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Air gasification of rice husk in a dual distributor type fluidized bed gasifier

机译:双分配器流化床气化炉中稻壳的空气气化

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In this study, a dual distributor type fluidized bed gasifier was used for the air gasification of rice husk in view of producing fuel gas. The effects of varying fluidization velocity (0.22,0.28 and 0.33 m s~-1) and equivalence ratio (0.25,0.30 and 0.35) on the gasifier performance were discussed. The steady state temperature varied between 665 and 830 deg C. The fluidization velocity of 0.22 m s~-1 and equivalence ratio of 0.25 appeared to be the optimum conditions with respect to the quality of gas. The mole fractions of the combustible components reached their maximum values at these conditions with a typical gas composition of 4 H_2, 5 hydrocarbons (CH_4, C_2H_2, C_2H_4 and C_2H_6), 15 CO_2, 20 CO and 57 N_2. The higher heating value of the gas obtained at these fluidization velocity and equivalence ratio (3.09-5.03 MJ Nm~-3) compared very well with published data from air-blown biomass gasifiers of similar scale of operation. The gas yield and carbon conversion were in the range of 1.30 to 1.98 Nm~3 kg~-1 and 55.0 to 81.0, respectively.
机译:在这项研究中,考虑到产生燃料气体,将双分配器型流化床气化炉用于稻壳的空气气化。讨论了流化速度(0.22、0.28和0.33 m s〜-1)和当量比(0.25、0.30和0.35)对气化炉性能的影响。稳态温度在665至830摄氏度之间变化。相对于气体质量,0.22 m s〜-1的流化速度和0.25的当量比似乎是最佳条件。在这些条件下,典型的气体成分为4 H_2、5种碳氢化合物(CH_4,C_2H_2,C_2H_4和C_2H_6),15 CO_2、20 CO和57 N_2,可燃成分的摩尔分数达到最大值。在这些流化速度和当量比下(3.09-5.03 MJ Nm〜-3)获得的气体的较高的热值与来自类似操作规模的风吹式生物质气化炉的公开数据相比非常好。气体收率和碳转化率分别在1.30至1.98 Nm〜3 kg〜-1和55.0至81.0的范围内。

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