Update : 'Chintamani Agrotech Plans For Sugar, Distillery & Co-Gen Power Plant'...
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RELEASED : ISSUE MAY 04 /14
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Chintamani Agrotech Plans For
Sugar, Distillery & Co-Gen Power Plant
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Update : Ref Our Earlier Report
14.06.2011, 12.09.2012, 07.05.2013 & 19.11.2013
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Chintamani Agrotech ( India) Limited plans for a Sugar Plant having Capacity of 3,500 TCD, Molasses Based Distillery having Capacity of 45 KLD along with a Cogeneration Power Plant of 30 MW at Bijora Village in Yavatmal District, Maharashtra..
Capacity:
Sugar Plant : 3,500 TCD
Distillery : 45 KLD
Co-Gen Power Plant : 30 MW
Location :
Bijora Village, Yavatmal District
Maharashtra
As on May 06, 2014: The Project is to start by May 2014.
Total site area is 60 Acres.
An area of about 33% of the total project area will be developed with green belt.
IMPORTANT: As per the discussion we had on 30.04.2014 with
Chintamani Agrotech ( India) Limited the Project Work is to commence by May 2014.
The company has already received Environmental clearances for
3,500 TCD Sugar Plant & 30 MW Power Plant.
The Project has been delayed, because the company was waiting for financial closure.
Cogeneration Power Plant:
30.00 MW installed capacity
18.34 MW (Avg. exportable power, Season- 160 days)
26.23 MW (Avg. exportable power, Off Season- 170
days)
Sugar & Power Plant is scheduled to be completed First.
The Distillery will be set up after the commissioning of Sugar & Power Plant .
Entire Project is scheduled to be completed by March,2016.
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The Main Scope of Supply includes:
1. Boiler : 150 TPH - 1 No.
Fuel : Bagasse (Main Fuel -During Cane crushing season)/
Coal (Auxiliary fuel -During off season)
2. Boiler : 20 TPH - 1 No.
(Exact Capacity/Spec. yet to be freezed)
for Distillery
Heat Exchangers, Air Pre-heater/Economiser)
Wet Scrubber for arresting fly ash
Air Pollution Control Equipment :
The sources of emissions from the proposed expansion of sugar & cogen plant
shall be boilers of 150 TPH (1 No.) based on bagasse & coal.
The sources of emissions from the distillery shall be incineration boilers of
20 TPH (1 No.) due to burning of spent wash slops along
with coal.
Adequate air pollution control equipment in the form of Electro static
Precipitator shall be provided for the proposed boilers of
150 TPH capacity (01 Nos.).
Adequate air pollution control equipment in the form of cyclone dust
collectors shall be provided for the proposed incineration boilers.
The air pollution control equipment proposed for all the boilers shall
ensure that the air emissions shall confirm to CPCB standards.
Apart from the boilers, standby DG sets shall be the stationary sources.
However, the usage of the same shall be for very limited periods. DG sets shall be provided with stacks of adequate height & noise control measures.
Steam Turbine : 30 MW
Type : Double extraction - cum condensing
Coal handling system
Ash handling system
Ash handling system collecting ash from furnace, Combustion chamber ,Economiser, air heater and wet scrubber shall be transported by
Belt Conveyors to a Silo to be provided.
Turbo Alternator :
Air Cooled Condenser
Power plant stack
Single Chimney
Fuel system
Manufacturing Process : Sugar Plant
The process of manufacturing process:
1. Extraction of juice (Crushing)
2. Clarification of juice
3. Concentration of juice (juice to syrup) by evaporation
4. Boiling of Syrup to grain (crystallization)
5. Separation of crystals from mother liquor (Centrifuging)
Cane receiving
Sugarcane Weighment
Sugarcane Unloading: The cart cane will be manually unloaded directly to the cane carrier.
The cane from the trucks and tractor- trailers will be unloaded with the help of cane un-loader crane. The cane will be unloaded on to the feeder table.
Sugarcane Conveying:
The cane from the feeder table will be then dumped to the main cane carrier, which conveys the cane to the cane preparatory devices.
Electronic devices, depending on the cane-crushing
rate control the speed of the cane carrier, and level in the cane carrier etc.
Sugarcane preparation:
The sugar cane will be passed through the cane preparatory devices called leveller, cutter and fibriser where in the cane is cut into small pieces to expose the juice cells for extraction. The preparatory index is about 85-90 %.
Milling:
The prepared cane will then be passing through the milling tandem having
4 mills of three rollers and necessary feeding device.
The mills will be running at about 4.5 to 6.0 RPM driven through hydraulic motors or DC variable speed drives.
The mills loaded hydraulically extract juice from the cane and is subjected for the extraction of juice aided by maceration water and compound imbibition.
The cane will be conveyed between mills with the help of rake type mechanical Conveyors.
Screens then will filter the extracted juice and filtered juice is pumped for further processing.
The fibrous residue after juice extraction known as bagasse will be withdrawn from the last mill and conveyed through drag type steel conveyors to boiler for steam generation. Surplus bagasse will be withdrawn from the conveyor and stored for reuse when necessary.
The bagasse conveyor also has return conveyor to feed the stored bagasse.
DISTILLERY–Alcohol Manufacturing Process
1. Dilution - Preparation of molasses for fermentation
2. Fermentation - Production of alcohol from fermentable
sugars in molasses solution
3. Distillation - Product Recover
All the Conveyors will be covered with GI sheets to prevent the fugitive dust emission into the atmosphere.
Cooling Tower
Storage Tanks
within the distillery premises.
DG set :
One Additial Dg Set will be installed for stand by arrangement..
Silencer (Acoustic enclosures) to be provided to D.G.)
Clarifier :
Vacuum Filter
Injection pumps
Sugar Receiving Gross Hopper
Sugar Belt Conveyor
Fluidised Bed Sugar Dryer.
Bottling Plant
Dryer
Multiple Effect Evaporators
Centrifugal Machines
CO2 Recovery Plant (In future)
Water storage tanks
Piping works
Weigh bridge
Air compressor
Water Treatment Plant, Effluent Treatment Plant,
Oxidisation Chamber,Filter, R.O. Plant.
Pumps Valves, Custom Pipeline Work
---------------------------------------------
The water consumption in the Sugar Plant including Power Generation will be 1250 m3/day.
Total water requirement for Distillery Plant is 540 m3 /day,
Effluent Treatment System and Scheme
Industrial wastewater system from Cogeneration unit
shall be separated into two systems.
1.Plant Drain System
2. Neutralization and Chemical Drain system
The plant drain system is collecting / shall collect and treat the wastewater from the floors, area wash downs, drainage from the turbine and boiler areas as well as equipment drains. Drains, which potentially could contain oil and grease, are / shall be routed to an oil/water separating system. The system shall divert oil or grease removed to a separate collection drum. The waste oil and grease collected shall be disposed of as via and approved waste oil scavenger service for recycling or disposal.
The neutralization and chemical drain system is collecting / shall collect & neutralize
regeneration waste from the boiler feed water blow down, if found necessary. It shall also collect and treat as it is and caustic waste from the de-mineralized water production plant and bulk chemical storage area drains, chemical feed area drains, along with wash down water collected from these areas.
The neutralization tank is / shall be sized from one and one half times the nominal volume of the demineralised regeneration waste of one demineralised train. The neutralization basin is / shall be internally coated with the computable with the acid and caustic waste.
A neutralization and chemical drain system is / shall be operated on automatic batch wise basis. After the neutralization tank reaches specified level, wastewater shall be neutralized by an automatic pH control system.
The wastewater generated from the Distillery plant will be segregated as process effluent and non process effluent to adopt separate treatment schemes.
Spent wash will be generated as process wastewater from the distillation column. The other wastewater from the plant include, cooling tower blow down, water treatment plant regeneration, floor washings and domestic wastewater.
Other Equipment
Material Handling Equipment : Conveyor, Hydraulic Equipment
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, Hoses,Cables
Ventilation & Exhaust System
Complete Laboratory Equipments
Fire fighting System as per TAC norms,
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 :
Chintamani Agrotech (India) Limited
101, East High Court Road, New Ramdaspet
Nagpur - 440010, Maharashtra, India
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Tel : + 91-712-2551306/2425266
Email : chintaman...@gmail.com
Registered Office:
Chintamani Agrotech ( India) Limited
A-155, Mittal Tower
Nariman Point,Mumbai – 400021, Maharashtra, India
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Tel : + 91-22-40824600
Fax : + 91-22-40824666
Email : chintaman...@gmail.com
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