The invention relates to a process and a device for reclaiming blown gas made from
coal and by
oxygen-enriched
combustion. The flow of the reclaiming process comprises that: gas making furnace residue and
coal ash are sent to the lower part of a
fluidized bed furnace through a screw-type
coal feeder and subjected to heat exchange through an
air preheater, primary air
fluidization at the temperature of approximately 120 DEG C and partial
combustion reaction; uncombusted portions are continuously combusted in secondary air and generate high-temperature
flue gas at the temperature of between 950 and 1,000 DEG C which enters a
cyclone dust collector in a blown gas
combustion furnace;
flue gas subjected to dust collection by the
cyclone dust collector is drained into the blown gas combustion furnace from the top of the
cyclone dust collector; the blown gas is completely combusted under the action of the secondary air;
flue gas reaches the temperature of between 950 and 1,050 DEG C, is drained out from the blown gas combustion furnace and enters a boiler
system; and finally
flue gas at the temperature of between 130 and 150 DEG C is emptied by chimneys. The device of the reclaiming process comprises the
fluidized bed furnace, the blown gas combustion furnace and the cyclone dust collector, wherein a furnace chamber of the
fluidized bed furnace is communicated with the cyclone dust collector in the blown gas combustion furnace through a flue; the lower part of the fluidized
bed furnace is provided with a primary air and fuel inlet, and the lower part and the middle part of the fluidized
bed furnace are provided with a secondary air inlet respectively; the inside of the blown air combustion furnace is provided with the cyclone dust collector; and the upper part of the blown air combustion furnace is provided with a blown gas inlet and the lower part of the blown air combustion furnace is provided with a
flue gas outlet
pipe.