Co-Operative Company Plans For Expansion of Distillery with New Co-Gen Power Plant..
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Co-Operative Company Plans Expansion
Distillery with New Co-GenPower Plant
Co-Operative Company Ltd. plans for Expansion & Modernization of its Molasses based Distillery Capacity from 10 KLPD to 100 KLPD and to set up a NEW 3.0 MW Co-Generation Power Plant (Bagasse /Rice Husk ) at Tapri Village in Saharanpur District, Uttar Pradesh.
Distillery : 10 KLPD to 100 KLPD
New :
Captive Power Plant : 3.0 MW
( Fuel : Bagasse/Rice Husk )
Project Cost : Rs. 120.50 Crores
Location : Tapri Village, Saharanpur District, Uttar Pradesh.
As on June 18, 2015 : The Project is under Planning Stage.
The unit would come up in the same premises of its its existing
9.84 Acres of Land .
Out of this about 33% (3.24 Acre) of the area will be developed as Green Belt.
IMPORTANT: As per the the discussion we had
on 15.05.2015 with Co-Operative Company Ltd.
the Project is under Panning Stage.
The company is now waiting for Environmental clearances in place .
The Project is Scheduled to be Completed in
15-18 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 : *25 TPH
Fuel(as avialable) : Bagasse/Rice Husk)
Stack Height
: 60 M
Heat Exchanger, Air Pre-Heater/ Economiser
===============================
Steam Requirement (*Break Up):
Multi-Pressure
Distillation : 11.67 TPH
Multi Effect Evaporation : 6.67 TPH
Boiler Deaeration : 3.0 TPH
-------------------------------------------------------------
Total : 21.35 TPH
Boiler with 25 TPH capacity is proposed to be installed.
=============================================
Note : Existing Boiler of 4 TPH capacity with scrubber as APCE will be dismantled and a new Boiler with 25 TPH capacity is proposed to be installed.
======================================================
Raw Materials :
Molasses : 410 TPD Ton/Day
- Sulphuric Acid
- Sodium Hydroxide (Caustic)
NH2-CO- NH2 (Urea;46 % N2)
Air Pollution Control Equipment :
Bag Filter
To control the particulate emissions from Coal Fired boiler will be controlled by Bag Filter and emissions will be dispersed through Stack Height of 60 Meters.
CO2 generated during the fermentation process is collected by utilizing CO2 Scrubbers and sold to authorized vendor.
Steam generated from the boiler will be utilized in the generation of
3.0 MW Power and will also be used for Boiler feed water heating and Distillery.
Flue gases after super heating the steam will pass through Economizer where they will Pre-Heat the boiler Feed water before it enters the boiler drum. After Economizer, flue will pass through Air Pre-Heaters where they will heat the air which will be fed to the boiler furnace for burning the fuel.
After Air Pre Heaters flue gases will pass through an Bag Filter where the Dust Particles will be collected on charged electrodes. After passing through Bag Filter, 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 will be collected from the bottom
of the ESP.
Power Requirement and Source:
The total estimated consumed load for the Project is estimated to be 2.4 MW.
The company’s proposal is to install 3.0 MW Co – Generation Power Plant.
Steam generated from the boilers of will be utilized in the generation of 3.0 MW Power 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 Bag Filters where the dust particles are collected on charged electrodes. After passing through Bag Filters, 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 .
High pressure superheated steam from boiler will pass through a steam turbine will be used for distillery.
While passing through the turbine, 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.
************************************************************************
Steam turbine
Ash handling system
Air Cooled Condenser
Power plant stack
Single Chimney
Fuel system
Cooling Tower
Pumps
*************************************
Cooled Condenser :
Use of Air Cooled Condenser to be used to reduce water consumption.
DG set :
750 KVA – 1 No.
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 after expansion will be
851 m3/day (Net fresh water after recycle ) will be sourced from Ground Water & Recycled water.
Water requirement for first run would be 3070 m3/ day.
WATER INPUT FOR Molasses Based Operation
PROCESS WATER IN LIQN & FERMENTATION : 812 KLD
DM WATER IN DISTILLATION
FOR RS DILUTION : 746 KLD
SOFT WATER FOR CT MAKEUP : 710 KLD
DM WATER AS BOILER FEED : 530 KLD
SOFT WATER FOR ANALYSER FLASH TANK : 130 KLD
WATER IN MOLASSES : 62 KLD
DOMESTIC CONSUMPTION : 10 KLD
SOFT WATER FOR PUMP SEALING & VACCUM PUMP : 60 KLD
MISS, WASHING : 10 KLD
________________________________________________________
TOTAL WATER REQUIREMENT (A) : 3070 KLD
TOTAL WATER OUTPUT
STEAM CONDENSATE : 396 KLD
WATER In SPENT WASH : 893 KLD :
SPENT LEES RECTIFIER :746 KLD
SPENT LESS PRE-RECTIFIER : 245 KLD
CT EVAPORATION & DRIFT LOSSES : 710 KLD
DOMESTIC CONSUMPTION : 10 KLD
BOILER DRIFT AND BLOWDOWN LOSSES : 30 KLD
VACUUM PUMP & SEALING : 30 KLD
MISS. WASHING 10 KLD
_______________________________________________________
TOTAL (B) : 3070 KLD
RECYCLING & UTILIZATION STREAM
LEES RECYCLE FOR RS DILUTION : 650 KLD
STEAM CONDENSATE RECYCLE FROM BOILER : 396 KLD :
SPENT LEES (RECT) - COOLING TOWER MAKEUP : 90 KLD
SOFT WATER FOR VACUUM PUMP & OTHERS : 30 KLD
PROCESS CONDENSATE RECYCLE TO PROCESS : 923 KLD
PRC LEES FOR FLAS TANK 130 KLD
________________________________________________________
Total Recycling of water per day (C) : 2219 KLD
TOTAL FRESH WATER INPUT (A- C) : 851 KLD
* Water requirement for first run would be 3070 m3/ day.
Total Fresh Water Requirement : 851 KLD
************************************
Effluent Treatment Plant :
An ETP of 350 m3/day capacity is proposed to be installed.
The flow diagram is shownThe 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 :
Co-Operative Company Ltd.
( A Group company of Harish Aneja Group )
D10/1, Okhla Industrial Area,
Phase 1, New Delhi 110020
Delhi, India.
-------------------------------------
Tel : +91 8587000051/52/53
Fax : +91 8587000050
Email : in...@lahag.com
Website : www.lahag.com
=======================
Plant :
Co-Operative Company Ltd.
( A Group company of Harish Aneja Group )
Yusufpur Road, Tapri
Saharanpur - 247001, Uttar Pradeh, India
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