Article ID Journal Published Year Pages File Type
9623839 Chemical Engineering Journal 2005 9 Pages PDF
Abstract
A low Reynolds number k-ɛ computational fluid dynamics (CFD) model has been used for the description of flow pattern near the wall. An excellent agreement has been shown between the predicted and experimental hold-up and velocity profiles. The CFD model has been extended for the prediction of heat transfer for two-phase gas-liquid flows in bubble columns. A comparison has been presented between the predicted and the experimental data.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
Authors
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