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CFD simulation of complete drawdown of floating solids in a stirred tank.
- Source :
- Canadian Journal of Chemical Engineering; Jan2015, Vol. 93 Issue 1, p141-149, 9p
- Publication Year :
- 2015
-
Abstract
- Computational fluid dynamics (CFD) simulations were carried out to find a CFD methodology to predict the critical impeller speed ( N<subscript> CS</subscript>) for the complete drawdown of floating solids in a stirred tank with an up- and down-pumping pitched blade turbine (PBTU and PBTD). CFD models along with six mixing parameters predicted that N<subscript> CS</subscript> was 7.5 rps and 5.8 rps, respectively, for PBTU and PBTD, when impeller submergence ( S) was equal to half of the liquid height ( H/2). Reasonable agreement was observed between CFD simulations and published empirical correlation. N<subscript> CS</subscript> was smaller for PBTD relative to PBTU at S = H/2, which agreed with results in the literature. The drawdown mechanisms based on the mean drag, turbulent fluctuations or large scale eddies failed to explain the difference in N<subscript> CS</subscript> between PBTU and PBTD. The flow patterns based on a simulated velocity field were further investigated and successfully accounted for this difference. [ABSTRACT FROM AUTHOR]
Details
- Language :
- English
- ISSN :
- 00084034
- Volume :
- 93
- Issue :
- 1
- Database :
- Complementary Index
- Journal :
- Canadian Journal of Chemical Engineering
- Publication Type :
- Academic Journal
- Accession number :
- 99778332
- Full Text :
- https://doi.org/10.1002/cjce.22097