两级中试规模生物质固定床气化炉的设计与实验研究

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

摘要

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