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Multi-fluid modeling of density segregation in a dense binary fluidized bed 被引量:2
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作者 Zhongxi Chao Yuefa Wang +2 位作者 Jana P. jakobsen Maria Fernandino hugo a. jakobsen 《Particuology》 SCIE EI CAS CSCD 2012年第1期62-71,共10页
This paper presents simulation results of the density segregation in a dense binary gas fluidized bed using a multi-fluid model from Chao et al. (2011), The segregation behavior of two types of particles with approx... This paper presents simulation results of the density segregation in a dense binary gas fluidized bed using a multi-fluid model from Chao et al. (2011), The segregation behavior of two types of particles with approximately same particle diameters and different particle densities was studied and validated using the experimental data from Formisani et al, (2008). Some detailed information regarding the gas, particle velocity profiles, the distributions of the particle volume fractions and the flotsam-to-total par- ticle volume fraction ratios is presented. The simulation results show that the simulated axial average flotsam-to-total particle volume fraction ratio distribution agrees reasonably with the experimental data of Formisani et al. (2008). The binary particle velocities are closely coupled though the segregation exists, The segregation behavior and the particle velocity profiles are superficial gas velocity dependent. The number and distribution of particle velocity vortices change dramatically with superficial gas velocity: at a comparatively low superficial gas velocity, the particles mainly segregate axially, and at a comparatively high superficial gas velocity, the particles segregate both axially and radially. 展开更多
关键词 Fluidized bedBinary flowDensity segregationMulti-fluid modelGranular flow
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化学反应器的模化 多相反应流,第2版,2卷本
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作者 hugo a. jakobsen 陈宏刚 《国外科技新书评介》 2015年第8期21-22,共2页
化学反应器是任何一个化工过程的核心,化学反应器设计的优劣决定着工程建设的成败,化学反应器的设计和模化是化工技术的关键。
关键词 化学反应器 模化 反应流 反应器设计 化工过程 化工技术
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