摘要
This paper presents an improved three-dimensional non-equilibrium mixing pool model.It is a simplified form of the original model and is more practical for applications.The simulation re-sults show that the industrial scale distillation tray columns can be described closely by the improvedmodel.The effects of model parameters,such as the number of mixing pools,the point efficiencyand flow pattern,on separation are analyzed quantitatively.
This paper presents an improved three-dimensional non-equilibrium mixing pool model. It is a simplified form of the original model and is more practical for applications. The simulation results show that the industrial scale distillation tray columns can be described closely by the improved model. The effects of model parameters, such as the number of mixing pools, the point efficiency and flow pattern, on separation are analyzed quantitatively.
基金
Supported by the National Natural Science Foundation of China.
