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甲苯液相催化氧化过程模拟与优化(英文)

Simulation and Optimization in the Process of Toluene Liquid-phase Catalytic Oxidation

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【作者】 张玉坤李初福何小荣陈丙珍

【Author】 ZHANG Yukun , LI Chufu , HE Xiaorong and CHEN Bingzhen Department of Chemical Engineering, Tsinghua University, Beijing 100084, China

【机构】 Department of Chemical Engineering Tsinghua UniversityDepartment of Chemical EngineeringTsinghua UniversityBeijing 100084China

【摘要】 Liquid-phase oxidation of toluene with air has become the main technology for producing benzoic acid in a reactor at present. Based on the kinetic model of the toluene oxidation process obtained from laboratory and mass balance of key component, a novel model is established to simulate the industrial toluene oxidation process, in which the effects of benzaldehyde and benzyl alcohol are considered and the kinetic parameters are revised by in-dustrial data. The simulation results show that the error of benzoic acid yield is within 3.5%. Based on the simula-tion model, to maximize the benzoic acid yield, an optimization model is proposed to optimize the operating pa-rameters, including toluene feed-in mass flux and temperature. The optimization result indicates that on the allow-able operating conditions, the maximum benzoic acid yield obtained with the reaction temperature at 167.2°C and the mass flux at 104.1 t·h-1 is greater than the current one, which can be used to guide industrial reactor’s operation.

【Abstract】 Liquid-phase oxidation of toluene with air has become the main technology for producing benzoic acid in a reactor at present. Based on the kinetic model of the toluene oxidation process obtained from laboratory and mass balance of key component, a novel model is established to simulate the industrial toluene oxidation process, in which the effects of benzaldehyde and benzyl alcohol are considered and the kinetic parameters are revised by in-dustrial data. The simulation results show that the error of benzoic acid yield is within 3.5%. Based on the simula-tion model, to maximize the benzoic acid yield, an optimization model is proposed to optimize the operating pa-rameters, including toluene feed-in mass flux and temperature. The optimization result indicates that on the allow-able operating conditions, the maximum benzoic acid yield obtained with the reaction temperature at 167.2°C and the mass flux at 104.1 t·h-1 is greater than the current one, which can be used to guide industrial reactor’s operation.

  • 【文献出处】 Chinese Journal of Chemical Engineering ,中国化学工程学报(英文版) , 编辑部邮箱 ,2008年01期
  • 【分类号】TQ032
  • 【被引频次】12
  • 【下载频次】189
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