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Industrial demonstration plant for the gasification of herb residue by fluidized bed two-stage process

机译:工业示范工厂,通过流化床两阶段工艺气化草药残渣

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摘要

A fluidized bed two-stage gasification process, consisting of a fluidized-bed (FB) pyrolyzer and a transport fluidized bed (TFB) gasifier, has been proposed to gasify biomass for fuel gas production with low tar content. On the basis of our previous fundamental study, an autothermal two-stage gasifier has been designed and built for gasify a kind of Chinese herb residue with a treating capacity of 600 kg/h. The testing data in the operational stable stage of the industrial demonstration plant showed that when keeping the reaction temperatures of pyrolyzer and gasifier respectively at about 700 degrees C and 850 degrees C, the heating value of fuel gas can reach 1200 kcal/Nm3, and the tar content in the produced fuel gas was about 0.4 g/Nm(3). The results from this pilot industrial demonstration plant fully verified the feasibility and technical features of the proposed FB two-stage gasification process. (C) 2016 Published by Elsevier Ltd.
机译:已经提出了由流化床(FB)热解器和运输流化床(TFB)气化器组成的流化床两阶段气化方法,以气化低焦油含量的生物质以生产燃料气体。在我们之前的基础研究的基础上,设计并建造了一种自动热两级气化炉,用于气化一种处理能力为600 kg / h的中草药残留物。工业示范厂运行稳定阶段的测试数据表明,将热解炉和气化炉的反应温度分别保持在700℃和850℃左右时,燃气的发热量可以达到1200 kcal / Nm3,产生的燃料气体中的焦油含量约为0.4 g / Nm(3)。该试验性工业示范工厂的结果充分验证了拟议的FB两阶段气化工艺的可行性和技术特点。 (C)2016由Elsevier Ltd.出版

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