L H Sugar Plans To Set Up 60 KLPD Distillery with Captive Power
Industrial Directory Of India
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L H Sugar Plans To Set Up
60 KLPD Distillery with Captive Power
L H Sugar Factories Limited plans to set up a 60 KLPD Molasses based Distillery along with 2.0 MW Co-Generation Power Plant (Coal/Rice Husk/ Bagasse ) at Jangraulipul Village, Tehsil : Pilibhit in Pilibhit District, Uttar Pradesh.
Capacity :
Distillery : 60 KLPD
Captive Power Plant : 2.0 MW
( Fuel : Coal/Rice Husk/ Bagasse)
Bottling Plant
Total Working Days in a year : 270 days
Location : Jangraulipul Village, Tehsil : Pilibhit
Pilibhit District, Uttar Pradesh
As on January 23, 2014 : The Project is under Planning Stage.
The unit would come up in the same premises of its its existing
10000 TCD Capacity Sugar Mill that has 29.6 Acres of Land .
Out of this about 33% (9.76 Acre) of the area will be developed as Green Belt.
IMPORTANT: As per the the discussion we had
on 27.12.2013 with L H Sugar Factories Limited
the Project is under Panning Stage.
The company is now waiting for Environmental clearances .
The Project Work is likely start by February/March,2014.
The Project is Scheduled to be Completed in
12-15 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 : *20 TPH
Fuel(as avialable) : Coal/Rice Husk/Bagasse)
Fuel Consumption : Coal : 96 MT/Day/
Rice Husk : 124 MT/Day/
Bagasse : 208 MT/Day
Stack Height : 45 M
Heat Exchanger, Air Pre-Heater/ Economiser
===============================
Steam Requirement (*Break Up):
Multi-Pressure
Distillation : 8.7 TPH
Multi Effect Evaporation : 7.8 TPH
-------------------------------------------------------------
Total : 16.5 TPH
Boiler with 20 TPH capacity is proposed to be installed.
===============================
Raw Materials :
Molasses : 280-285 Ton/Day
- Sulphuric Acid
: 90 Kg/day
- Sodium Hydroxide (Caustic) : 600 Kg/day
NH2-CO- NH2 (Urea;46 % N2) : 144 Kg/day
Air Pollution Control Equipment :
Electrostatic Precipitators/ Bag Filter
To control the particulate emissions from Coal Fired boiler will be controlled by ESP and emissions will be dispersed through Stack Height of 45 Meters.
Steam generated from the boiler will be utilized in the generation of
2.0 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 Electro Static Precipitator where the Dust Particles will be 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 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 1.6 MW.
The company’s proposal is to install 2.0 MW Co – Generation Power Plant.
Steam generated from the boilers of will be utilized in the generation of 2.0 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 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 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
Coal handling system
Ash handling system
Air Cooled Condenser
Power plant stack
Single Chimney
Fuel system
Cooling Tower
Pumps
*************************************
Details of Material Handling for Distillery:
Bucket Elevators, Vibrating Screen,
Hammer Mills, Screw Conveyor
GRAIN STORAGE : Pre-Cleaning and to store in Storage Silos.
GRAIN STORAGE : The grain has to be lifted in Bucket Elevators,
screened followed by removal of stones and iron matter.
Cleaned Grains are then milled using dry milling process in Hammer Mills.
The flour is fed through the Bucket Elevators and conveyed to the Batch Tipping Machine through a Screw Conveyor.
=======================
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 :
750 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
597m3/day (Net fresh water after recycle ) will be sourced from Ground Water & Recycled water.
Water requirement for first run would be 2076 m3/ day.
WATER INPUT FOR Molasses Based Operation
PROCESS WATER IN LIQN & FERMENTATION : 522 KLD
DM WATER IN DISTILLATION
FOR RS DILUTION : 575 KLD
SOFT WATER FOR CT MAKEUP : 276 KLD
DM WATER AS BOILER FEED : 480 KLD
SOFT WATER FOR ANALYSER FLASH TANK : 117 KLD
WATER IN MOLASSES : 56 KLD
DOMESTIC CONSUMPTION : 10 KLD
SOFT WATER FOR PUMP SEALING & VACCUM PUMP : 30 KLD
MISS, WASHING : 10 KLD
________________________________________________________
TOTAL WATER REQUIREMENT (A) : 2076 KLD
TOTAL WATER OUTPUT
STEAM CONDENSATE : 364 KLD
WATER In SPENT WASH : 670 KLD :
SPENT LEES RECTIFIER :575 KLD
SPENT LESS PRE-RECTIFIER : 76 KLD
CT EVAPORATION & DRIFT LOSSES : 276 KLD
DOMESTIC CONSUMPTION : 10 KLD
BOILER DRIFT AND BLOWDOWN LOSSES : 65 KLD
VACUUM PUMP & SEALING : 30 KLD
MISS. WASHING : 10 KLD
_______________________________________________________
TOTAL (B) : 2076 KLD
RECYCLING & UTILIZATION STREAM
LEES RECYCLE FOR RS DILUTION : 495 KLD
STEAM CONDENSATE RECYCLE FROM BOILER : 364 KLD :
SPENT LEES (RECT) - COOLING TOWER MAKEUP : 80 KLD
SOFT WATER FOR VACUUM PUMP & OTHERS : 30 KLD
PROCESS CONDENSATE TO PROCESS : 510 KLD
________________________________________________________
Total Recycling of water per day (C) : 1479 KLD
TOTAL FRESH WATER INPUT (A- C) : 597 KLD
* Water requirement for first run would be 2076 m3/ day.
Total Fresh Water Requirement : 597 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 :
L H Sugar Factories Limited
Civil Lines
Pilibhit - 262001
Uttar Pradesh, India
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Tel : + 91-5882-256053 /255867
Fax : + 91-5882-255518
Email : lhs...@rediffmail.com / ma...@lhsugar.com
Website : www.lhsugar.com
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