A biomass low-temperature carbon-gas cogeneration device, a biomass low-temperature carbon-gas cogeneration device, and a biomass low-temperature carbon-gas cogeneration method
A technology of biomass charcoal and biomass, which is applied in the direction of biofuel, manufacture of combustible gas, granular/powdered fuel gasification, etc. It can solve the problems of long residence time, burning loss of biochar, short residence time of biochar, etc.
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Embodiment 1
[0037] Embodiment 1: as figure 1 The schematic diagram of a biomass low-temperature carbon-gas cogeneration device is shown in the schematic diagram. The device includes a feeding device 1, a fluidized bed charcoal-gas cogeneration furnace body 2, a biomass charcoal reheating device 3, a gas-solid separation device 4, an adiabatic Combustion device 5, waste heat boiler 6, induced draft fan 7, blower fan 8, gas nozzle 9, biomass charcoal cooling and collection device 10, flue gas fan 11, expansion zone 12, standpipe 13, temperature and speed regulation nozzle 14.
[0038] The fluidized bed charcoal gas cogeneration furnace body 2 (bubbling fluidized bed is adopted in this embodiment) is connected with the feeding device 1, and the bottom is connected with a biomass charcoal cooling and collecting device 10 and a blower 8, and the fluidized bed charcoal gas The middle and upper part of the co-production furnace body 2 are provided with a temperature-regulating and speed-regulati...
Embodiment 2
[0040] Biomass charcoal and steam are produced by using a biomass low-temperature charcoal-steam cogeneration device of the present invention. The selected raw material is corn stalks with a length of about 2-4cm and a water content of <18%. The selected bed material is ceramic balls with a particle size of 0.2-0.7mm.
[0041] Put the above-mentioned raw materials and bed materials into the bubbling fluidized bed charcoal-gas cogeneration furnace through the feeding device, blow air into the furnace through the blower, adjust the steam flow from the waste heat boiler, and control the gas flow rate in the furnace to 2.5m / s, The reaction temperature in the furnace was controlled at 500°C.
[0042] The raw material undergoes pyrolysis and gasification reaction in the furnace, and the generated biomass gas carries the biomass charcoal into the biochar reheating device for gas-solid separation, and the straw char is heated again in the biochar reheating device for about 3 minutes t...
Embodiment 3
[0044] Biomass charcoal and steam are produced by adopting a kind of biomass low-temperature carbon-steam cogeneration device of the present invention, the selected raw material is bamboo chips, the length is about 0-5cm, the moisture is <25%, the selected bed material is ceramic balls, the particle size 0.2-1mm.
[0045] Put the above-mentioned raw materials and bed materials into the bubbling fluidized bed charcoal-gas cogeneration furnace through the feeding device, blow air into the furnace through the blower, adjust the flue gas flow rate from the waste heat boiler, and control the gas flow rate in the furnace to 3m / s. Control the reaction temperature in the furnace to 550°C.
[0046] The raw material undergoes pyrolysis gasification reaction in the furnace, and the generated biomass gas carries the biomass charcoal into the biochar reheating device for gas-solid separation. The bamboo charcoal is reheated in the reheating device for about 4 minutes to improve the quality...
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