The invention relates to a pulverized
coal fluidized bed gasifier and an operation method, in particular to a pulverized
coal fluidized bed gasifier capable of improving circulation ratio and an operation method. The invention aims to solve the problems of high specific
coal consumption and low carbon conversion rate caused by the fact that gas in the gasification furnace flows back into a blanking
pipe and the circulating ratio of
fly ash is too low. The material return unit is installed in the material return
pipe, the pressure is reduced and the speed is increased after a
water vapor laval
nozzle is sprayed, and circulating ash at the inlet of the gradually-shrinking inlet section is injected into the second
throat pipe. Mixed working media are violently mixed in the second
throat pipe, and the speed is reduced after energy and
momentum exchange, so that the pressure in the material return pipe is increased, and
airflow in the furnace is prevented from reversely flowing to the
cyclone separator; meanwhile, more
fly ash particles are introduced into the gasification furnace, so that the carbon content of
fly ash is reduced, the amount of ash circulating back to the gasification furnace is increased, and the carbon conversion rate is improved. The method is applied to the fields of production of
chemical synthesis or
fuel oil synthesis feed gas, industrial
fuel gas, civil gas, metallurgical reducing gas,
combined cycle power generation
fuel gas and the like.