基于离散颗粒法模拟搅拌釜气含率分布
O3; The discrete particle method was used to simulate the distribution of gas holdup in a gas-liquid standard Rushton stirred tank. The gas phase was treated as a large number of bubbles and their trajectories were tracked with the results of motion equations. The two-way approach was performed to c...
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Published in | 中国化学工程学报(英文版) Vol. 15; no. 6; pp. 808 - 813 |
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Main Authors | , , |
Format | Journal Article |
Language | Chinese |
Published |
College of Chemical Engineering,Xiangtan University,Xiangtan 411105,China
2007
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Subjects | |
Online Access | Get full text |
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Summary: | O3; The discrete particle method was used to simulate the distribution of gas holdup in a gas-liquid standard Rushton stirred tank. The gas phase was treated as a large number of bubbles and their trajectories were tracked with the results of motion equations. The two-way approach was performed to couple the interphase momentum exchange. The turbulent dispersion of bubbles with a size distribution was modeled using a stochastic tracking model,and the added mass force was involved to account for the effect of bubble acceleration on the surrounding fluid. The predicted gas holdup distribution showed that this method could give reasonable prediction comparable to the reported experimental data when the effect of turbulence was took into account in modification for drag coefficient. |
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ISSN: | 1004-9541 2210-321X |