CIESC Journal

• 化工学报 •    下一篇

精馏过程的新逐板计算法——(I)多元精馏过程的操作型计算

张瑞生,吴俊生,陈敏恒   

  1. 华东化工学院 ,华东化工学院 ,华东化工学院
  • 出版日期:1983-12-25 发布日期:1983-12-25

A New Plate-to-Plate Method for Calculating Distillation Processes (I) Performance Prediction of Multicomponent Distillation Processes

Zhang Ruisheng, Wu Junsheng and Chen Mingheng East China, Institute of Chemical Technology   

  • Online:1983-12-25 Published:1983-12-25

摘要: 本文应用迭代数学理论提出了一个适用于理想系统和与之相近的轻烃系统的多元精馏操作型计算的新逐板计算法.它将整个迭代过程重组为总量迭代和比值迭代二个平行的迭代过程,获得了快速且均匀的收敛性.本法为直接设计型计算法打下了必要基础.

Abstract: In the present paper, a new plate-to-plate method is developed for performance prediction of ideal systems and those close to ideal ones. The sum ofmole fractions of heavy components in the top product, ∑HP, as well as mole fraction ratios of heavy components in the upper part of a column and those of light components in the lower part, vij s and μij s, are selected as iterative variables instead of individual concentrations. Two parallel iterations are suggested. The first one is for ∑HP. The mole fractions of various light components are calculated top-down towards the match plate. The mole fraction of various heavy components are calculated bottom-up towards the match plate. ∑HP is then relaxed with the total match tolerance of heavy components. The second one is for vijs and μijs. The subsequent guess of vijs and μijs is calculated from the solution of tridiagnol matrices with the phase equilibrium constants Kijs obtained from the plate-to-plate calculation. Consequently, the related loops consist of a single strong loop accompanied by a number of comparatively insignificant loops. Thus, a multi-variable system can be converted into a single variable system and the convergence can be dramatically accelear-ated. A rapid and stable convergence is finally achieved. This procedure has been successfully used for complex columns with multifeed and multi-side-stream .