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OXYGEN CARRIER/CARBON CARRIER-BASED BIOMASS CHEMICAL LOOPING GASIFICATION METHOD AND DEVICE

机译:基于氧载体/碳载体的生物质化学环化气化方法及装置

摘要

An oxygen carrier/carbon carrier-based biomass chemical looping gasification method and device. The device comprises an air reactor (1), a second separator (5-2), a calcination reactor (3), a first separator (5-1), and a gasification reactor (2) connected in sequence. The top of the calcination reactor (3) is communicated with an air inlet of a third cyclone separator (4-3). A solid particle discharge port on the bottom of the third cyclone separator (4-3) is communicated with the calcination reactor (3). An exhaust pipeline of the third cyclone separator (4-3) is communicated with the air inlet on the bottom of the calcination reactor (3) by means of a valve. An air outlet of the gasification reactor (2) is communicated with the air inlet of a first cyclone separator (4-1). The solid particle discharge port of the first cyclone separator (4-1) extends into the bottom in the gasification reactor (2) by means of the pipeline. The air outlet of the gasification reactor (2) is communicated with the air inlet of a second cyclone separator (4-2). By combining respective advantages of the chemical looping gasification and CaO absorber methods, the method optimizes the existing chemical looping gasification process, improves the energy utilization efficiency of a biomass, and effectively separates CO 2 generated by a reaction.
机译:基于氧载体/碳载体的生物质化学回路气化方法和装置。该装置包括依次连接的空气反应器(1),第二分离器(5-2),煅烧反应器(3),第一分离器(5-1)和气化反应器(2)。煅烧反应器(3)的顶部与第三旋风分离器(4-3)的进气口连通。第三旋风分离器(4-3)底部的固体颗粒排出口与煅烧反应器(3)连通。第三旋风分离器(4-3)的排气管道通过阀与煅烧反应器(3)底部的进气口连通。气化反应器(2)的空气出口与第一旋风分离器(4-1)的空气入口连通。第一旋风分离器(4-1)的固体颗粒排出口通过管道延伸到气化反应器(2)的底部。气化反应器(2)的空气出口与第二旋风分离器(4-2)的空气入口连通。结合化学环化气化和CaO吸收器方法各自的优点,该方法优化了现有的化学环化气化工艺,提高了生物质的能量利用效率,并有效分离了反应生成的CO 2

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