DCM Shriram Ltd. Plans To Set Up 200 KLPD Distillery with Captive Power
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DCM Shriram Ltd. Plans To Set Up
200 KLPD Distillery with Captive Power
DCM Shriram Ltd. plans to set up a Molasses based Distillery Plant having capacity of 200 KLPD along with 6 MW Co-Generation Power Plant (Coal/Bagasse/Rice Husk ) at Hariawan in Hardoi District, Uttar Pradesh.
Distillery : 200 KLPD
Captive Power Plant : 6 MW
CO2 Plant
Total Working Days in a year : 330 days
Project Cost : Rs. 188 Crores
Location : Hariawan, Hardoi District, Uttar Pradesh
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Note: DCM Shriram Limited is having 4 Nos. sugar manufacturing units in U.P. named DSCL Sugar - Ajbapur, District Lakhimpur Kheri and DSCl Sugar- Loni, Rupapur & Hariawan all in District Hardoi.
The proposed plant is adjacent to nearby Sugar Mill named DSCL Sugar- Hariawan having 7500 TCD capacity and for this proposed distillery project Molasses and Bagasse will be sourced from the Sugar Mills.
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As on February 10, 2016 : The Project is under Planning Stage.
The unit would come up within the premises of its existing 16.75 Ha of Land .
Out of this about 33% (5.53 ha,) of the area will be developed as Green Belt.
IMPORTANT: As per the the discussion we had
on 06.02. 2016 with DCM Shriram Ltd.
the Project is under Panning Stage.
The company is waiting for Environmental clearances .
The Project is
Scheduled to be Completed in
18-24 Months from the date of commencement of the project work.
=======================================
So, this is the RIGHT TIME to contact and Follow Up at following address
to obtain the detailed Enquiry of each product in time and to
submit your quotation subsequently.
The Main Scope of Supply includes:
Boiler : *60 TPH - 1 No.
Fuel(as avialable) : Coal/Bagasse/Rice Husk)
Fuel Consumption: Coal : 625 Ton/Day /
Bagasse/Rice Husk : 310 Ton/Day
Heat Exchanger, Air Pre-Heater/ Economiser
===============================
Steam Requirement (*Break Up):
Multi-pressure Distillation : 28.10 TPH
Multi Effect Evaporator : 19.75 TPH
Boiler Deaeration : 2.15 TPH
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Total : 50 TPH
Boiler with 1 X 60 TPH capacity is proposed to be installed.
===============================
Raw Materials :
Molasses : 915 TPD Ton/Day
- Sulphuric Acid
- Sodium Hydroxide (Caustic)
NH2-CO- NH2 (Urea;46 % N2)
Air Pollution Control Equipment :
Electrostatic Precipitators/ Bag Filter
1; ESP with stack of adequate height will be installed with the boiler to control the particulate and gaseous emissions due to combustion of fuel.
2. CO2 produced during the fermentation process will be collected and utilized as an industrial gas.
3. DG Sets with acoustic enclosures will also have adequate stack height as per CPCB Guidelines.
4. All the internal roads will be asphalted.
5. Development of Green Belt around the periphery & within the premises of the plant will help in attenuating the pollutants emitted by the plant.
Power Requirement and Source:
The company’s proposal is to install 6 MW Co – Generation Power Plant.
Steam generated from the boilers of will be utilized in the generation of 6 MW which will be for own consumption.
Steam generated from boiler will also be used for boiler feed water heating and distillery.
Fuel in the steam boiler will be burnt with the help of air in the boiler furnace. Water will be circulated in the boiler drum and tubes thus getting heated by the flame burning in the boiler furnace. Water comes out of the boiler drum located at the top of the boiler as steam. Flue gases rise in the boiler furnace and come in contact with the steam coming out of boiler drum. Steam after coming in contact with flue gases gets heated up further thus getting superheated. Super heated steam leaves the boiler in a pipe. Flue gases after super heating the steam pass through economizer where they pre-heat the boiler feed water before it enters the boiler drum. After economizer, flue gases pass through air pre-heaters where they heat the air which is
fed to the boiler furnace for burning the fuel. After air pre heaters flue gases pass through an Electro Static Precipitator where the dust particles are collected on charged electrodes. After passing through ESP, clean flue gases with dust particle concentration also known as SPM level less than 100 mg/Nm3 through a chimney of prescribed height. The dust is collected from the bottom of the ESP.
High pressure superheated steam from boiler will pass through a steam turbine will be used for distillery.
While passing through the turbines ( Turbine : 6 MW) , the high pressure and temperature steam will rotate the turbine rotor and an electric alternator mounted on the same shaft. Electric power will be generated by the alternator. This electric power generated will be consumed in house i.e. for running the distillery and utilities like boilers auxiliaries etc.
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Steam turbine
Coal handling system
Ash handling system
Air Cooled Condenser
Power plant stack
Single Chimney
Fuel system
Cooling Tower
Pumps
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Cooled Condenser :
Use of Air Cooled Condenser to be used to reduce water consumption.
All the Conveyors will be covered with GI sheets to prevent the fugitive dust emission into the atmosphere.
DG set :
1500 KVA – 2 Nos.
will be installed for emergency power Back-up during power failure.
Stack Height (above roof level) : As per CPCB/SPCB norms
Pollution Control Equipment Measures : Adequate stack height/ Acoustic
will be installed for emergency power Back-up during power failure:
Water Treatment Plant
Oxidisation Chamber, Pressure Sand Filter / IRF, R.O. Plant,
Tube Settler
Pumps Valves, Custom Pipeline Work.
Total water requirement for the above project will be
1792 m3/day (Net fresh water after recycle ) will be sourced from Groundwater.
Water requirement for first run would be 5119 m3/ day.
WATER INPUT
Process water in Fermentation : 1608 KLD
Water in Molasses :183 KLD
DM water for RS Dilution : 360 KLD
DM water for Boiler Feed : 1438 KLD
Soft water for Vacuum Pump & Others : 200 KLD
Soft Water Makeup for Cooling Tower 1300 KLD
Miscellaneous Washings(Provisional) : 20 KLD
Other Domestic usage (Provisional) : 10 KLD
________________________________________________________
TOTAL WATER REQUIREMENT : 5119 KLD
TOTAL WATER OUTPUT
Steam Condensate : 1250 KLD
Water in Spent Wash :1649 KLD
Spent Lees (Rectifier) : 360 KLD
Spent Lees (Pre-Rectifier) : 300 KLD
CT Evaporation & Drift Losses : 1300 KLD
Domestic Consumption 10 KLD
Boiler Drift & Blow down : 40 KLD
Vacuum Pump Sealing Water : 200 KLD
Miscellaneous Washings (Provisional) 10 KLD
________________________________________________________
TOTAL WATER OUTPUT : 5119 KLD
************************************
Effluent Treatment Plant :
The plant washing of will be fed to clarifier.
The overflow from clarifier & the NF Reject will be taken to the collection tank for proper mixing. Effluent from the collection tank will be pumped to aeration.
The stream from clarifier will be feed to in Anaerobic Treatment followed by separator the sludge is separated and will be sent to equalization tank.
Waste water generated or distillery effluent stream is known as spent wash.
It is a dark brown highly organic effluent and is approximately 10-12 times by volume of
the product alcohol. It is one of the most complex, troublesome and strongest
organic industrial effluents, having extremely high COD and BOD values.
Because of the high concentration of organic load, distillery spent wash is a potential source of
renewable energy. Liquid effluents that come from a grass roots distillery are :
#The spent wash from analyzer column bottom ;
#The effluent from water treatment plant – water softening plant and DM plant.
# Cooling water purge from cooling towers.
#Boiler blow down
# Spent lees from exhaust column bottom, spent lees from re-rectification
column of ENA plant and spent lees from vaporizer column bottom in the
dehydration (absolute alcohol) plant.
# Floor washings and washings from equipment.
The spent wash from analyzer column bottom is collected in clarifier for removal of
suspended particles and then treated anaerobically to produce value addition
products like methane & Bio-compost and to achieve zero discharge.
*************************************
Other Equipments:
Material Handling Equipment : Conveyor, Hydraulic Equipment/Cranes,
DG Set, Air Compressor. DC/VFD Drive, Gear Box, Insulation, Valves, Pipes & Tubes, Cables, Automatic Weighing Machines for Bulk & Liquid Materials. Straight Line Steam Tunnel, Pneumatic Piston Filler, Pressure Filler,Storage Tank, Cooling Tower/ Plant, Air Conditioning Plant, Complete Laboratory Equipments etc
Fire Fighting System shall be as per the TAC Norms and cover all areas where alcohol is produced, handled and stored.
Provision of Foam System for Fire Fighting to control fire from the alcohol storage tank.
Green Belt Development plan in 33 % area and a scheme for Rainwater Harvesting have to be put in place.
Scope Of Entire Civil & Construction Work:
Construction of Office Building, Factory Shed- Boiler House, Substation-Control Panel- Electrical Work, Plumbing Work, Structural Steel fabrication and Erection Work, Fabrication Storage Tank, Vessels etc. etc.
Companies/ General Industries/ Contractors/ Sub Contractors/ Manufacturers of Boiler, Material Handling Equipment , Water Treatment Plant, Effluent Treatment Plant, Air Pollution Control Equipments, Cooling Tower, Blowers, Cranes, Hydraulic Equipments, Water line Valve, Pump, Pipeline etc. related to Distillery Plant may Contact for Specified Enquiry at :
DCM Shriram Ltd.
1st Floor, Kanchenjunga Building
18, Barakhamba Road, New Delhi 110001, Delhi, India.
------------------------------------------------
Tel : +91-11-23316801−08
Fax : +91-11-23318072
Email : resp...@dcmshriram.com
Website : www.dcmshriram.com
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