Kinetic theory based computation of PSRI riser: Part I-Estimate of mass transfer coefficient

被引:93
作者
Chalermsinsuwan, Benjapon [2 ,3 ]
Piumsomboon, Pornpote [2 ,3 ]
Gidaspow, Dimitri [1 ]
机构
[1] IIT, Dept Chem & Biol Engn, Chicago, IL 60616 USA
[2] Chulalongkorn Univ, Fuels Res Ctr, Dept Chem Technol, Fac Sci, Bangkok 10330, Thailand
[3] Chulalongkorn Univ, Ctr Excellence Petr Petrochem & Adv Mat, Bangkok 10330, Thailand
关键词
Clusters; Computational fluid dynamics; Fluidization; Hydrodynamics; Multiphase flow; Turbulence; FLUIDIZED-BED RISER; CFD SIMULATION; FCC PARTICLES; SOLID DISPERSION; GAS-FLOW; TURBULENCE; STRESSES; SECTION;
D O I
10.1016/j.ces.2008.11.010
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The PSRI benchmark challenge problem one is modeled using kinetic theory based CFD with the energy minimization multi-scale (EMMS) drag law. These computations give a better comparison than the previous models to measured solids mass flux, solids density and pressure drop. The computer model was also used to calculate axial and radial normal Reynolds stresses, energy spectra, power spectra, granular temperatures, the FCC viscosity and axial and radial dispersion coefficients. The computed cluster sizes agreed with the published empirical correlations. Then, the mass transfer coefficients and the Sherwood numbers are estimated based on particle cluster sizes. The conventional Sherwood number is scaled with the particle cluster diameter. The Sherwood number is the order of 10(-2) and the mass transfer coefficient is the order of 10(-3) m/s. This Sherwood number is two orders of magnitude smaller than the diffusion controlled limit of two based on particle diameter, in agreement with the experimental data for fluidization of fine particles. (c) 2008 Elsevier Ltd. All rights reserved.
引用
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页码:1195 / 1211
页数:17
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