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Comparative analysis of particle density effects on initial fluidization in gas-solid fluidized beds

摘要:Gas-solids fluidization technology is commonly used in chemical engineering processes involving high-density particles, often encountering poor defluidization phenomena. However, there is limited research examining the applicability of flow characteristics and empirical correlations established for low-density, easily fluidizable particles in guiding the flow behavior of high-density particles. This knowledge gap poses significant challenges for designing and operating fluidized beds in relevant processes involving high-density particles. This study comprehensively evaluates the effect of particle density on hydrodynamics during the initial fluidization stage using experimental, empirical correlations and simulation methods. Results of preliminary experiments indicate that empirical correlations for predicting Umf may exhibit significant errors of high-density particles. However, the experiments face challenges in eliminating the influence of different particle size distribution. In contrast, the simulation results present a high consistency with the experiments after sensitivity analysis. Further simulation results illustrate that empirical correlations for Umf may only yield relatively accurate predictions within the narrow density range. As the particle density increases, the predicted errors tend to increase. During the initial fluidization stage, three distinct fluidization stages can be observed, as revealed by both experiments and simulations. These stages can be attributed to the practical particle size distribution. Furthermore, it is noted that as the particle density increases, the fluidization performance tends to deteriorate. This study endeavors to advance the understanding of the effect of particle density on hydrodynamics during the initial fluidization stage. Nonetheless, more studies are still needed to enhance and deepen the current knowledge of the fluidization of high-density particles. ? 2023 Elsevier B.V.

ISSN号:1385-8947

卷、期、页:卷477

发表日期:2023-12-01

影响因子:15.100000

期刊分区(SCI为中科院分区):一区

收录情况:SCI(科学引文索引印刷版),EI(工程索引),SCIE(科学引文索引网络版)

发表期刊名称:Chemical Engineering Journal

参与作者:王欢

第一作者:李舒月,张永民

论文类型:期刊论文

论文概要:李舒月,张永民,王欢,Comparative analysis of particle density effects on initial fluidization in gas-solid fluidized beds,Chemical Engineering Journal,2023,卷477

论文题目:Comparative analysis of particle density effects on initial fluidization in gas-solid fluidized beds

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