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生物质在微型流化床中热解动力学与机理
引用本文:余剑,朱剑虹,郭凤,段正康,刘云义,许光文.生物质在微型流化床中热解动力学与机理[J].燃料化学学报,2010,38(6):666-672.
作者姓名:余剑  朱剑虹  郭凤  段正康  刘云义  许光文
作者单位:1.State Key Laboratory of Multi-phase Complex System,; Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China;; 2.Chemical Engineering Institute of Xiangtan University, Xiangtan 411105, China;; 3.School of Chemical Engineering, Shenyang Institute of Chemical Technology, Shenyang 110142, China
基金项目:国家重点基础研究发展规划(973计划,国家高技术研究发展计划(863计划,中国博士后科学基金
摘    要:利用微型流化床反应分析仪(MFBRA)研究了生物质在氩气氛中的热解反应,通过在线反应物供给和生成气组成变化监测,实现了设定温度下生物质热解反应速率的测试、动力学参数的求算和反应机理的分析。应用该仪器测定的生物质在800℃的热解时间为10s,明显小于传统文献报道值。测试的气体释放顺序与反应动力学参数初步证实了生成的不同气体间存在耦合反应,且各气体生成难易程度存在差异。测试的反应级数为1.62,以整体挥发分为基准的活化能与指前因子分别是11.77kJ/mol和1.45s-1,明显小于常规热重方法的测试值。

关 键 词:  style="font-size:  9pt  line-height:  微型流化床" target="_blank">150%">微型流化床  反应动力学  生物质热解  
收稿时间:4 February 2010
修稿时间:26 April 2010

Reaction kinetics and mechanism of biomass pylolysis in a micro-fluidized bed reactor
YU Jian,ZHU Jian-hong,GUO Feng,DUAN Zheng-kang,LIU Yun-yi,XU Guang-wen.Reaction kinetics and mechanism of biomass pylolysis in a micro-fluidized bed reactor[J].Journal of Fuel Chemistry and Technology,2010,38(6):666-672.
Authors:YU Jian  ZHU Jian-hong  GUO Feng  DUAN Zheng-kang  LIU Yun-yi  XU Guang-wen
Institution:a State Key Laboratory of Multi-phase Complex System, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China;b Chemical Engineering Institute of Xiangtan University, Xiangtan 411105, China;c School of Chemical Engineering, Shenyang Institute of Chemical Technology, Shenyang 110142, China
Abstract:A Micro Fluidized Bed Reaction Analyzer (MFBRA) was used to study the pyrolysis of biomass in argon. Through on-line pulse feeding of reactant and continuously monitoring the composition changes of gas product, the MFBRA enables the measurement of reaction rates at arbitrary temperatures, the deduction of kinetic parameters and the analysis of reaction mechanism. By applying to biomass pyrolysis this article found that the pyrolysis reaction can finish in about 10s, which is much shorter than the other literature values obtained in larger fluidized bed reactors but very close to the theoretically anticipated values. The detected evolving sequences of different gas species and the deduced kinetic parameters demonstrate further that the reactions between/among the formed different gas species in pyrolysis prevail to certain degree and there are different pathways for forming the different gas species. The activation energy and pre-exponential factor derived by treating the pyrolysis gas as a single product are 11.77kJ/mol and 1.45s-1, which are obviously lower than the literature values measured in thermogravimetric analyzers.
Keywords:micro fluidized bed  reaction kinetics  biomass pyrolysis
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