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采用流化床两段法气化草本残余物的工业示范工厂。

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

机构信息

State Key Laboratory of Multi-Phase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China.

College of Chemical Engineering, Inner Mongolia University of Technology, Hohhot 010051, China.

出版信息

Bioresour Technol. 2016 Apr;206:93-98. doi: 10.1016/j.biortech.2016.01.075. Epub 2016 Jan 29.

Abstract

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 °C and 850 °C, the heating value of fuel gas can reach 1200 kcal/Nm(3), 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.

摘要

提出了一种流化床两段气化工艺,包括流化床(FB)热解器和输送流化床(TFB)气化炉,用于气化生物质以生产低焦油含量的燃料气。基于我们之前的基础研究,设计并建造了一种自热两段式气化炉,用于气化一种中国草药残渣,处理能力为 600 千克/小时。工业示范装置运行稳定阶段的测试数据表明,当分别保持热解器和气化炉的反应温度在约 700°C 和 850°C 时,燃料气的热值可达 1200 千卡/Nm(3),并且产生的燃料气中的焦油含量约为 0.4 克/Nm(3)。该中试工业示范装置的结果充分验证了所提出的 FB 两段气化工艺的可行性和技术特点。

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