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SIMULATION AND EFFICIENCY OF LARGE TRAY Part Ⅰ EDDY DIFFUSION MODEL WITH NONUNIFORM LIQUID VELOCITY FIELD

YU Kuotsung; HUANG Jie; GU Fangzhen   

  1. Department of Chemical Engineering, Tianjin University
  • Received:1900-01-01 Revised:1900-01-01 Online:1983-12-28 Published:1983-12-28
  • Contact: YU Kuotsung

SIMULATION AND EFFICIENCY OF LARGE TRAY Part Ⅰ EDDY DIFFUSION MODEL WITH NONUNIFORM LIQUID VELOCITY FIELD

余国琮; 黄洁; 顾芳珍   

  1. Department of Chemical Engineering, Tianjin University
  • 通讯作者: 余国琮

Abstract: Experimental study of flow pattern and liquid velocity distribution by the tracer technique in a twometers diameter single pass sieve half-tray using air-water system reveals that there exists a highlynonideal flowing behavior.Typical residence time distribution curves covering the whole tray are presented,from which four flow regions can be observed: a main channelling region of nonuniform flow,a slowly forward flow region in the segmental area,a small region of backward flow and a complete-mixing region next to the inlet weir.The tray models available in literature seem incapable to simulateall these complicated hydrodynamic phenomena in a large tray.An eddy diffusion model with consideration of nonuniform liquid velocity field has been developedfrom the basic partial differential equation of mass transfer by introducing a velocity distributionfunction j.The nonlinear partial differential equation is solved by the method of finite element.Acomputer program is compiled according to this method to compute numerically the concentration pro-files in the whole tray as well as the Murphree tray efficiency enhancement under various operatingconditions.Typical computed results are presented and discussed.

摘要: Experimental study of flow pattern and liquid velocity distribution by the tracer technique in a twometers diameter single pass sieve half-tray using air-water system reveals that there exists a highlynonideal flowing behavior.Typical residence time distribution curves covering the whole tray are presented,from which four flow regions can be observed: a main channelling region of nonuniform flow,a slowly forward flow region in the segmental area,a small region of backward flow and a complete-mixing region next to the inlet weir.The tray models available in literature seem incapable to simulateall these complicated hydrodynamic phenomena in a large tray.An eddy diffusion model with consideration of nonuniform liquid velocity field has been developedfrom the basic partial differential equation of mass transfer by introducing a velocity distributionfunction j.The nonlinear partial differential equation is solved by the method of finite element.Acomputer program is compiled according to this method to compute numerically the concentration pro-files in the whole tray as well as the Murphree tray efficiency enhancement under various operatingconditions.Typical computed results are presented and discussed.