumption of water for fermentation and distillation is 18.2 KLD (approx)

waste water generated from above process is 11.7 KLD (Approx). Effluents

generated from the process are discharged to concrete made closed pit

(10x10x11) cu. feet situated inside the premises and then routed to ETP for

treatment. Treated water from ETP will be reused for cooling purpose and

process. Other, wastewater generation will be mainly due to the sanitary

wastewater generated due to domestic uses. There will be ‘zero discharge’

from the unit and there will not be any contamination of surface water bodies

or ground water due to effluent discharges.


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Waste Generation and Management

The manufacturing unit will generate solid waste & liquid effluents and will be

fully equipped to handle its domestic sewage.

The plant will not have any gaseous emissions. All air emissions of the plant

through stack will be through the most efficient pollution control equipments

and will not have any adverse impact on the land or marine environment.

Solid Waste Generation and Utilization

No hazardous waste will be generated either in the process or pollution

control facilities. There will be solid wastes from the process. All domestic

waste will be routed to septic tank and then to soak pit.




Table 3.6-Solid Waste Generation & Management

Sl.

No. SOURCE OF

GENERATION

QUANTITY IN Kg MANAGEMENT PLAN

1

Mahua Flower Residue Generation

1141.68 Kg/day

Will be completely stacked inside the factory premises and then sun dried & sold as Cattle Feed

2 Waste from rice husk

fired

Bhatti(Ash)

948.72 Kg/day Will be sold for fly ash brick

making unit.

3 Used Oil / Lubricants 0.7 Liter Will be sold to authorized

Re-processors.

Noise Levels

The noise generation from the unit is minimal. The noise levels at the

periphery of the plant are well within the stipulated norms of noise pollution.

Green Belt Development

Greenbelt will be developed along with the project. The total greenbelt area

will be around 0.04 Ac (20 % of total area.)The main objective of the

greenbelt is to provide a barrier between the plant and the surrounding

areas. The greenbelt helps to capture the fugitive emissions and to attenuate

the noise generated in the unit apart from improving the aesthetics of the

plant site. The Greenbelt will be adequately sized and will have a suitable

density so as to mitigate the effects of emissions from the unit. Roads for


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vehicular movement will be paved and adequate mitigation measures will be

provided to prevent fugitive emissions.


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Annexure-4

10 km radius Google Map


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pre feasibility report on proposed production of …...pre feasibility report on proposed production...

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