Design and experimental study of a two-stage pilot scale biomass fixed bed gasifier

Zhongqing Ma, Yimeng Zhang, Qi-sheng Zhang, Jianbin Zhou, Haiyan Wang, Phuong T. M. Tong
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引用次数: 2

Abstract

Two stage biomass fixed bed gasifier has the advantage of lower tar content and higher calorific value of producer gas. This paper presented design and experimental investigation of a 190KWe (nominal) pilot scale biomass fixed bed gasifier using a double air stage downdraft approach. Wood chips were used as feedstock. The results demonstrated that due to the secondary air supply, a temperature as high as 900oC in the oxidation zone for a better tar cracking. Use of both stirrer and reciprocating grate avoided bridging and channeling. A direct connection of the gasification chamber and charcoal cooling chamber could minimize gas storage space to avoid deflagration. The average value of the composition was about 16.6% (CO), 2.3% (CH4), 16.1% (H2), 13.8% (CO2) and 0.4% (O2) whereas the average calorific value was 4.7MJ/ Nm3. The maximal LHV was 5.28 MJ/ Nm3 when the frequency of draft fan and secondary air supply were 45 Hz and 54 Nm3/h respectively.
两级中试规模生物质固定床气化炉的设计与实验研究
两段式生物质固定床气化炉具有产气焦油含量低、热值高的优点。本文介绍了采用双空气级下吸法的190KWe(标称)中试规模生物质固定床气化炉的设计和实验研究。以木屑为原料。结果表明,由于二次送风,氧化区温度高达900℃,焦油裂解效果较好。使用搅拌器和往复式炉排避免桥接和通道。气化室和木炭冷却室直接连接,可以减少气体储存空间,避免爆燃。其组成平均约为16.6% (CO)、2.3% (CH4)、16.1% (H2)、13.8% (CO2)和0.4% (O2),平均发热量为4.7MJ/ Nm3。风机频率为45 Hz,二次送风频率为54 Nm3/h时,最大LHV为5.28 MJ/ Nm3。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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