ALTERNATING FLOW MODEL FOR MASS AND HEAT DISPERSION IN PACKED-BEDS

被引:12
|
作者
KLINGMAN, KJ [1 ]
LEE, HH [1 ]
机构
[1] UNIV FLORIDA,DEPT CHEM ENGN,GAINESVILLE,FL 32611
关键词
HEAT TRANSFER - Packed Beds - MASS TRANSFER - Packed Beds;
D O I
10.1002/aic.690330303
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The alternating flow model (AFM) views dispersion in packed beds as a sequence of streamline plugs that must repeatedly split and merge as the bulk fluid traverses the vessel. Thus, the flow in the AFM is ordered, as opposed to the random flow implied by the Fickian analogy. For mass dispersion only, model parameters arise from a priori considerations of packing geometry. Steady state and transient data (5. 6 less than D//t/d//p=21 54. 4, 100 less than Re//p less than 1000, gases and liquids) show the AFM to surpass the Fickian analogy (based on correlations for dispersion coefficients) in most cases.
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页码:366 / 381
页数:16
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