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生物质流化床氧气-水蒸气气化实验研究

苏德仁 刘华财 周肇秋 阴秀丽 吴创之

苏德仁, 刘华财, 周肇秋, 阴秀丽, 吴创之. 生物质流化床氧气-水蒸气气化实验研究[J]. 燃料化学学报(中英文), 2012, 40(03): 309-314.
引用本文: 苏德仁, 刘华财, 周肇秋, 阴秀丽, 吴创之. 生物质流化床氧气-水蒸气气化实验研究[J]. 燃料化学学报(中英文), 2012, 40(03): 309-314.
SU De-ren, LIU Hua-cai, ZHOU Zhao-qiu, YIN Xiu-li, WU Chuang-zhi. Biomass gasification with oxygen and steam in a fluidized bed gasifier[J]. Journal of Fuel Chemistry and Technology, 2012, 40(03): 309-314.
Citation: SU De-ren, LIU Hua-cai, ZHOU Zhao-qiu, YIN Xiu-li, WU Chuang-zhi. Biomass gasification with oxygen and steam in a fluidized bed gasifier[J]. Journal of Fuel Chemistry and Technology, 2012, 40(03): 309-314.

生物质流化床氧气-水蒸气气化实验研究

基金项目: 国家高技术研究发展计划(863计划, 2007AA05Z410, 2009AA05Z434);中国科学院创新方向项目(KGCX2-YW-329)。
详细信息
    通讯作者:

    阴秀丽, 研究员, 研究方向为生物质能源利用, E-mail: xlyin@ms.giec.ac.cn。

  • 中图分类号: TK6

Biomass gasification with oxygen and steam in a fluidized bed gasifier

  • 摘要: 在小型流化床气化装置上进行了氧气-水蒸气气化实验,考察了原料、当量比、水蒸气配比、温度、二次风和床料对气化特性的影响。结果表明,原料中C和H含量越高,气化气中H2和CO含量越高,焦油含量越低;当量比为0.27和水蒸气配比为0.6时,H2含量达到最大值;温度的升高可提高H2含量,在840 ℃以上,可提高CO含量;二次风从进料口偏上且二次风比率为15%通入,气体组分变化较明显,二次风通入点位置越高,焦油含量降低幅度越大;白云石和石灰石裂解焦油和提高H2含量的活性高于橄榄石,但同时明显提高了气体中的灰分含量。
  • 吴创之, 阴秀丽, 徐冰燕, 罗曾凡, 刘平. 生物质富氧气化特性的研究[J]. 太阳能学报, 1997, 18(3): 237-242. (WU Chuang-zhi, YIN Xiu-li, XU Bing-yan, LUO Zeng-fan, LIU Ping. The performance study of biomass gasification with oxygen-rich air[J]. Acta Energiae Solaris Sinica, 1997, 18(3): 237-242.)
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    SWIERCZYHSKI D, COURSON C, BEDEL L, KIENNEMANN A, VILMINOT S. Oxidation reduction behavior of iron-rearing olivines (Fe Mg1-x)2SiO4 used as catalysts for biomass gasification[J]. Chem Mater, 2006, 18(4): 897-905.
    陈汉平, 杨海平, 李斌, 杨国来, 王贤华, 张世红. 生物质流化床气化焦油析出特性的研究[J]. 燃料化学学报, 2009,37(4): 433-437. (CHEN Han-ping, YANG Hai-ping, LI Bin, YANG Guo-lai, WANG Xian-hua, ZHANG Shi-hong. Evolving characteristics of tar during biomass fluidized bed gasification[J]. Journal of Fuel Chemistry and Technology, 2009, 37(4): 433-437.)
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出版历程
  • 收稿日期:  2011-04-03
  • 刊出日期:  2012-03-31

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