Experimental Study on Coal Multi-generation in Dual Fluidized Beds

来源 :Journal of Thermal Science | 被引量 : 0次 | 上传用户:flash021
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An atmospheric test system of dual fluidized beds for coal multi-generation was built.One bubbling fluidized bedis for gasification and a circulating fluidized bed for combustion.The two beds are combined with two valves:one valve to send high temperature ash from combustion bed to the gasification bed and another valve to sendchar and ash from gasification bed to combustion bed.Experiments on Shenhua coal multi-generation were madeat temperatures from 1112 K to 1191 K in the dual fluidized beds.The temperatures of the combustor are stableand the char combustion efficiency is about 98%.Increasing air/coal ratio to the fluidized bed leads to theincrease of temperature and gasification efficiency.The maximum gasification efficiency is 36.7% and thecalorific value of fuel gas is 10.7 MJ/Nm3.The tar yield in this work is 1.5%,much lower than that of pyrolysis.Carbon conversion efficiency to fuel gas and flue gas is about 90%. An atmospheric test system of dual fluidized beds for coal multi-generation was built. One bubbling fluidized bed for gasification and a circulating fluidized bed for combustion. Two of the two beds are combined with two valves: one valve to send high temperature ash from combustion bed to the gasification bed and another valve to sendchar and ash from gasification bed to combustion bed.Experiments on Shenhua coal multi-generation were madeat temperatures from 1112 K to 1191 K in the dual fluidized beds.The temperatures of the combustor are stable and the char combustion efficiency is about 98%. Increasing air / coal ratio to the fluidized bed leads to the increase of temperature and gasification efficiency. The maximum gasification efficiency is 36.7% and the calorific value of fuel gas is 10.7 MJ / Nm3. The tar yield in this work is 1.5 %, much lower than that of pyrolysis. Carbon conversion efficiency to fuel gas and flue gas is about 90%.
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