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固定床反应器中生物油水溶性组分热解反应动力学
引用本文:刘少敏,陈明强,胡青松,杨忠连,李峰,汪娟,王君. 固定床反应器中生物油水溶性组分热解反应动力学[J]. 石油学报(石油加工), 2013, 29(3): 422-426. DOI: 10.3969/j.issn.1001-8719.2013.03.009
作者姓名:刘少敏  陈明强  胡青松  杨忠连  李峰  汪娟  王君
作者单位:1安徽理工大学 地球与环境学院, 安徽 淮南 232001; 2安徽理工大学 化学工程学院, 安徽 淮南 232001
基金项目:高等学校博士学科点专项科研基金(20093415110003);安徽省教育厅自然科学基金重点项目(KJ2012A070)资助
摘    要:在空气气氛下采用热重分析法研究了固定床反应器中生物油水溶性组分的热解特性,利用Achar微分法和Coats-Redfern积分法相结合的方式进行动力学分析,计算了挥发和热分解的活化能、反应级数和动力学参数,确定了机理函数,并建立了热解动力学模型。结果表明,生物油水溶性组分的热解可分为3个阶段,即轻组分挥发段、重组分热解段和焦炭燃烧段,重组分热解段活化能较轻组分挥发段的活化能低很多。轻组分挥发段反应级数近似为一级,可采用一级反应模型来模拟,而重组分热解段反应级数近似为二级,可采用二级模型来表示。

关 键 词:生物油  热重分析  反应级数  动力学模型  
收稿时间:2012-05-07

Pyrolysis Kinetic Analysis for Water-Soluble Fraction of Bio-oil in Fixed Bed Reactor
LIU Shaomin,CHEN Mingqiang,HU Qingsong,YANG Zhonglian,LI Feng,WANG Juan,WANG Jun. Pyrolysis Kinetic Analysis for Water-Soluble Fraction of Bio-oil in Fixed Bed Reactor[J]. Acta Petrolei Sinica (Petroleum Processing Section), 2013, 29(3): 422-426. DOI: 10.3969/j.issn.1001-8719.2013.03.009
Authors:LIU Shaomin  CHEN Mingqiang  HU Qingsong  YANG Zhonglian  LI Feng  WANG Juan  WANG Jun
Affiliation:1School of Earth Science and Environmental Engineering, Anhui University of Science and Technology, Huainan 232001, China; 2. School of Chemical Engineering, Anhui University of Science and Technology, Huainan 232001, China
Abstract:The pyrolysis behaviors and kinetics of the water-soluble fraction of bio-oil in the oxygen atmosphere in a fixed bed reactor were studied by thermogravimetric (TG) analysis. Based on the experimental data, activation energies, reaction order and kinetic parameters were calculated by the Achar differential method and the Coats-Redfern integral method, the most probable mechanism functions were worked out, and therefore, thermal kinetic equations were finally obtained. The results showed that the pyrolysis of water-soluble fraction of bio-oil could be divided into three stages, that is, the evaporation of volatile fractions, the decomposition of heavy fractions and char combustion. The activation energies of volatilization were higher than those of decomposition stage. The first stage was expressed as first order reaction, which could be simulated by first order reaction model, and the second stage was expressed as second order reaction, which could be presented by the corresponding reaction model.
Keywords:bio-oil  thermogravimetry  reaction order  kinetics model  
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