100kw, 200kw, 300kw, 1mw Coconut Shell Power Plant

Products profit at 1mw
This project main production is electricity and can also produce charbiomass. The annual operating time is 8000 hours, It consumes about 12000-15000 tons (particles) of raw materials each year.
and the long-term continuous operation power is 85-90%% of the basic power.Each plant Gross generation per yeari 1000kW A 8000 hours / year A 0.9= 7200000 kWh,it will produce 20% -25charcoal that means it can produce around 3000ton charcoal ,can produce wood vinegar 400tons ;the Waste heat from 1mw generator is 1250000-3000000kcal.
1kg raw material will produce the charcoal 0.015-0.02kg,1kg can produce vinegar around 3-5%
1kg woody biomass generate syngas 2.2-2.5mA , 1kg herbal biomass generate syngas 1-1.5mA Heating value of syngas 1100-1300 kcal/mA
Drying layer
on the top of gasifier is the dryer layer and fuel will be delivered to this area from upside.
The moisture inside fuel will evaporate by heat exchange with hot air coming from the below three reaction area and temperature of this layer is 100-200A C.
Output is the dried material and vapor.
Vapor will go outside together with the waste heat from below reaction layers.
The dried material will go down to pyrolysis layer.
Pyrolysis layer
the dried material go down to pyrolysis layer and heat the biomass material for pyrolysis reaction.
Most volatile component will be separated from solid & charcoal left behind when the temperature is 200-500A C
Output of pyrolysis layer is carbon, H2, vapor, CO, CO2, CH4, tar and other material.
Oxidation layer
the remaining charcoal will make strong reaction with air and release lots of heat. At the same time, the incomplete combustion will produce CO and heat, owing to anaerobic combustion and insufficiency O2.
In Oxidation layer, the temperature can reach 800-1000A C, and the reaction equation: C+O2=CO2+a H, a H=408.8KJ
It is combustion reaction in this Oxidation area and release heat energy, that supply energy to reduction area for reduction reaction, material pyrolysis and drying. The hot air (CO & CO2) from Oxidation area will enter into reduction area, and ash will drop into the bottom room.
Reduction layer
there is no O2 in reduction area and the CO2 from Oxidation area will have reduction with charcoal and vapor to produce CO and H2. The temperature will drop down to 600-800A C, owing to the reduction is endothermic reaction. The main output of reduction layer is CO, CO2 and H2.
Gasification always come with material drying and pyrolysis. In actual operation, there is no clear border during the described four area, that is interpenetrating and interlocking, so the main gas output is CO, CO2, H2, CH4, tar, small amount alkanes, vapor and little dust.