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A non-conventional, CO-Generation, Renewable energy
source, a green Project. This process is a major achievement in the
development of renewable energy systems. It is a thermo-chemical process
that converts of renewable energy systems. It is a thermo-chemical process
that converts solid waste, coal to a low heat value (LHV) gaseous fuel
called “Producer Gas”. This producer gas is fuel for many different
applications of shaft power, thermal power or electricity in the equipment.
Receiving GOL backing, utilizes Municipal solid
Waste as fuel, viz – waste Wood, saw dust, furniture
Waste wood, bagasse, rice husk, Coconut Shells,
Thermocol, waste plastic, rubber, tyres, leather, Coal
etc.
Max.Output of a single Unit-05 Mega Watts. & Minimum
Output-500 Kw.
For higher requirements multiple
Units can be commissioned.
PYROLATIC GASIFIER WITH EXTENDED SHAFT
The equipment to be utilized is the new generation Gasifier a modified
version developed recently to obtain clean, rich and consistent supply of
producer Gas soots and smoke formed by cracking of tar with higher
gasification efficiency and low coal consumption rate. Further Volatile
Matter contents of the coal are converted into fix carbon which on
gasification increases the calorific value of gas & reduce fuel conception
and ioncreases the overall efficiency of gasification. The modified design
has been developed by consistent
R & D at Bijendra by incorporating
new modifications to get better viability of gasifiers .
The two in -line ESP’s or electro static precipitators help in the removal
of tar developed in the process of Pyrolysis.
COAL GASIFIER TECHNOLOGY
The Gasifier, which can gasify variety of coals & low grade fuels & produce
Producer Gas. In the thermal application, the Producer Gas is burnt directly
in Kiln, Furnaces, Hot Air Generator and Boiler with the help of specially
design Producer Gas burners with proper mixing of combustion air to replace
any type of existing liquid fuel.
CONVENTIONAL GASIFIER TECHNOLOGY
Gasification technology has proven results of one hundred
percent replacement of liquid fuels, at a net saving of almost 50 percent,
in the existing fuel consumption for industries consuming from 1000
to 20,000 liters per day. (Thermal Output range
10,00,000 to 60,00,000 K.Cal/Hr)
EXTENDED SHAFT
GASIFIER TECHNOLOGY
In the new design the extended shaft is made to transform the feed
coal from hopper into nearly charcoal state and removing most of its
volatile matters towards faster gasification process. This down ward flow of
coke carburizes the upward moving Producer Gas to enrich its calorific
value.. The height of the shaft is optimized by trial & error to avoid over
cooling of PG and keeping the gas below the cracking temperature of Tar.
The height of the coal bed is designed to avoid crushing of coal which leads
to uneven flow of saturated air and gas and causing difficulty in rotation
of the Rotary Grate. New design covers the double off-taking of PG from the
extended shaft for smoother gas off-take and imparting uniform gas flow from
the coal bed void spaces. Reverse flow gas wash out with recalculated
phenolic water is provided for getting no effluent of any kind from the
process. In the thermal application, the Producer Gas is burnt directly in
Kiln, Furnaces, Hot Air Generator and Boiler with the help of specially
design Gas burners for proper mixing of secondary combustion air to provide
ease of combustion control.

Feature &
Advantages:
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The producer gas generated in the Pyro – Gasifier has higher Calorific
Value in the range of 1000-14000 K.Cal/NM3 which is suitable for getting
high flame tempearature in the range of 1200-14000C as required by most of
the thermal processes.
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Tar Content in the gas by pyro-gasification is minimal as the gas
temperature is @ 1500C, thus delivering gas of higher calorific value to
result in higher gasification efficiency and lower coal consumption rate.
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Due to cleaner gas, the occurrence of choking of the burner and duck
pipes is less, which results in increase in productivity and lesser
cleaning interruptions in the process.
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Minor traces of Sox / Nox formation due to low gasification & low flame
temperature.
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There is no effluent output in the process. The washing of gas is done
with hot (70-800 C) re-circulated water which separates out the Tar in
liquid form like FO which can be burnt in the furnace for giving extra
energy to combustion.
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The two in line ESP’s or Electro Static Precipitators help in the removal
of Tar from the gas produced during the process of pyrolysis.
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Extremely Low Particulates and smoke emission due to the complete direct
firing of producer Gas & lesser than Pollution Control board norms.
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Worldwide accepted environment friendly Renewable Energy technology.
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Very early payback period.
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