Baramati Agro Plans For Expansion Of Sugar,Co-Gen Power & New Distillery
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RELEASED : ISSUE DECEMBER 08 /13
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Baramati Agro Plans For Expansion
Of Sugar,Co-Gen Power & New Distillery
Baramati Agro Limited plans for expansion of its Sugar Plant from 4500 TCD to 7000 TCD, Cogeneration Power Plant from 14.75 MW to 30 MW and to set up a New Molasses Based Distillery of 60 KLD at Rai Kankavatinagar Village, Tehsil: Kannad in Aurangabad District, Maharashtra..
Capacity:
Expansion:
Sugar Plant : 4500 TCD to 7000 TCD
Co-Gen Power Plant : from 14.75 MW to 30 MW
New Plant:
Distillery : 60 KLD
Distribution of Power:
Season / Off Season
Power to Office/colony 0.20 0.20
Power Export 19.57 12.30
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30.00 MW 15.25 MW
Location :
Rai Kankavatinagar Village, Tehsil: Kannad
Aurangabad District, Maharashtra.
As on December 10, 2013: The Project is in planning stage.
Proposed expansion of the sugar Cane crushing capacity from 4500 TCD to 70000 TCD, expansion of Co-generation of power from 14.75 MW to 30 MW & New Molasses based Distillery of 60 KLD shall be located within the vacant area of the existing premises.
IMPORTANT: As per the discussion we had on 03.12.2013 with Baramati Agro Limited the project is under planning stage.
The company is waiting for Environmental clearances.
The Project is Scheduled to be Completed in
Two Years from the date of commencement of the project.
So, this is the RIGHT TIME to contact and Follow Up Contractor at following address to obtain the detailed Enquiry of each product in time and to submit your quotation subsequently.
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The Main Scope of Supply includes:
Boiler : 110 TPH - 1 No.
Fuel : Bagasse
Stack : 75 Meter
Wet Scrubber for arresting fly ash
Air Pollution Control Equipment :
The sources of emissions from the proposed expansion of sugar & cogeneration plant
shall be boiler of 110 TPH (01 No.) based on bagasse .
In the co-gen power plant high efficiency Electro Static Precipitators (ESP) will be installed to bring down the particulate matter in the exhaust gas and will be let out into atmosphere through 75 Meter height of RCC Chimney
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.
The proposed Co‐generation plants will generate gross power output of 30 MWH during cane crushing season and off‐season at the generator terminal. After meeting the in house requirement for Sugar and Cogeneration power plants (including losses), the excess power will be export to the Grid.
Steam turbine : 17 MW – 1 No.
During Season, the proposed Co‐generation Boilers supplying steam to a common header from where steam will be supplied through the connecting piping to the Turbogenerator of installed capacity of 17 MW for the first 160 days & 20 MW for the remaining days in season.
The turbogenerators will be a Bleed cum Back Pressure and double extraction cum condensing type.
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
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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:
Sugarcane from the fields are weighed and fed in cane carrier by means of cane unloaders. The cane is passed through kicker, leveler and Fibrizer. The Fibrizer improves the extraction of the mills by breaking the rigid ness of the cane and so facilitating its disintegration and extraction of its juice.
The fibres are then crushed in mill house, consisting of the 4 mills. During crushing, juices present in the cane cells are extracted by the mills. The juice obtained from milling is sent for process, fibre that comes out from 4thmill is termed as bagasse and it is used as fuel in boilers.
Clarification:
The extracted juice from mills is called as raw juice and it is heated to 70 – 75 Deg. C. in juice heaters and treated simultaneously with the milk of lime and sulphur dioxide gas in order to separate the impurities. The sulphited juice is again heated to 102 Deg. C through juice heaters and allowed to settle in the clarifier. The purified juice, which comes out from clarifier, is called as clear juice and is sent to evaporator for concentration. The settled impurities are called mud. The mud contains small amount of juice, which is separated in vacuum filters.
Crystallisation:
The sulphited syrup is concentrated further in the vessels called pans. During the above process, sugar crystals are developed by means of exhaustion. The formed crystals are then cooled in crystallisers. The crystals are surrounded by thin film liquid called as mother liquor. The crystal along with the mother liquor (Molasses) is called as massecuite.
Curing:
The above massecuites are centrifuged in centrifugals, where crystals are separated from the mother liquor. Separated mother liquor of massecuites is again used for boiling and maximum exhausted mother liquor is called as Final Molasses, which is stored in the steel tanks and sent to distillery for manufacture of Ethyl alcohol. The separated sugar crystals are dried in hopper, sieved in graders and bagged.
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Conveyors.
Cush - Cush conveyor :
Double scroll type
The bagasse conveyor also has return conveyor to feed the stored bagasse
Screens : Rotary screen .
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.
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 :
(For DistillerY)
Cooling System : For Power Plant
Mud Belt Conveyor : 1 No.
Gross Hopper Conveyor : 1 No
Fluidized Bed Dryer
Vibratory Screen
Cane Weighbridges
Mills
JUICE PUMPS
Mill House Crane
Air Compressor
Plate Heat Exchangers :
Wash Pre-heating PHE(SS316) .
Recycle Wash Cooler (Recycle) PHE
Spent Wash Cooler PHE (SS316)
Propagation Vessel :
(For DistillerY)
PROCESS PUMPS
(For DistillerY)
Molasses feed pump .
Fermenter Cooling Pump
Fermenter Discharge Pump
Wash Transfer Pump
Sludge Pump
Recycle Pump
Propagation II Cooling Pump
Defoaming oil dosing Pump
Fire fighting system for complete complex:
Fire water pump motor driven
Fire water pump diesel set driven
Jacky pump
Storage Tanks:
For various purposes in Sugar, Power & Distillery Plants.
DG Set:
One Additial DG Set of will be installed for stand by arrangement..
Silencer (Acoustic enclosures) to be provided to D.G.)
Clarifier :
Vacuum Filter
Injection pumps
Water Treatment Plant, Effluent Treatment Plant,
Oxidisation Chamber,Filter, DM. Plant, Softener.
Pumps Valves, Custom Pipeline Work
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After the expansion, water
consumption shall be 2590 m3/day.
The water required for the proposed expansion project will be
met from the Ambadi Reservoir.
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Effluent Treatment System and Scheme
The effluent generated from boiler blow down, cooling tower blow down and WTP wash shall be treated in ETP and treated water will be partly used for ash quenching and gardening.
Sewage and other effluents from sugar and Co-Gen plant will be treated and recycled and discharged on 33 % of open land left for green belt . As treated water has all the parameters within CPCB limit no danger to ground water.
Effluent treatment Plant having size to treat 712 m3 of waste for waste water from sugar cane and power plant will be established.
Sewage to the tune of 2.4 M3/Day will be treated in septic tank followed by soak pit.
Ash 21 ton per day from power plant is sold to brick manufacturer.
180 ton of press mud per day will be used for composting. 180 tons /day of molasses generated is used for manufacturing alcohol.
PROCESS DESCRIPTION
The proposed waste water treatment plant shall consist of following treatment units.
PRIMARY TREATMENT
· Screen
· Oil & Grease trap
· pH adjustment
· Equalization Tank
SECONDARY TREATMENT
· Anaerobic reactor
· Aeration Tank
· Secondary Clarifier
· Sludge Drying Beds
Screen Chamber:
Screen chamber constructed in RCC shall be provided with SS 304 fabricated bar screen for removal of free and floating material. The screen shall be inclined at 45 Deg with horizontal.
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 :
Baramati Agro LimitedPimpali, Baramati
Pune - 413102, Maharashtra, India.
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Tel : + 91-2112-221001/ 2/ 4/5
Fax : + 91-2112-221003
Email : ma...@baramatiagro.com
Website : www.baramatiagro.com
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