CIESC Journal

• 化工学报 •    下一篇

大型塔板的模拟与板效率的研究(Ⅱ)——二维定数混合池模型

余国琮,顾芳珍   

  1. 天津大学化工系 ,天津大学化工系
  • 出版日期:1981-06-25 发布日期:1981-06-25

Simulation and Efficiency of Large Tray(II)——Two Dimensional Fixed Number Mixing Pool Model

Yu Kuo-tsung and Gu Fangzhen Department of Chemical Engineering, Tianjin University   

  • Online:1981-06-25 Published:1981-06-25

摘要: 为研究大型塔板在复杂流动情况下的浓度分布与板效率计算方法,本文提出二维、固定混合池数、可调整流量的数学模型。此模型可以比较灵活地模拟大型塔板上的各种实际流动现象,并能比较方便地计算出在该流动情况下的塔板浓度分布及板效率值。

Abstract: A new mathematical model of mixing pool type is proposed to simulated the fluid flow and mass transfer behavior in a large tray. In the proposed model, the whole tray deck is divided into a number of square (or rectangular) compartments or mixing pools, each of which is assigned to have adjustable flow and backmixing in both z (along the main flow path) and w (perpendicular to the main flow path) directions. The chief features of present model are: (1)It is a two dimensional model instead of usual one dimensional so that more complicated actual flowing condition obtained from hydrodynamic study in a large tray can be closely simulated by adjusting the flow among mixing pools in both z and w directions. (2)Since backmixing is taken into account, the number of mixing pools in a tray can be fixed instead of varied as in conventional mixing pool model;thus, the application of matrix computation is possible. (3) The present model can be reduced to other tray models depending on the number of mixing pools to be chosen in each direction. The application of present model to predict the liquid phase concentration profiles and Murphree efficiencies in a tray with complicated flow pattern and velocity distribution as we observe in our experimental study are demonstrated. The effects of liquid flow rate, non-uniform velocity field, directional splashing and subsidiary flow are also investigated and discussed.