采用一维拟均相绝热径向反应器模型模拟乙苯负压脱氢径向反应器。
An one dimensional homogenous adiabatic fixed bed reactor model was adopted to simulate a radial flow reactor for dehydrogenation of ethylbenzene to styrene under vacuum.
由丁径向反应器内气体流道面积的变化，其着火和熄火规律与轴向床有所不同。
Ignition and extinction of radial flow reactors are different from those of axial flow ones because of the change of gas velocity.
相应推导出了径向反应器和轴向反应器的微分方程组，为重整反应过程计算机模拟提供了理论依据。
Differential equations of both reactors were deduced correspondently. These supply theoretical basis for computer simulation of reforming.
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