Radial hydrodynamics in risers

被引:20
作者
Godfroy, L
Patience, GS [1 ]
Chaouki, J
机构
[1] Dupont Co, Wilmington, DE 19880 USA
[2] Ecole Polytech, Dept Chem Engn, Montreal, PQ H3C 3A7, Canada
关键词
D O I
10.1021/ie960784i
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
On the basis of the benchmark modeling exercise at Fluidization VIII, predicting riser hydrodynamics continues to be more of an art than a science. Ten different hydrodynamic models were compared with a set of experimental data that covered a wide range of operating conditions and showed reasonable to poor overall agreement. Herein, we describe the model that gave the best overall agreement with: the experimental data. Density is calculated by a correlation based on slip factor, and the radial voidage profile depends solely on the cross-sectional average void fraction. Both the gas and velocity profile follows a power law type expression; the gas velocity at the wall is zero. The model predictions agree well with experiments conducted with sand but not as well as those conducted with fluidized catalytic cracking catalyst.
引用
收藏
页码:81 / 89
页数:9
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