Embed Size (px)
Citation preview
Environment Management Plan
for
195KLD Grain Based Fuel Ethanol
Plant & 6 MW Co- Generation Power
Plant
At
Village – Khapa Tehsil - Waraseoni
Distt - Balaghat (MP)
Proposed By M/s Visag Biofuels Pvt Ltd
Shreeji Mall
Mahaveer Chowk, Balaghat MP 481001
ENVIRONMENT MANAGEMENT PLAN (EMP)
1. INTRODUCTION
Visag Biofules Pvt. Ltd. is a company interested in venturing into manufacturing of fuel
ethanol and its by-products like CO2, DDGS and captive power generation. The project
will be based on MULTI FEED grains like broken rice, maize, FCI Rice etc for utilization of
their starch to manufacture bio-ethanol and other constituents like protein & fibre to
produce value added cattle feed. The group wants to generate this environment
friendly fuel to promote the concept of sustainable development as well as to promote
Agro-based industries with assured returns for the farmers. By setting up distilleries and
manufacturing fuel ethanol. This venture would boost job opportunities and would also
spur indigenous technological development. According to the Govt. of India Ethanol
Blending Programmed (EBP), India aims to achieve 20% ethanol blending in petrol by
2025.Thus ethanol from multifeed Grains for consumption, would be a great boost to the
EBP plan execution.
Visag Biofules Private Limited is a company, incorporated under Companies act, 1956,
at Balaghat M.P. The company aims to set up a 195 KLPD Multi Feed Based distillery and
will procure around 11.3514 hectare of land for the proposed project in Vill. Khapa,
Tehsil- Waraseoni , Dist. Balaghat M.P.
Sufficient area will be made available for green belt development and Effluent
Treatment Facilities as it plans for zero liquid discharge
A good network of internal as well as main approach roads would be prepared. The
unit would be designed in versatile fashion by adopting latest CDM (Clean
Development mechanism) process techniques as well as with latest state-of-the art
machinery. The project would be formulated in such a fashion and manner so that
utmost Safety Norms & Environment Protection shall be taken careof.
The Promoters:
The promoters are well experienced in business, management, technology and process
orchestration and have made a thorough study of the entire project, planning as well
as implementation schedule. The company will have well defined managerial and
technical team looking after entire operation. Shri Atul Vaidya will be director of the unit
and shall be look after entire project under his supervision.
Following are the directors of the Company
1. Shri Atul Vaidya Ward no 06 Balaghat MP
2. Shri Gyanendra Singh Jabalpur MP
3. Shri Riyaz Uddin Farooqui Bhopal MP
2. BRIEF DESCRIPTION OF NATURE OF THE PROJECT
The present proposal is for setting up a grain based 195 KLD of fuel ethanol unit with
cogeneration of power (6 MW) at Village – Khapa, Tehsil- Waraseoni, Dist. Balaghat
(MP) in the State of Madhya Pradesh at an estimated cost Rs. 155.07 Crores.
The Products will have specified as 195 KLPD of fuel ethanol. The by product is identified
as CO2 which will generate at about -145 TPD (total generation). DDGS 96-98 TPD) shall
also be recovered from the proposed unit
The Company proposes to set up an integrated pollution free (Zero discharge) Distillery
Complex in the State. The proposed Industrial Complex shall process waste and coarse
grains as its raw material to produce fuel ethanol, CO2 etc. :
Silent Feature Of The Project
Liquefaction:
1. Maximum conversion of starch to sugar
2. Recycle of lees thus minimizing the fresh water requirement.
Fermentation:
1. High alcohol productivity with high efficiency of fermentation of up to 92%.
2. Higher alcohol content in the fermented mash, thus lower steam requirement.
3. High ease of operation
4. Design of equipment, piping and provision of cleaning in place ensures minimum
bacterial activity.
5. Mash coolers designed to reduce the possibilities of choking.
6. Water recycle and reuse system reducing fresh water requirement.
Distillation:
1. Plant with maximum heat integration to produce alcohol with lowest energy
consumption.
2. Energy efficient integrated system Distillation efficiency up to 99.5% whilst
producing AA
3. Well-engineered plants with high efficiency trays to ensure elaborate separation
and removal of impurities ensuring superior quality of Spirit.
Proper care in design of calming zone on trays, large area of down-comers, gas-
liquid separators with tangential entry and vapor bottles ensures proper gas-liquid
disengagement and eliminates chances of liquid carryover
4. Mash column with hyper stat Rh Grid trays ensure high turbulence on tray, this
minimizes chances of scaling. Also, this special construction of trays and access to
each tray helps in easier cleaning of column internals.
5. Condensers are designed with multiple passes to ensure high velocity and to
minimize scaling inside tubes.
6. Water recycle and reuse system reducing fresh water requirement.
Integrated Evaporation:
1. Concentrated spent wash up to 40 % w/w solids with low steam.
2. The process condensate after the condensate treatment used as cooling tower
make up thus reducing the fresh water requirement.
3. Possibility of Higher value realization obtained from mixing of syrup with wet cake in
the dryer.
4. Water recycle and reuse system reducing fresh water requirement.
Dryer:
1. Multiple working references
2. Low Temperature drying – No product degradation
3. 100 % syrup can be consumed
4. Robust construction
Process Condensate Treatment Plant:
Designed to treat process condensate + Cooling Tower Blow down + Dryer vapour
condensate thus enhancing recycle and reducing fresh water requirement to up to
5.2lit/lit for Distillery process
1. Technology available indigenously with successful plants running based on the
technology with focus on reducing water ,energy and carbon footprint
2. Provided with most efficient Fed batch Fermentation technology
3. Distillation operating on Multi-Pressure Technology – an efficiently heat
integrated system, operating on fully automated PLC control system
4. Most efficient process technologies for liquefaction, fermentation, MPR
distillation, dehydration and evaporation to attain maximum and sustainable plant
outputs
5. Extensively process and heat integrated system to reduce energy consumption
6. Water management design based upon three principles of reduce, reuse and
recycle water to minimize fresh water requirement.
7. Zero effluent and liquid discharge norms applied while designing the plant.
8. Ethanol produced from the proposed 1G ethanol facility will be as per Indian
specifications (IS 15464:2004) of anhydrous ethanol for use of blending in
automobile fuel.
3. SALIENT FEATURES OF THE PROPOSED PROJECT
Salient Features of The proposed Project
Site Address Khasara No. Part of 448/1 & 448/2
village Khapa – Tehsil- Waraseoni Dist.
Balaghat (MP)
Production Capacity Grain base fuel ethanol unit of 195 KLPD
along with 6.0 MW Power Plant and 145
TPD CO2 generation
Cost of Project 155.07 Crore
Grain Requirement ( Broken Rice/ Corn/Maize) 420 MT
Boiler capacity at MCR (100% Load) 45 TPH @ 45 Bar
Steam Requirement 35 TPH @ 3.5 kg/cm2(g)
Fuel Requirement 192 TPD coal
Total water Requirement 3400 KLD
Total Recycling of Water 2185KLD
Net Fresh Water Requirement 1215 KLD
Spent Wash Generation 1170 TPD
DDGS Generation 96-98 TPD
Ash Generation from Boiler 58 TPD
Operating Power Requirement 5325KWH
Capital Cost for Environmental measures MEE,
Dryer, BG for boiler (proposed )
2752 Lacs
Recurring cost for environmental Management
etc ( Proposed )
92-95 Lacs
Total Acquired Land 11.3514ha
Total Built Up area of Plant 2.4379ha
Proposed area for plantation 4ha
Alternative Source of Power DG set of 1010 KVA
Employment Generation 185 no.
4. ENVIORNMENT SETTING OF THE PROECT
S.
No.
Particulars Details
1. Locations
A. Village Khapa
B. Tehsil Waraseoni
C. District Balaghat
D. State Madhya Pradesh
Toposheet No. 64C/1, 64C/2, 55O/14, 55O/13
2. Latitude
Longitude S. no. Latitude Longitude
1 21°46'7.83"N 79°59'57.64"E
2 21°46'16.16"N 80°0'1.24"E
3 21°46'18.98"N 80°0'8.51"E
4 21°46'23.04"N 80°0'9.58"E
5 21°46'20.30"N 80°0'9.70"E
6 21°46'19.17"N 80°0'13.34"E
7 21°46'17.66"N 80°0'12.06"E
8 21°46'16.36"N 80°0'14.99"E
9 21°46'9.50"N 80°0'10.41"E
10 21°46'10.50"N 80°0'7.58"E
11 21°46'4.60"N 80°0'2.99"E
3. General ground level Highest elevation – 322 m
Lowest elevation- 313 m
4. Nearest Highway Rampayli-Waraseoni road-3.00-
5. Nearest Railway Station Sawangi Railway Station – 2.75 km
6. Nearest Airport Nagpur airport -120.25 km
7. Nearest Tourist Place within 10km
radius None within 10 km Radius
8. Archaeological Important Place
within 10km radius None within 10 km Radius
9. National park/Wild Life Sanctuaries
within 10km radius None within 10 km Radius
10. Reserved / Protected Forest within
10km radius (Boundary to boundary
distance)
Protected forest -0.10 km-NW
11. Nearest major city with 100000
population within 10km radius
Waraseoni -4.50 km- E
12. Nearest Town / City within 10km
radius
Waraseoni -4.50 km- E
13. Nearest Village Khapa -1.75 km- SE
14. Nearest River Chandan river-1.25 km-NNE
15. Nearest Lake/ Ponds Pond -0.50 km- E
Pond -0.75 km-ENE
Pond -1.75 km – E
Pond -1.25 km- SE
Pond -1.75 km –SSE
Pond -1.75 km –SSW
Pond -3.25 km –NNW
Pond – 3.75 km –NNW
Pond- 5.50 km –ENE
Pond -8.25 km -ESE
16. Nearest Nadi / Nala Wainganga canal-0.50km –SE
Kas nala -2.15 km-NNW
Canal – 2.50 km –N
Tandoiya nala -7.75 km – SE
Katangjhari canal – 3.75km- NNE
17. Nearest Hill Ranges None within 10 km Radius
18. Industry located within 10km radius None within 10 km Radius
Google Image of the site
5. ENVIORNMENT MNGEMENT PLAN
5.1 AIR ENVIRONMENT
Particulate matters & other gaseous emission are envisaged as pollutant from boiler,
whereas fugitive emissions are also envisaged from various material transfer points.
To mitigate the impact of pollutants from boiler stack, sources of fugitive emission and
vehicular traffic during the operational phase of the site, following measures are
proposed for implementation:
• ESP shall be provided at stack of boiler to control the emission below 50 mg per cubic
meter.
• Provision of Good quality of coal for boiler , whenever it is used instead of rice husk
• Adequate stack height of 46 mt for boiler and 30 mt for the DG set (1X1010 KVA) shall
be provided for better dispersion.
• Provision of Dust collectors system at various material transfer points.
• Provision of Online continuous monitoring system for stack of boiler
• Provision of regular Ambient air quality monitoring to ensure that ambient air quality
shall be met the limit
• Development of green belt in time bound manner in consultation with forest
department.
• Dense phase conveying system for ash (58 TPD) handling shall be provided to prevent
the fugitive emission.
• Provision of enclosure for all the loading & unloading operations, where ever required.
• Provision of cover over coal conveyors belt along with dust suppression system
• Provision of dust mask for workers and instruction of compulsory use.
Details of Pollution Control Equipments
Sl.
No.
Pollution Control
Equipments
Description
1 ESP The height of stack is proposed as 46 mt. The ESP will be
provided at boiler stack to control the air pollution and
to meet the norms fixed by State Pollution Control
Board.
2 Coal Storage and
Handling
Coal will be conveyed by road and it will be unloaded
and stored in the covered shed. Coal will be
transported to plant by belt conveyor. Water spraying
arrangement shall be provided over the belt conveyors
to prevent fugitive emission during handling of coal.
3 Handling of fly ash
generated from Co
gen Plant
The quantity of fly ash going with the flue gases from
boiler at different zones viz furnace, bank tubes,
economizer & ESP will be collected and conveyed to
common bunker by dense phase conveying system.
The fly ash from the common bunker will be conveyed
to silo. The whole system is totally enclosed and no
emission will be generated.
Control and Monitoring Of Secondary Fugitive Emissions
Fugitive emissions from the proposed plant would be significant considering the
activities like material handling & milling, transfer points of materials and movement of
vehicles. These operations generate dust. Specific instances of fugitive dust generation
may include dust blown by wind from the raw-materials stockpile, dust caused by
vehicular traffic within & outside of the factory, dust leakage from conveyors, conveyor
transport points, storage hoppers and packers etc, Good housekeeping, proper
maintenance, wetting of dusty areas, use of enclosed storage wherever feasible etc.,
will considerably reduce fugitive dust. M/s Visag Biofules Pvt. Ltd. proposes the following
measures to control the fugitive emission:
Provision of earmarking of storage area.
Provision of enclosure for points of loading & unloading and transfer operations.
Regular spraying of water over internal road and approach road to control dust
Development of green belt around the periphery of plant and along the road to arrest
the fugitive emissions.
Provision of regular training to the personnel operating and maintaining fugitive
emissions control systems.
Provision of pucca road within the plant premises.
Prevention of Idle running of vehicles during material loading / unloading operations.
5.2 NOISE AND ODOUR ENVIRONMENT
Noise generating sources in a plant are identified as steam release valves, compressors,
blowers, turbine and DG set etc. No person is required to remain constantly at the
above-mentioned units and will go occasionally to check the systems.
Noise attenuating devices like earplugs and earmuffs shall be provided to workers
exposed to high noise levels. Noise barriers, silencer and enclosures shall be
incorporated in the equipments, which emit high noise level. All basic equipments and
various machineries should be kept well maintained. Green belts are good noise
barriers and same will be developed around the plant. The sufficient green belt may be
proposed to control noise levels.
Following are the measures proposed to control the higher noise level.
Provision of acoustic enclosure for STG, DG set
Provision of lining with sound absorbing materials for walls and ceilings of the concerned
buildings.
Provision of insulated enclosures at area close to the high noise sources.
Provision of noise attenuating devices like ear plugs and ear muffs to the workers
exposed to high noise level.
Development and maintenance of sufficient green belt.
Regular monitoring of noise level followed by corrective measures in concerned
machinery.
Maintenance of machinery & vehicles will be done in a sustainable manner to ensure
best performance and less noise.
Disallowing vehicles for parking towards highway. Provision shall made for specified
parking area for vehicle
Continues exposure to workers in higher noise prone area shall be avoided. Workers will
be subjected to regular medical examination for any symptoms of hearing loss.
Provision of training to workers to generate awareness about effects of noise and
importance of using PPEs.
ODOUR MANAGEMENT
Sources of Odour
Odour may be caused due to bad management of fermentation house, long retention
of fermented wash, unattended drains.
Management:
Adaptation of covered fermentation process along with CO2 recovery system
Wet cake will not be stored for more than 36 hours to prevent odour generation
Better housekeeping by regular steaming of all fermentation equipments.
Use of efficient biocides to control bacterial contamination.
Control of temperature during fermentation to avoid in-activation / killing of yeast.
Avoiding storage of fermented wash.
Regular use of bleaching powder in the drains to avoid generation of putrefying micro-
organisms.
Closed operation of the process should be practiced effectively.
5.3 WATER ENVIRONMENT
Total water requirement is estimated as 3400KLD and after recycling & reuse of 2185 KLD
of water, net fresh water requirement is estimated as 1215 KLD, which will be sourced
through Chandan river water supply system.
The sources of water pollution may be from following:
Spent wash from manufacturing process
Cooling water blow down
Boiler blow down
RO Reject
Softener reject from D.M. Plant
It is proposed to provide MEE, Drier, CPU and RO to maintain zero liquid discharge from
the fuel ethanol unit.
Decantation section will comprise of centrifuge decanter for separation of suspended
solids from spent slops coming out of distillation plant. Wet cake will have 32-35% w/w
solids as removed from bottom of decanter and will be mixed with concentrate syrup
from evaporation in ribbon mixer. This mixture known as DWGS having 32-35%w/w solids
will fed to drier where it will be further concentrated using steam to about 90% w/w
solids. This product is known as DDGS. Thin slops coming out of decanter will be
collected in a tank and transferred for part recycle & further for evaporation.
Condensate will be recycled back into the process.
Fresh Water requirement of the plant will be around 1215 KLD and after recycling &
reuse, which is about 4.9kl per kl of production. Water requirement of the plant will be
met by MPIDC resource in combination with and internal recycling of water.
During operation, Grain Slops will be taken through Centrifuge Decanters for separation
of suspended solids.
• Spent wash (1170M3 per day) will pass through centrifuge decanter for separation of
solid. The part of thin slope from centrifuge will be recycled to process.
• The remaining slop will be concentrated through multi effect evaporator.
• The concentrated syrup will be mixed uniformly in the ribbon mixer to form DWGS (150
MT per day). Final product will be in the form of DDGS at 96-98 tons per day.
• DWGS/DDGS powder will be sold as cattle feed.
Treatment Scheme
Decantation Section
• Centrifuge Decanter is used for separation of suspended solid from the spent wash
coming out of the distillation plant.
• Wet cake has 30-35% w/w solids as removed from the bottom of the Decanter.
• Thin slops coming out from decanter will be collected in a tank & transferred for the
partial recycling & remaining for Evaporation.
Evaporation section
The suggested treatment scheme is a Multi Effect Evaporator with thermal
recompression for Thin Slops Evaporation. The following points will elucidate the basic
working principal:
• Shell & Tube type Evaporators with highly efficient liquid distributor working on the
principal of Falling Film Evaporation.
• Analyzer vapors are fed to the 1st effect evaporator shell side at the given pressure &
temperature as the heating medium.
• The Feed is fed from the top of the 1st effect evaporator which is Falling Film Evaporator-
1
• Vapors generated in the 1st effect VLS (vapor Liquid Separator) are used as heat source
in the 2nd effect. 3rd effect is on vapours from second effect. Vapors generated in the
2nd & 3rd effects VLS are condensed on shell side of Surface Condenser for Evaporator.
• Part concentrated solids will be obtained at the outlet of the 3rd effect evaporator. A
shell & tube type multi pass surface condenser is employed for condensing the shell side
vapors.
• The operation of the plant will be under vacuum. Vacuum will be created with the help
of a water ring vacuum pump. Cooling water from the cooling tower is used in the
surface condensers for condensing the vapors.
• Spent lees will be recycled back for Grain liquefaction section &Process condensate is
fed to CPU unit.
• 522TPD @approximate treated water will return back to process for utilization in
liquefaction/fermentation/cooling tower etc. .
• Rainwater will be utilized to recharge the underground resource through scientifically
designed rainwater harvesting system.
• RO reject from CPU will be sent for ash quenching.
Storm Water Management:
The quantity of storm water will constitute runoff from buildings, roads and paved areas.
Contamination of storm water is possible from the following sources:
• Diesel and oil spills from diesel generator & fuel storage area.
• Oil spills and leaks from vehicle parking lots and washing area.
• Leachate generation from the waste.
A detailed “Storm Water Management Plan” will be implemented in consideration of
above sources.
Provision of drainage network in above area.
Regular inspection and cleaning of storm drains.
• Provision of cover at waste storage areas.
• Provision of secondary containment and dykes in fuel/oil storage facilities.
• Preparation of spill response plans, particularly for fuel and oil storage areas.
• Good housekeeping in the above areas.
Water and Mass Balance for the proposed project
5.4 SOLID AND HAZARDOUS WASTE MANAGEMENT
Following will be solid waste management practice to be adopted by unit:
Solid And Hazardous Waste Management
Type Of Waste Quantity Storage Utilization/ Disposal
DDGS – (by product)
96-98 TPD Covered shed Sold as Cattle Feed, Poultry &Fisheries
Boiler ash 58 TPD Silo Brick making or land filling
Waste papers/Boxes
0.1 TPD Covered shed to recyclers
Used Oil <150Lt/Yr HDPE drums
in covered shed
Given to re-cycler
authorized by MPPCB/MoEF
Spent Resin from DM Plant
<30Kg/Yr HDPE drums in covered shed
Given to re-cycler authorized by MPPCB/MoEF
5.5 BIOLOGICAL ENVIRONMENT
Total land area is 11.3514 hact and out of that 4.00ha area is kept for green belt
development which is more than 33% of the area. Which will contribute to increase the
aesthetic beauty of the area and reduction of pollution. Topography of the core zone is
flat. Present land use of the core zone has already has been diversified for industrial
activities.
Time Bound Plantation Programme
Year Area (sq mt) Number of Plants
1st Year 20000 4000
2nd Year 20000 4000
Total 40000 8000
Proposed Plantation Detail
Description Qty Location
Neem 200 Boundary Wall
Putran Jeeva 200 Approach Road and Parking
Bargad 50
Inside the boundary wall at eastern
side
Moleshree 400 CPU & Western Side
Amaltash 400 Road Main Gate - Admin Block
Arjun 400
Along the Boundary wall and
internal road
Gulmohar 500 Road Main Gate – Admin Block
Achar 400 Around canteen
Ficus Benjamina 600 Around Admin Block
Satparni 600 Around Admin Block
Ashoka Tree 500
Around Admin Block and around
boundary limit
Gobar Champa 500
Around Storage area and
distillation Plant
Anjan 300 Boundary wall and around CPU
Bel 100 Near Main Gate
Guava 400 Near water reservoir
Karanj 200 Near water reservoir
Awala 2000
Around Garden and back side of
the unit.
Harra 50
Boundary wall and along approach
road
Jack Fruit 100 Boundary wall
Khamer 100 Near pump house
TOTAL 8000
5.6 HEALTH AND SAFETY
Occupation safety and health is very closely related to productivity and good
employer-employee relationship. Occupational health of workers may be affected by
fugitive emission, dust and noise. Safety of employee during operation and
maintenance of equipment and handling of materials are proposed to be taken care
as per regulations.
The following measures will be taken to prevent occupational diseases and health
hazards.
Pre - employment and periodic medical examination of employees.
Regular monitoring of working environment and implementation of safety and control
measures.
Use of protective equipment, clothing, helmets, gas mask, shoes, etc.
Provision of rest shelters for workers/staff with amenities like drinking water, fans, toilets
etc.
Rotation of workers exposed to high noise area
Dust suppression of road
First-aid facilities in the plant area.
A safety committee under MP Factory Rule 1962 has been constituted.
Emergency Plan duly approved by the Director, Industrial Health and Safety has been
approved.
5.7 SOCIO ECONOMIC ENVIRONMENT
Tota project Cost is 15507 Lacs and 2.0% of the cosst i.e. 310.14Lacs shall be kept for
CER/CSR activities shall be carried out which will be need base of the area and in
consultation with district administration.
S. No. Activities
3 Year Plan for CER/CSR
(in Rs. Lakhs)
Ist IInd IIIrd Total
1.
Health (Infrastructure for Primary Health Center,
Veterinary Hospitals/ Dispensaries) at Khapa,
Waraseoni, Budbuda, Jaliwada, Wara,
50 50 50 150
2.
Actions for COVID-19 (Supply of Hospital beds,
Ventilator, Sanitation equipment, PPE Kits, Body
Temperature Scanner, etc.) at Waraseoni and
50 50
nearby PHC
3.
Education (Construction/ Extension/ additional
facilities e.g. Laboratory, Library, Computer
class, Toilets, Drinking Water Facilities etc. for
village schools) at Khapa, Khandwa, Chandori,
Bodalwara, Mehdiwara,
10 10 10 30
4.
Drinking Water Facilities (Hand Pumps, Wells,
Tap Water, Water Storage Tanks, Deepening &
Cleaning of Ponds, Roof Top Rain Water
Harvesting Structure etc.) at Khapa, Khandwa,
Chandori, Bodalwara, Mehdiwara,
10 10 10 30
5.
Sanitation (Construct Community Toilets,
Construct Drainage System, Solid Waste
Management etc.) at Khapa, Khandwa,
Chandori, Bodalwara, Mehdiwara,
15 15 15 45
9. Others Local Social Needs of Khapa,
Khandwa, Chandori, Bodalwara, Mehdiwara, 5.14 -
5.14
Grant Total 140.14 85 85 310.14
5.8 TRAFFIC MANAGEMENT
The movement of trucks/tanker at the site will be regulated as per the traffic rules
framed and given below:-
Driver of the truck will park the vehicle at the ear marked site and report at the site
office.
After submission of documents/PUC, checking, making entries driver will be given a
TOKEN and directed to report for unloading/loading.
After the TOKEN is checked and verified, truck/tanker will be unloaded/loaded and
allowed to move out.
Only R.T.O. passed and PUC checked vehicle will be allowed for unloading/loading
and up to the permissible limit.
No gate pass will be given to the vehicle to move out unless all safety measures are in
place.
6. COST OF MEASURES UNDER EMP
Sufficient fund allocation will be made towards environmental management and
monitoring program. Following provisions are proposed to be taken for improving,
control and monitoring of environment protection measures
Environmental Monitoring Cost
Segment Plan Action Plan Budget allocation per Annum
(Approx)
Air Environment Monitoring of Environmental Every month Rs. 1,92,000/- @ 4000 per
parameters of AAQM sample
Monitoring of stack emission Continuous On line
system
Rs. 1,00,000 ( Approx)
Water
Environment
Monitoring of ground water (Pre and post
Mansoon )
Rs. 1,20,000/ @ 10,000 per
sample
For 12 sample in a year
Monitoring of Surface water
courses
(Pre and post
Mansoon )
Rs. 1,20,000/ @ 10000 per
sample
For 12 sample in a year
Treated water from Treatment
plant
Monthly Rs. 60,000/ @ 5000 per sample
For 12 sample in a year
Noise
Environment
Monitoring of noise prone
location
Quarterly Rs 64,000/- @ 2000 per sample
for 32 samples in year
Soil
Environment
Monitoring of soil quality
villages around plant site
Yearly Rs. 60,000/ @ 10,000 per
sample
For 06 sample in a year
Health
surveillance
Programme
Regular Health check up of
employees
Once in year for
200 number
Rs 10,00,000/-
(Rs 5000/- per head for 100
number)
Ground water
table
monitoring
Within and surrounding villages
( total 6 samples)
Pre and post
monsoon
Rs 12,000 /- per annum
Misc. - - Rs. 2,00,000/-
Total (A ) Rs 18,28,000/- @18.30
Total Cost (EMP + Plantation + Monitoring )
Sn Particular Proposed Amount (Rs in
Lacs) per annum –
Recurring
1 Dust Suppression through tanker over 3 km road * 6.0m (15
Rs/km ) Approx running per day 18 km @300 day mm= 5400
km
0.80
2 Maintenance of Plantation (Along the Road (500) and Plant
site -8000 ) @ Rs 45/- per plant 3.83
3 Occupational health and Safety exp. @ 185 no Rs 5000 per
workers 9.25
5 Environmental Monitoring cost 18.30
6 O&M cost for APC, CPU, etc 60.00
Grand Total 92.18 Lacs
Capital Investment for proposed Environmental Protection (Rs. in Lacs
S. No. Particular Proposed Cost
1. Bag Filter/ESP 200
2 M.E.E 900
3 Waste Water Treatment Plant for Process Condensate 275
4 Decanter & Dryer 1350
5 Green Belt development (4 Ha) 11.60
6 Occupational Health & Safety (185 no) 9.25 @ 10.0
7 Misc RWH etc 5.00
Total 2751.60 @ 2752
7 TIME BOUND ACTION PLAN FOR IMPLEMENTATION OF MEASURES OF EMP
Activity Action Plan
Water spraying over on the road During construction & operation of plant
Development of green belt at the boundary Immediate (may be started from coming
monsoon)
Cleaning and maintenance of storm water
drain
Before and after monsoon
Installation of Continuous online monitoring
system for proposed 60 KLD unit
Before commissioning of plant
Maintenance and Construction of retaining
wall along the nalla
During construction of plant
Provision and compulsory use of Dust mask,
ear plugs, safety shoos and other PPE to all
workers
During construction and operation of plant
Regular health monitoring (as per rules) of During construction and operation of plant
workers
Provision of rest shelters for plant workers with
amenities like drinking water, fans, toilets etc.
During construction and operation of plant
Socio economic measures During construction and operation of plant
8 CONCLUSION
It can be seen from the foregoing chapters that air emission due to proposed alcohol
plant will not be significant to put the adverse impact on air environment. The TPM
emission from the boiler stack will be below the 50mg/nm3. Adequate stack height and
control measures will be provided.
Zero discharge effluent treatment system shall be provided with a basic principle of
concentrating/evaporating the effluent. Ground water table will is not expected to be
disturbed due to ground water withdrawal as water harvesting system and water
reservoir will be provided.
No significant impacts is envisaged on other environmental aspects such as
meteorology, topography and geology, mineral resources, archaeology, cultural,
religious and land use.
There may be positive impact on socio economic conditions and infrastructural facilities
due to the proposed industry.
Considering the proposal of zero discharge concept, It is requested that necessary
environmental clearance may be granted for the proposed fuel ethanol unit of M/s
Visag Biofuels Pvt. Ltd. with appropriate stipulations.
