摘要
用V_2O_5为活性组分的SD固体催化剂,在等温积分反应器中研究了文题。实验在工业生产操作条件下进行,用氧化还原动力学模型进行参数估值,给出了苯氧化反应动力学参数,该参数可用于反应器模拟计算。
The reaction kinetics of the oxidation of benzene to maleic anhydride over vanadium oxide catalysts has been studied in an isothermal integral reactor in the temperature range from 360 to 400℃. The rate data were correlated by the expressions based upon the steady state oxidation-reduction model. The parameters of kinetics has been obtained and can be used for both research and design of industrial reactors.
关键词
顺丁烯二酸酐
苯
固定床反应器
kinetics
fixed bed reactor
benzene
maleic anhydride
catalytic reaction
