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    10 MWth串行流化床生物质化学链燃烧装置设计

    Design of a 10 MWth chemical looping combustion system of biomass based on interconnected fluidized beds

    • 摘要: 采用钙钛矿作为载氧体、木屑作为燃料,开展了10 MWth生物质化学链燃烧装置热力学设计。研究结果为获得了在自热操作条件下,化学链燃烧系统反应器尺寸和关键热平衡参数。结果如下:空气反应器选用高效的快速流化床设计,其床层高度为45.5 m,横截面积为2.96 m2,表观气速为4.37 m/s;燃料反应器设计为上下2层,上层为快速流化床,下层为鼓泡流化床。床层总高为31.06 m,上层床高26.21 m,下层床高9.31 m,上下层横截面积分别为1.94和7.76 m2,上下层表观气速分别为3.52和0.31 m/s,满足载热条件下的载氧体循环流率为101.14 kg/s。该热力学计算结果为以生物质为燃料的化学链燃烧系统的设计提供了参考。

       

      Abstract: Using perovskite as oxygen carrier and wood chips as fuel, the thermodynamic analysis of 10 MWth biomass chemical looping combustion system is conducted. The results obtain the reactor size and key thermal balance parameters required by the system under self-thermal operation conditions. The results are as follows: The results are as follows: the air reactor is efficient rapid fluidized bed design, its bed height is 45.5 m, cross-sectional area is 2.96 m2, apparent air velocity is 4.37 m/s; the fuel reactor is designed as two upper and lower layers, the upper layer is fast fluidized bed and the lower layer is bubble fluidized bed. The total height of the bed is 31.06 m, the height of the upper bed is 26.21 m, the height of the lower bed is 9.31 m, the cross section area of the upper and lower layers is 1.94 m2 and 7.76 m2 respectively, the apparent gas velocity of the upper and lower layers is 3.52 m/s and 0.31 m/s respectively, and the circulation rate of the oxygen carrier is 101.14 kg/s under the heat load condition. The thermal calculation results provide a reference for the design of a chemical looping combustion system with biomass as a fuel

       

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