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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.
A new model for determining bubble size distributions in bubble columns by the dynamic gas disposition (DGD) technique is developed. It is based on an idea of non-uniform steady-state distribution 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 are asstid by the technique.The results for an air-water system agree with those measured by afive-point conductivity probe technique. The resulting axial gas holdup distributions agree well withreported measurements and the radial gas holdup distributions are also reasonable.