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