对苯与低浓度丙烯合成异丙苯的催化精馏过程建立非平衡级模型。
The non-equilibrium stage model is used to simulate catalytic distillation process for cumene synthesis using low concentration propylene and benzene.
通过计算获得了界面温度、速度、溶质浓度及非平衡分配系数随界面位置的变化。
The interface temperature, velocity, solute concentration and non-equilibrium partition coefficient varying with interface location are calculated.
利用与非静力平衡中尺度气象模式完全耦合的区域沙尘数值模式，模拟研究这次强沙尘天气过程中沙尘浓度的空间分布结构和时间演变趋势。
The spatial and temporal distribution and development of dust concentration and structure were simulated by a coupled dust model with non-hydrostatic mesoscale model.
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