PRE - FEASIBILITY REPORT
FOR
PROPOSED 35 KLPD MOLASSES
BASED DISTILLERY PLANT
BY
M/S. SHREE MAROLI VIBHAG KHAND UDYOG
SAHAKARI MANDLI LTD.
SURVEY NO.: 71, 72 & 80 AT-KOLASARA
(KALYAN NAGAR) P.O- MAROLI BAZAR,
TALUKA JALALPORE,
DISTRICT NAVSARI-396436
GUJARAT
SUMMARY
M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd is an existing sugar mill located, at
Survey No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O- Maroli Bazar, Taluka Jalalpore, District Navsari,
Gujarat. Capacity of the existing Sugar Industry is 3000 TCD producing 11200 MT/Month of White Crystal
Sugar. Now Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd has proposed 35 KLPD Molasses
based distillery unit within existing company premises.
PROJECT COST The total cost of the project will be around Rs. 30.0 crores. Total capital cost of pollution control measures
will be Rs. 3.0 crores & recurring cost per annum will be 1.0 crores.
DETAILS OF PRODUCTS Details of existing and proposed products are given in following table.
LIST OF EXISTING AND PROPOSED PRODUCTS AND PRODUCTION CAPACITY
SR.
NO. NAME OF THE PRODUCTS
EXISTING
QUANTITY
ADDITIONAL
QUANTITY TOTAL
(A) PRODUCTS
1 White Crystal Sugar 11200 MT/Month -- 11200 MT/Month
2 Captive Power Plant (In
House During Crushing Season) 5.85 Mw/Hr. -- 5.85 Mw/Hr.
3 Rectified Spirit/Anhydrous
Alcohol -- 35 KLPD 35 KLPD
(B) BY PRODUCTS
4 Molasses 5,200 MT/Month -- 5,200 MT/Month
5 Bagasse 33,500 MT/Month -- 33,500 MT/Month
6 Press Mud 4,200 MT/Month -- 4,200 MT/Month
7 Bio Compost 4,200 MT/Month -- 4,200 MT/Month
REQUIREMENTS FOR THE PROJECT
LAND
No new land will be acquired for the proposed project. Out of total land area (i.e. 1,53,262 m2) around
8,000 m2 open land area will be utilized for the proposed distillery unit.
WATER
For the proposed project additional 506 m3/Day water will be required. Existing water required of the sugar
plant is 428.7m3/Day, after proposed project total water required will be 934.7m
3/Day. Source of water for
existing unit is Borewell/ Canal and for the proposed distillery unit surface water (i.e canal water) will be
utilized.
ELECTRICAL ENERGY For proposed project additional power requirement will be 400 KW/Hr. Existing connected Power load is
299.10 KWH/MT. Power supply shall be full-filled by Dakshin Gujarat Vij Company Limited.
MANPOWER
At present, 237 personnel are working in the sugar industry. For proposed project additional 24 personnel
will be employed who will come from local area. Total manpower after proposed project will be 261
personnel.
FUEL
For the proposed project, energy requirement will be met from existing boiler (2 Nos.) having capacity of
50 and 30 TPH, for the proposed project Baggase (1.9 MT/Hr) will be used as fuel in existing boiler.
SOURCES OF AIR POLLUTION AND CONTROL MEASURES
EMISSIONS FROM COMBUSTION OF FOSSIL FUELS FROM STATIONARY OR MOBILE
SOURCES
Sr.
No. Stack Attached To
Stack Height
In Meter
Air Pollution Control
Devices Parameter
EXISTING
1. Boiler No. 1
(Bidrum Water Tube 50t/Hr) 45.0 (common
stack)
Ventury Type Wet
Scrubber
PM < 150 Mg/Nm3
SO2 < 100 ppm
NO2 < 50 ppm
2. Boiler No. 2
(Bidrum Water Tube 30t/Hr)
Ventury Type Wet
Scrubber
PM < 150 Mg/Nm3
SO2 < 100 ppm
NO2 < 50 ppm
3. D. G. Set
(500 KVA – Stand By) 11.0 --
PM < 150 Mg/Nm3
SO2 < 100 ppm
NO2 < 50 ppm
PROPOSED: No any additional utilities are required for the proposed project.
WASTE WATER GENERATION AND IT’S TREATMENT: Wastewater generated from the sugar factory is being treated in existing ETP unit and treated water is being
used in bio-composting.
Waste water generated from the proposed distillery unit in the form of spent wash will be concentrating in
multi effective evaporator and then sent for bio-composting. Condensate from MEE will be recycled back
to the process, while spent less and other waste water will be treated in ETP units and treated water will be
used for the bio-composting. Thus achieve the’ Zero Liquid Discharge’.
NOISE POLLUTION AND CONTROL MEASURES: From the existing and proposed manufacturing unit noise pollution will generate which will be controlled
by adopting different types of noise pollution control measures. Main sources of the noise pollution are
machineries, Electric motors, etc.
Following noise control measures to be adopted in the existing and proposed project,
� Encasement of noise generating equipment.
� Greenbelt all around the plant boundary.
� In addition personnel, working near high noise level generating sources, will be provided with ear
muffs.
� Proper and suitable acoustic barrier will also be provided around, areas generating high noise.
� Effective preventive maintenance and vibration measurement of all rotating equipment will help in the
improvement of plant life and also noise reduction.
SOLID WASTE GENERATION AND ITS DISPOSAL METHOD The details of solid/Hazardous waste generation and its management are given in the following table.
Sr.
No.
Name of the
Waste
Cat
No.
Existing
(MT/Year)
Additional
(MT/Year)
Total
(MT/Year) Method of Storage & Disposal
1. ETP Waste 34.3 58
(MT/Year) --
58
(MT/Year)
Collection, Storage and used as
Manure.
2.
Used Oil
5.1 1.45
(MT/Year)
0.55
MT/Year
2.0
(MT/Year)
Collection, Storage, transportation
and disposal by selling to GPCB
approved registered recyclers /
reuse.
3.
Discarded
Container/Barrel
s/ Linear
33.3 150
Nos./Year --
150
Nos./Year
Collection, Storage and disposal by
selling to GPCB approved
registered recyclers.
GREEN BELT DEVELOPMENT Company is having total 1,53,262 m
2 land area is available. The company has green belt area with Lawn,
plants and flowers spread across about 33% of the total area. Further it will be developed at plant boundary.
INDEX
CHAPTER
NO. CONTENT
1 Introduction of the Project
2 Project Description
3 Site Analysis
4 Planning Brief
5 Proposed Infrastructure
6 Rehabilitation and Resettlement (R & R) Plan
7 Project Schedule & Cost Estimates
8 Analysis of Proposal
1
CHAPTER-1
INTRODUCTION OF THE PROJECT
1.1 IDENTIFICATION OF PROJECT
M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd. is a sugar industry located at Survey No. 71,
72 & 80 At-Kolasara (Kalyan Nagar) P.O-Maroli Bazar, Taluka Jalalpore, District Navsari, Gujarat. Molasses
is produced as a by-product during manufacturing of sugar. Maroli sugar industry is planning to set up 35
KLPD distillery plant within existing premises using molasses as a basic raw material.
1.2 BRIEF DESCRIPTION OF NATURE OF THE PROJECT
M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd is planning for installation of the molasses
based distillery unit at Survey No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O-Maroli Bazar, Taluka
Jalalpore, District Navsari, Gujarat.
LIST OF PRODUCTS AND PRODUCTION CAPACITY
Sr.
No. Name of the Products
Existing
Quantity
Additional
Quantity Total
(a) Products
1 White Crystal Sugar 11,200 MT/Month -- 11,200 MT/Month
2 Captive Power Plant (In House
During Crushing Season) 5.85 Mw/Hr. -- 5.85 Mw/Hr.
3 Rectified Spirit / Anhydrous
Ethanol -- 35 KLPD 35 KLPD
(b) By Products
4 Molasses 5,200 MT/Month -- 5,200 MT/Month
5 Bagasse 33,500 MT/Month -- 33,500 MT/Month
6 Press Mud 4,200 MT/Month -- 4,200 MT/Month
7 Bio Compost 4,200 MT/Month -- 4,200 MT/Month
1.3 NEED FOR THE PROJECT AND ITS IMPORTANCE TO THE COUNTRY AND OR REGION.
In India economy many industries are dependent over agriculture produce for production of luxury and need
based committees. Alcohol is used in chemical industry as well as for preparation of beverages. The use of
alcohol for the purpose of potable liquor is as high as its use for industrial purpose. As a source of income to
the government, the potable liquor units get assured quota of alcohol. This trend is continuing and will
continue in view of the fact that potable liquor has larger revenue generating potential. Denatured sprits are
Rectified Sprit made unfit for drinking by addition of chemicals which have strong disagreeable odor and
which cannot be easily separated from sprit. Ethyl alcohol is important feedstock for manufacture for basic
carbon base products like Acetic Acid, Butanol, Butadiene, Acetic anhydride, Vinyl acetate, PVC etc. which
are needed in pharmaceuticals, paints and other important industries as they are value added products. Ethyl
alcohol has been a source of large amount of revenue by way of excise duty levied by Government on
alcoholic liquor. Fermented ethyl alcohol has also great demand in countries like Japan, United state, Canada,
Sri Lanka etc. as synthetic alcohol produced by these countries from Naphtha of Petroleum Crude is not
suitable for beverages. Ethylene, Ethylene oxide and mono-ethylene glycol can be manufactured from
petrochemical route. However, latest technological development and taking into account increasing cost of
petrochemical raw material the above mentioned chemicals can be easily manufactured from ethyl alcohol.
1.4 DEMANDS-SUPPLY GAP The gap between the availability of alcohol and the requirement by the industry has been widening. The
existing requirement of alcohol by the industries is around 600 million liters annually. In 1992-93, alcohol
consumed for industrial purpose was 450 million liters and utilization for potable purpose was 434 million
liters. The trend is expected to continue over last 9-10 years.
1.5 EMPLOYMENT GENERATION: For the proposed project additional 24 nos. of personnel (existing 237 nos.) will be employed.
2
CHAPTER-2
PROJECT DESCRIPTION
2.1 TYPE OF PROJECT
M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd is an existing sugar mill located, at Survey
No. 71, 72 & 80 At-Kolasara (Kalyan Nagar) P.O-Maroli Bazar, Taluka Jalalpore, District Navsari, Gujarat.
Molasses is produced as a by-product during manufacturing of sugar. Maroli sugar factory is planning to set
up distillery plant within existing premises of sugar plant to manufacture 35 KLPD Rectified Spirit and/or 35
KLPD Anhydrous Alcohol using molasses as a basic raw material.
2.2 LOCATION
M/s. Shree Maroli Vibhag Khand Udyog Sahakari Mandli Ltd located at Survey No. 71, 72 & 80 At-Kolasara
(Kalyan Nagar) P.O- Maroli Bazar, Taluka Jalalpore, District Navsari Gujarat. It is situated at 21°01'.18.24"
North latitude and 73°54'59.47" East longitude. A map showing location of the presentated in figure-1and
detailed plan layout in shown in figure- 2.
FIGURE- 1 LOCATION MAP
3
FIGURE-2 PLAN LAYOUT
4
2.3 PROCESS DESCRIPTION
MANUFACTURING PROCESS OF DISTILLERY UNIT
The manufacturing process of rectified spirit/ anhydrous alcohol involves two major steps. Molasses is the
basic raw material. Generally sulphuric acid is not required, nutrients like yeast, anti-foam agent etc, will be
used.
Following steps are required for the Ethanol Production.
1) Fermentation Section
Molasses handling: Molasses from the own sugar factory will be utilized for the proposed production.
Molasses is then after weighted, sent for storage or to the process diluter tank.
Yeast Propagation: Best strain of yeast is required for the production of alcohol, yeast is bought from nearby
vendor and is developed further in propagation section and maintain the viable cell population of about 300
million cells/ml by yeast recycling and continuous aeration of the fermenter.
Fermentation: When Yeast is added in container, yeast works on sugar present in molasses, break down the
sugar into alcohol and carbon-dioxide, required temperature controlled to be 30-32°C (by circulating cooling
water). From Fermenter CO2 collected and directed to scrubber. Remaining content is “wash”.
2) Distillation Section
The “wash” from the fermentation enters into distillation section. The hardware contains columns basically
for two functions, namely Stripping and Rectification. Thus, 1) Analyser column – Operated under vacuum
and 2) Rectifier cum Exhaust Column – operated under pressure. (Additional columns only for refinement).
The “wash” from fermentation is first preheated in heater and fed to analyser column. Alcohol from the wash
in form of vapour from the analyser column is fed to pre-rectifier column (under vaccum). The impure spirit
drawn from the top of column were collected at bottom which is fed into the rectified cum exhaust column
(under pressure). Alcohol is enriched towards the top and drawn out as Rectified Spirit about 95% v/v
concentrations. Fusel oil generated is drawn out to tank, washed with water, decanted, layers separated and
alcohol layer returned as recovery.
3) Molecular Sieve Dehydration
Molecular sieve dehydration is to produce anhydrous alcohol from rectified spirit. Water molecules are
absorbed on the pore surface and the larger alcohol molecules are excluded and exit from the sieve unit. The
absorption is a vapour phase process and hence, rectified spirit, vaporized and super heated in a
vaporizer/column is passed through sieve unit. Generally there are two sieve units. One is under adsorption
while the other is under regeneration. The cycle time for adsorption and regeneration varies from 5 to 10
minutes. Thus forms Absolute Alcohol of desired 99.8% v/v purity. There is alternate Sieve Bed 2 ready for
next operation.
4) Multi-Effect Evaporation
Spent wash from the process is fed into bio-digester thus result in recovery of bio-gas and also reduce the
COD and BOD. Then after spent wash will be sent in multi effective evaporator. Whole process is under
vacuum and vapor generated are compressed and used as steam. Condensate water generated from
evaporation will be recycled back into the process.
5
PROCESS FLOW DIAGRAM OF MOLASSES BASED DISTILLERY AFTER PROPOSED
Water requirement and waste water generation for 35 KLPD molasses distillery
WATER CONSUMPTION KLD WASTE WATER GENERATION KLD
For Fermentation 263 Drift + Evaporation + pure from
cooling from tower 93
For Dilution 21 Spent Lees 4
For Cooling Tower 187 Spent Wash 373
For Boiler 28 Steam condensate Evaporation Losses 28
Miscellaneous 5 Miscellaneous 5
Domestic 2 Domestic 2
TOTAL 506* TOTAL 506
*Above table represents maximum fresh water requirement.
2.4 RAW MATERIALS REQUIREMENT
Details of raw material consumption are given in following table.
LIST OF RAW MATERIALS
Sr.
No.
Name of the Raw
Material
Existing Quantity
(MT/Month)
Additional Quantity
(MT/Month)
Total
(MT/Month)
1. Sugar Cane 93,000 -- 93,000
2. Lime 205 -- 205
Molasses Storage
and Handling
Fermentation
Multi-Pressure
Distillation
Spent wash
Rectified spirit/ Anhydrous
Alcohol
Bio -
Methanation
Multi-Effect Evaporator
Condensate
Process/Cooling
Sent for Bio -
composting
Bio-gas
recovered
6
Sr.
No.
Name of the Raw
Material
Existing Quantity
(MT/Month)
Additional Quantity
(MT/Month)
Total
(MT/Month)
3. Sulphur 47 -- 47
4. Phosphoric Acid 4.5 -- 4.5
5. Hydrochloric Acid 0.01 -- 0.01
6. Caustic Soda (Sodium
Hydroxide) 1.11 10.5 11.61
7. Urea -- 0.8 0.8
8. Antifoam Agent -- 1.74 1.74
9. Molasses (From own
Sugar factory) -- 4,200 4,200
10. Yeast (Active Dry
Yeast/Distiller’s Yeast) -- Own Propagation
2.5 RESOURCE OPTIMIZATION / RECYCLING AND REUSE IN THE PROJECT
Water as a resource is recycled at each possible step of the process and latest technology and methodology
will be adopted to conserve and reuse the resources. Waste water generated from the process goes to ETP and
treated water after pH corrections is used back again into the various processes and remaining is used for the
horticulture purposes.
2.6 AVAILABILITY OF WATER ITS SOURCE, ENERGY / POWER REQUIREMENT AND
SOURCE
2.6.1 WATER REQUIREMENT
For the proposed project additional 506 m3/Day water will be required. Existing water required of the sugar
plant is 428.7m3/Day, after proposed project total water required will be 934.7m
3/Day. Source of water for
existing unit is Borewell/ Canal and for the proposed distillery unit surface water (i.e canal water) will be
utilized.
2.6.2 POWER REQUIREMENT
For proposed project additional power requirement will be 400 KW/Hr. Existing connected Power load is
299.10 KWH/MT. Power supply shall be full-filled by Dakshin Gujarat Vij Company Limited.
2.6.3 FUEL REQUIREMENT
SR.
NO. FUEL
DAILY FUEL CONSUMPTION SOURCE & MODE OF
TRANSPORTATION EXISTING PROPOSED TOTAL
1. Diesel 15 Lit / Hr -- 15 Lit / Hr From Nearest Petrol Pump
2. Baggase 40 MT / Hr 1.9 MT/Hr 41.9 MT/Hr Within own sugar factory
premises
2.7 QUANTITY OF WASTES TO BE GENERATED (LIQUID, AIR AND SOLID) AND THEIR
MANAGEMENT / DISPOSAL
2.7.1 WASTE WATER GENERATION
For the proposed project additional 506 m3/day water will be generated. Existing waste water generation of
the sugar plant is 563.71m3/day, after proposed project total waste water generation will be 1069.71m
3/Day.
Waste water generated from the proposed distillery unit in the form of spent wash will be concentrating in
multi effective evaporator and then sent for bio-composting. Condensate from MEE will be recycled back to
the process, while spent less and other waste water will be treated in ETP units and treated water will be used
for the bio-composting. Thus achieve the’ Zero Liquid Discharge’.
7
2.7.2 AIR POLLUTION
EMISSIONS FROM COMBUSTION OF FOSSIL FUELS FROM STATIONARY OR MOBILE
SOURCES
SR.
NO. STACK ATTACHED TO
STACK
HEIGHT IN
METER
AIR POLLUTION
CONTROL
DEVICES
PARAMETER
EXISTING
1. Boiler No. 1
(Bidrum Water Tube 50t/Hr) 45.0 (common
stack)
Ventury Type Wet
Scrubber
PM < 150 mg/nm3
SO2 < 100 ppm
NO2 < 50 ppm
2. Boiler No. 2
(Bidrum Water Tube 30t/Hr)
Ventury Type Wet
Scrubber
PM < 150 mg/nM3
SO2 < 100 ppm
NO2 < 50 ppm
3. D. G. Set
(500 KVA – Stand By) 11.0 --
PM < 150 mg/nM3
SO2 < 100 ppm
NO2 < 50 ppm
PROPOSED: No any additional utilities are required for proposed project.
2.7.3 SOLID WASTE GENERATION AND THEIR DISPOSAL
The sources of solid wastes, generation and its management are as given in the following table.
SR.
NO. WASTE
EXISTING
QUANTITY
(MT/M)
PROPOSED
QUANTITY
(MT/M)
TOTAL
QUANTITY
(MT/M)
DISPOSAL
1. ETP Waste 58.0
(MT/Year) --
58.0
(MT/Year)
Collection, Storage and used as
Manure.
2.
Used Oil
1.45
(MT/Year)
0.55
MT/Year
2.0
(MT/Year)
Collection, Storage, transportation
and disposal by selling to GPCB
approved registered recyclers.
3.
Discarded
Container/Barrels/
Linear
150.0
Nos./Year --
150.0
Nos./Year
Collection, Storage and disposal
by selling to GPCB approved
registered recyclers.
8
CHAPTER-3 SITE ANALYSIS
3.1 CONNECTIVITY
3.1.1 RAIL
The nearest railway station is Maroli Railway station, which is around 2 km in west direction from the project
site.
3.1.2 ROAD
The site is well connected by road network to all the key places. The major highway passing near the project
site is NH - 8 which is approximately 6 km East direction from the project site.
3.1.3 AIR
The nearest airport from the project site is Surat Airport. The distance of airport from project site is around 21
km in North West.
3.1.4 COMMUNICATION
Project Site is well connected with telephone, telefax etc. all the communications facilities are well developed
in the district.
3.2 TOPOGRAPHY
Topography of the land is plane.
3.3 EXISTING LAND USE PATTERN
There is no Forest, National park; Wild life sanctuary within a radius of 10 Km. For the proposed project
existing infrastructure land will be utilized.
3.4 EXISTING SOCIAL STRUCTURE
Project site is located at a distance of around 9 km from Navsari city. All the infrastructures are available
within city like Schools, Hospitals & community facilities.
9
CHAPTER – 4 PLANNING BRIEF
4.1 PLANNING CONCEPT
Molasses is the by-product in processing sugar cane for production of sugar. In general the molasses
production is about 4.5% on cane crushed. The Carbohydrates in Molasses are already in the form of Sugars.
Hence molasses does not need any pretreatment for production of Alcohol. Repeated evaporation and
Centrifugation decreases the sugar content of molasses and increases the viscosity and concentration of salts
and other impurities. The residual syrup thus becomes thick, viscous and brown in colour and is very heavy.
The concentration of molasses is normally measured in Brix.
Molasses Scenario of India
Details of Molasses Production in India (Source-Indian Sugar Mills Association)
Season 2008-09 2009-10 2010-11 2011-12 2012-13 2013-14
Molasses
Production 6.542 8.40 10.97 11.824 11.744 10.881
4.2 LAND USE PLANNING
The plant general layout has been planned considering production facilities, auxiliary and ancillary facilities
and plant utilities & services. Out of the total plot area (1,53,262 m2) around 8000 m
2 of open area from the
existing unit will be utilized for the distillery plant.
4.3 AMENTIES / FACILITIES
Adequate storage facility for chemicals, machinery spares and consumables shall be provided. A small
mechanical and electrical/ instrument workshop facilities for repairs and maintenance shall be provided. Time
and security offices shall be provided in the plant. To avoid fire hazard, internal fire hydrants system unit will
be provided.
10
CHAPTER – 5 PROPOSED INFRASTRUCTURE
5.1 INDUSTRIAL AREA
No new land will be acquired for the proposed project. Out of total land area (i.e. 1,53,262 m2) around 8,000
m2 open land area will be utilized for the proposed distillery unit.
5.2 RESIDENTIAL AREA
There is no provision of housing for the employees at site.
5.3 GREEN BELT
The main objective of the green belt is to provide a barrier between the source of pollution and the
surrounding areas. The green belt helps to capture the fugitive emission and to attenuate the noise generated
apart from improving the aesthetics. Development of green belt and other forms of greenery shall also prevent
soil erosion and washing away of topsoil besides helping in stabilizing the functional ecosystem and further to
make the climate more conducive and to restore water balance. The company has green belt area with Lawn,
plants and flowers spread across about 33% of the total area. Further it will be developed at plant boundary,
road side, around offices & buildings and Stretch of open land.
The selection of tree species suitable for plantation at the industry are governed by guiding factors as stated
below:
• The trees should be tolerant to air pollutants present in the area
• The trees should be able to grow and thrive on soil of the area, be evergreen, inhabitant, having
minimum of leaf fall.
• The trees should be tall in peripheral curtain plantation and with large and spreading canopy in
primary and secondary attenuation zone.
• The trees should posses extensive foliar area to provide maximum impinging surface for continued
efficient adsorption and absorption of pollutants.
• The trees should be fast growing and indigenous and should maintain ecological, land and
hydrological balance of the region.
• It is also recommended to plant few trees, which are sensitive to air pollution, as air pollution
indicator.
• It is also recommended to carry out extensive plantation within premises.
Keeping in view the climatic conditions, status of soils and vegetation types in and around the project area the
species shall be selected for proposed green belt development.
5.4 SOCIAL INFRASTRUCTURE
Drinking water facility, proper sanitation, etc. will be provided to the workers working in plant.
5.5 CONNECTIVITY
As discussed earlier, proposed location of the plant is already well connected with the network of road & rail.
So there is no need to construct any new road or rail for the transportation.
5.6 WASTE WATER MANGAMENT
Waste water generated from the proposed distillery unit in the form of spent wash will be concentrating in
multi effective evaporator and then sent for bio-composting. Condensate from MEE will be recycled back to
the process, while spent less and other waste water will be treated in ETP units and treated water will be used
for the bio-composting. Thus achieve the’ Zero Liquid Discharge’.
11
5.7 INDUSTRIAL SOLID WASTE MANAGEMENT
From the proposed project activity detail for the solid/hazardous waste generation are given in below table.
DETAILS OF SOLID & HAZARDOUS WASTE GENERATION DURING OPERATION
SR.
NO.
NAME OF
THE
WASTE
CAT
NO.
EXISTING
(MT/YEAR)
ADDITIONAL
(MT/YEAR)
TOTAL
(MT/YEAR
)
METHOD OF
STORAGE &
DISPOSAL
1. ETP Waste 34.3 58.0
(MT/Year) --
58.0
(MT/Year)
Collection, Storage
and used as Manure.
2.
Used Oil
5.1 1.45
(MT/Year) 0.55
MT/Year
2.0
(MT/Year)
Collection, Storage,
transportation and
disposal by selling to
GPCB approved
registered recyclers /
reuse.
3.
Discarded
Container/Ba
rrels/ Linear
33.3 150.0
Nos./Year --
150.0
Nos./Year
Collection, Storage
and disposal by selling
to GPCB approved
registered recyclers.
12
CHAPTER – 6
REHABILITATION AND RESETTLEMENT (R & R) PLAN
The project is located on private land, which is already acquired and there is no habitat. So the project
proposal does not involve any Rehabilitation & Resettlement.
13
CHAPTER – 7
PROJECT SCHEDULE & COST ESTIMATES
7.1 TIME SCHEDULE FOR THE PROJECT
The implementation of the project will involve major activities like preparation of specification / drawings,
issue of tenders, receipt of quotations, scrutiny of tenders, placing of orders, civil & structural construction,
delivery & erection of equipment, test trial runs of various items of equipment and commissioning of the plant
& equipment and completion of the project will take about 6 months after the necessary clearances are
available, and the funding for the project has been tied up.
7.2 ESTIMATED PROJECT COST
The total cost of the project after proposed project will be around Rs. 30 crores. Total capital cost of pollution
control measures will be Rs. 3 crores & recurring cost per annum will be 1 crores.
7.3 BUDGETORY PROVISIONS FOR EMP
Adequate budgetary provisions have been made by the management for execution of environmental
management plans. The details of capital and recurring (per annum) budget earmarked for pollution
control / monitoring equipment; operation and maintenance of pollution control facilities, for greenbelt
development and maintenance.
COST OF ENVIRONMENTAL PROTECTION MEASURES
SR.
NO. PARTICULATES RS. IN CRORE
1. Capital Expenditure 3.0
2. Recurring expenditure on environmental management cell and on
pollution control systems per annum. 1.0
14
CHAPTER – 8
ANALYSIS OF PROPOSAL
8.1 FINANCIAL AND SOCIAL BENEFITS
The capital cost of the distillery unit in existing premises is estimated about Rs. 30.0 Crores for the
installation of plants & machinery along with required auxiliary and balancing facilities for the production.
For the coming of this project surrounding area will get developed due to this project and through the
Corporate Social Responsibility (CSR) activities, socio-economic status of the region will also get developed.
