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长链烷烃脱氢制单烯烃动力学模型

Kinetic Model of Heavy Paraffin Dehydrogenation to Mono-olefins

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【作者】 江洪波张晴周立群王玉曹晶

【Author】 JIANG Hongbo;ZHANG Qing;ZHOU Liqun;WANG Yu;CAO Jing;Research Institute of Petroleum Processing,East China University of Science and Technology;LAB Plant of Jinling Petrochemical Corporation of SINOPEC;

【机构】 华东理工大学石油加工研究所中国石化金陵石化有限责任公司烷基苯厂

【摘要】 根据长链烷烃催化脱氢反应机理,采用某新型国产长链烷烃脱氢催化剂,建立了工业反应条件下的直链烷烃脱氢制单烯烃表观反应动力学模型和催化剂失活模型。以在轴向连续流动固定床微型反应器中C10~C13直链烷烃脱氢反应的实验数据为基础,采用多元函数包维尔(Powell)法优化计算了反应速率常数、失活速率常数、失活级数与活化能,实验值与计算值拟合效果良好。动力学模型参数分析表明了所建模型动力学与热力学的合理性。

【Abstract】 Based on the reaction mechanism of heavy paraffin catalytic dehydrogenation,with a new domestic catalyst of paraffin dehydrogenation as research objective,apparent reaction kinetic model and catalyst deactivation model of heavy paraffins dehydrogenation to mono-olefins were established under industrial reaction conditions.Based on the experimental data of C10—C13 paraffins dehydrogenation in an axial continuous flow fixed bed microreactor,the reaction rate constants,deactivation rate constants,deactivation order and activation energy were calculated by multivariate function Powell method,and the fitting effect of experimental values and calculated values is good.The analysis of kinetic model parameters showed the rationality of kinetics and thermodynamics.

  • 【文献出处】 石油学报(石油加工) ,Acta Petrolei Sinica(Petroleum Processing Section) , 编辑部邮箱 ,2016年01期
  • 【分类号】TQ221.2
  • 【被引频次】2
  • 【下载频次】93
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