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BUBBLE SIZES AND HOLDUP STRUCTURE IN BUBBLE COLUMNS DETERMINED BY DYNAMIC GAS DISENGAGEMENT
作者姓名:罗和安  KaiHjarbo  HallvardSvendsen
作者单位:Department of Chemical Engineering,Norwegian Institute of Technology,7034 Trondheim,Norway,Department of Chemical Engineering,Norwegian Institute of Technology,7034 Trondheim,Norway
摘    要:A new model for determining bubble size distributions in bubble columns by the dynamic gasdisengagement(DGD)technique is developed.It is based on an idea of non-uniform steady statedirstribution of bubble dispersion.Interpreting the axial non-uniformity,this model gives axial gasholdup distributions.If assuming an axially homogeneous dispersion,a radial gas holdup distributioncan be obtained.The Sauter mean diameters or specific interfacial areas for several systems areestimated by the technique.The results for an air-water system agree with those measured by afive-point conductivity probe technique.The obtained axial gas holdup distributions agree well withreported measurements and the radial gas holdup distributions are also reasonable.

关 键 词:bubble  size  gas  holdup  measurement  dynamic  gas  disengagement
收稿时间:1994-11-2
修稿时间:1995-2-16  

BUBBLE SIZES AND HOLDUP STRUCTURE IN BUBBLE COLUMNS DETERMINED BY DYNAMIC GAS DISENGAGEMENT
LUO Hean,KaiHjarbo,HallvardSvendsen.BUBBLE SIZES AND HOLDUP STRUCTURE IN BUBBLE COLUMNS DETERMINED BY DYNAMIC GAS DISENGAGEMENT[J].Chinese Journal of Chemical Engineering,1996,4(2):150-161.
Authors:LUO Hean  KaiHjarbo  HallvardSvendsen
Affiliation:Department of Chemical Engineering, Norwegian Institute of Technology, 7034 Trondheim, Norway
Abstract:A new model for determining bubble size distributions in bubble columns by the dynamic gas disengagement (DGD) technique is developed. It is based on an idea of non-uniform steady state dirstribution of bubble dispersion. Interpreting the axial non-uniformity, this model gives axial gas holdup distributions. If assuming an axially homogeneous dispersion, a radial gas holdup distribution can be obtained. The Sauter mean diameters or specific interfacial areas for several systems are estimated by the technique. The results for an air-water system agree with those measured by a five-point conductivity probe technique. The obtained axial gas holdup distributions agree well with reported measurements and the radial gas holdup distributions are also reasonable.
Keywords:bubble size  gas holdup  measurement  dynamic gas disengagement
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