Globus Spirits Plans to Set Up Another 120 KLPD Distillery with Captive Power
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RELEASED : ISSUE NOVEMBER 03/13
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Globus Spirits Plans to Set Up Another
120 KLPD Distillery with Captive Power
Globus Spirits Limited plans to set up another 120 KLPD Grain Based Distillery along with
3.5 MW Co-Generation Power Plant (Coal/Rice Husk Based ) at Dhudhua Village, Jandaha Tehsil in Vaishali District, Bihar.
It will produce ENA (Extra Neutral Alcohol), Rectified Spirit, Indian Made Foreign Liquor (IMFL) & Country Liquor (CL) in the above plant.
Capacity :
Distillery : 120 KLPD
Captive Power Plant : 3.5 MW
( Fuel :
Coal/Rice Husk)
Bottling Plant
By Prouct : CO2 will be generated during fermentation
process which will be collected and sold to authorized vendor.
Location : Dhudhua Village, Jandaha Tehsil
Vaishali District, Bihar
As on November 06, 2013 : The Project is under Planning Stage.
The unit would come up on about 25 Acre of Land .
About 33% (8.25 Acre) of the area will be developed as Green Belt.
IMPORTANT: As per the the discussion we had
on 24.10.2013 with Globus Spirits Limited
the Project is under Panning Stage.
The company is now waiting for Environmental clearances .
The project work is likely to start in April, 2014.
The Project is Scheduled to be Completed
by June, 2015.
=======================================
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 : *35 TPH
Fuel : Coal/Rice Husk
(300 MT/Day)
Stack Height : 45 M
Heat Exchanger, Air Pre-Heater/ Economiser
===============================
Steam Requirement (*Break Up):
Cooking & Liquefaction : 4.30 TPH
Multi-pressure Distillation : 17.00 TPH
Evaporation (Integrated) : 2.70 TPH
DWGS Drier (DDGS) : 9.00 TPH
Boiler Deaeration : 2.00 TPH
-------------------------------------------------------------
Total : 35.00 TPH
===============================
Raw Materials :
- Grains containing 62% w/w Starch : 295 MT/day
- Antifoam Agent : 65 kg/day
- Yeast (Active Dry Yeast/ : 200 kg/day
Distiller’s Yeast
- Sulphuric Acid : As required
- Sodium Hydroxide (Caustic) : 1000 kg/day
For Main Process Plant (35% Strength)
- Liquefying Enzyme : 129 kg/day
- Saccharifying Enzym : 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
3.5 MW Power and wil 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.
High pressure superheated steam from boiler will pass through a Steam Turbine and at the lower pressure will go to the condenser.
The part of the steam will be extracted from the extraction points provided on the turbine, which will be used for distillery.
The condensed steam will return to the steam boiler as condensate and will again be boiled as steam.
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. and surplus power will be exported to the state grid.
Steam turbine
Coal handling system
Ash handling system
Air Cooled Condenser
Power plant stack
Single Chimney
Fuel system
Cooling Tower
=======================
Manufacturing Process:
GRAIN CLEANING, MILLING AND FLOUR HANDLING :
The grain is 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 elevator and conveyed to the Batch Tipping Machine through a Screw Conveyor. The flour addition is metered through the Batch Tipping Machine with load cell arrangement, before transferring the flour to the Slurry Tank through another Screw Conveyor (pre-masher) for slurry preparation process.
SLURRY PREPARATION & LIQUEFACTION :
Grain flour and process water is fed at controlled rate to Initial Liquefaction tank. Mixed slurry is taken to the Initial Liquefaction Tank where additional quantity of water is added as per requirement. Viscosity reduction Enzyme and stabilizing chemicals and a portion of liquefying enzyme are also added at this stage. This slurry is then “cooked” in the Jet Cooker.
The slurry is continuously pumped to a steam jet cooker where high-pressure steam rapidly raises the slurry temperature. The mixture of slurry and steam is then passed through the Retention Vessel. The retention vessel has sufficient capacity to provide the desired retention time at a given flow rate. The cooked mash is discharged to a Flash Tank.
The cooking process, accomplished in the above manner, converts the slurry into a hydrated, sterilized suspension and is therefore susceptible to enzyme attack for liquefaction.
The gelatinized mash from the Flash Tank is liquefied in the Final Liquefaction Tank where liquefying enzyme (alpha-amylase) is added. The liquefied mash is cooled in Mash Cooler and transferred to Saccharification cum fermentation section. This
process initiates the formation of sugar.
The gelatinized mash from the Flash Tank is liquefied in the Final Liquefaction Tank where liquefying enzyme (alpha-amylase) is added. The liquefied mash is cooled in Mash Cooler and transferred to Saccharification cum Fermentation section.
HIFERM-NM SACCHARIFICATION AND INSTANTANEOUS FERMENTATION :
Yeast seed material is prepared in water-cooled Yeast Activation Vessel by inoculating sterilized mash with Active Dry Yeast. Optimum temperature is maintained by cooling water. The contents of the Yeast Activation Vessel are then transferred to Fermenter.
Saccharification & Instantaneous Fermentation:
The Liquefied starch slurry comprising Dextrins is partly taken for Yeast development in Yeast Activation vessel and majorly transferred into the Fermenter. Amyloglucozydase and other nutrient Enzymes are first added to Saccharify the Starch Slurry causing formation of Sugars. Immediately, the Active Yeast is introduced in the system for simultaneous Fermentation. The process of fermentation is to convert the fermentable substrate into alcohol.
The carbon dioxide evolved during the process is vented to atmosphere after recovery of alcohol in a scrubber..
MULTI PRESSURE DISTILLATION :
This process utilizes following columns namely the Analyser, Degassifier, Pre-Rectifier Column, Stripper, Rectifier cum Exhaust, Extractive Distillation (ED) Column, Recovery Column and Simmering Column in ideal heat integration in order to reduce the energy consumption.
The Analyzer, Degassifier & Extractive Distillation Columns are operated under Vacuum whereas the Simmering, the Recovery Columns are operated under Atmospheric condition. The Pre-Rectifier, Rectifier-cum-Exhaust Columns are operated under Pressure.
The energy requirement for Analyser, Degassifier Column is met by Rectifier Column top vapours.
The Distillation Plant shall be designed for use of Grain starch route only.
ALCOHOL (ENA & TA) DAILY RECEIVERS & BULK STORAGE :
The Extra Neutral Alcohol & Technical Alcohol (Impure Spirit) is first taken to Daily receiver storage tanks, which is based on the State Excise laws, storage for three days considering the weekly holidays of two days. Thereafter, the alcohol is transferred to Bulk Storage Tanks after taking the daily receiver Dip. This is transferred using flameproof pumps. Final dispatch of alcohol is metered and again
is carried out using special flameproof pumps.
The Bulk Spirit Storage is proposed to be set up for 30 days.
*************************************
Details of Material Handling for Distillery:
Bucket Elevators, Vibrating Screen,
Hammer Mills, Screw Conveyor – 2 Nos.
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.
The flour addition is metered through the Batch Tipping Machine with load cell arrangement, before transferring the flour to the Slurry Tank through another Screw Conveyor (pre-masher) for slurry preparation process. It is proposed to have
2 x 8 TPH (+ 1 Standby option) as milling paraphernalia for this Distillery.
=======================
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 :
1250 KVA – 1 No
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 for the above project will be
1205 m3/day and will be sourced from Ground Water & Recycled water.
Note :
Water requirement (Grain Based Plant) for first run would be 3917 m3/day, which will be reduced through recycling of 2712 m3/ Day of treated water Condensates.
WATER REQUIREMENT FOR GRAIN BASED OPERATION
PROCESS WATER IN LIQN & FERMENTATION : 726 KLD
DM WATER IN DISTILLATION
FOR RS DILUTION : 1155 KLD
SOFT WATER FOR CT MAKEUP : 856 KLD
DM WATER AS BOILER FEED : 1080 KLD
BLENDING ( BOTTLING) : 30 KLD
BOTTLE WASHINGS : 10 KLD
DOMESTIC CONSUMPTION : 10 KLD
SOFT WATER FOR PUMP SEALING & VACCUM PUMP : 50 KLD
________________________________________________________
TOTAL WATER REQUIREMENT (A) : 3917 KLD
TOTAL WATER OUTPUT
STEAM CONDENSATE : 1031 KLD
SPENT LEES PR : 205 KLD :
SPENT LEES RECTIFIER :1155 KLD
WATER IN THIN SLOPS : 452 KLD
WATER IN WET CAKE : 82 KLD
SOFT WATER FOR VACUUM PUMP & OTHERS : 50 KLD
WATER IN PRODUCT : 30 KLD :
BOTTLE WASHING : 10 KLD
BOILER DRIFT AND BLOWDOWN LOSSES : 36 KLD
CT EVAPORATION & DRIFT LOSSES : 856 KLD
DOMESTIC CONSUMPTION : 10 KLD :
________________________________________________________
TOTAL (B) : 3917 KLD
RECYCLING & UTILIZATION STREAM
LEES RECYCLE FOR RS DILUTION : 924 KLD
STEAM CONDENSATE RECYCLE FROM PROCESS : 1031 KLD :
SPENT LEES (RECT) - COOLING TOWER MAKEUP : 231 KLD
SOFT WATER FOR VACUUM PUMP & OTHERS : 50 KLD
PROCESS CONDENSATE TO PROCESS : 254 KLD
THIN SLOPS RECYCLE : 221 KLD
________________________________________________________
Total Recycling of water per day (C) : 2712 KLD
TOTAL FRESH WATER INPUT (A- C) : 1205 KLD
* Water requirement for first run would be 3917 m3/day
Total Fresh Water Requirement : 1205 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.
In this process the bacteria is responsible for digestion process.
The bacteria take upon organic content of wastewater to metabolize it and
to produce biogas and are collected at the top.
The an-aerobically digested effluent is collected and sent to aeration tank. An aeration system consisting of surface aeration system shall be used to provide oxygen to bacteria. The microorganisms degrade soluble organics aerobically.
The mixed effluent from aeration tanks is then sent to Chlorination.
Chlorine dose will adjusted to maintain the residual chlorine concentration.
The treated waste water will further be subjected to de-chlorination.
The chlorinated waste water will then pump to multi grade filter followed by
Activated Carbon Filter where suspended solids are removed. Finally the treated water shall be stored in sump and shall be further used for Gardening, Ash conditioned and plant washing etc.
The sludge after treatment shall be further used as manure. Minor quantity of Biogas generation from Treatment will be vented to atmosphere.
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 (Approx. 8.25 Acre Acres) 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 :
Globus Spirits Ltd
F-0, Ground Floor,The Mira Corporate Suites
Plot No. 1 & 2, Ishwar Nagar,
Mathura Road, New Delhi 110065, Delhi, India
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Tel : + 91-11-66424600
Fax : + 91-11-66424629
Email : corpo...@globusgroup.in
Website : www.globusspirits.com
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