A detailed investigation of a thermodynamic process in a structured packing distillation column is of great importance in prediction of process efficiency. In order to keep the simplicity of an equilibrium stagemodel and the accuracy of a non-equilibrium stage model
a hybrid model is developed to predict the structured packing column in cryogenic air separation. A general solution process for the equilibrium stage model is developed to solve the set of equations of the hybrid model
in which a separation efficiency function is introduced to obtain the resulting tri-diagonal matrix and its solution by the Thomas algorithm. As an example
the algorithm is applied to analyze an upper column of a cryogenic air separation plant with the capacity of 17000 m
3
·h
-1
. Rigorous simulations are conducted using Aspen RATEFRACmodule to validate the approach. The temperature and composition distributions are in a good agreementwith the two methods. The effects of inlet/outlet position and flowrate on the temperature and composition distributions in the column are analyzed. The results demonstrate that the hybrid model and the solution algorithms are effective in analyzing the distillation process for a cryogenic structured packing colum
n.
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相关作者
Haotian Zheng
Zhixi Zhang
Guangyan Wang
Yatao Wang
Jun Liang
Weiyi Su
Yuqi Hu
Xiong Yu
相关机构
Coal Chemical R&D Center of Kailuan Group
School of Information Engineering, Tianjin University of Commerce
School of Chemical Engineering and Technology, National-Local Joint Engineering Laboratory for Energy Conservation in Chemical Process Integration and Resources Utilization, Hebei University of Technology
Engineering Research Center of Preparation Technology of Ultra-Pure Chemicals for Integrated Circuit, Ministry of Education, Beijing University of Chemical Technology
State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology