期刊
CANADIAN JOURNAL OF CHEMICAL ENGINEERING
卷 97, 期 -, 页码 1708-1717出版社
WILEY
DOI: 10.1002/cjce.23421
关键词
CFD-DEM; fluidized bed; drag models; mixing; segregation
资金
- Fundamental Research Funds for Central Universities [2017BSCXA11]
- Postgraduate Research & Practice Innovation Program of Jiangsu Province [KYCX17_1514]
The dense gas-solid fluidized beds with polydisperse particles are commonly encountered in the chemical industry. In this study CFD-DEM simulation of ternary particles in a bubbling fluidized bed were studied to assess four polydisperse drag correlations, using experimental data from Olaofe et al.[1] as the benchmark. The following was shown: (i) the drag force models of Sarkar et al.,[2] Cello et al.,[3] and Rong et al.[4] can correctly predict the minimum fluidization velocity of the mixture of ternary particles, but Gidaspow's model significantly over-predicts this;[5] (ii) no model can accurately predict the experimental segregation degree at different gas velocity, but for the cases that were studied, the models from Cello et al.[3] and Sarkar et al.[2] correlated relatively better with Olaofe et al.'s[1] experimental data than others; and (iii) detailed force analysis found that the collisional force of each type of particles is on average not equal to zero, especially for a system that is strongly segregated. In addition, the differences of drag force for different sizes of particles are the key reason for size segregation rather than pressure gradient force.
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