A rigorous model for the simulation of chemical reaction in gas-particle bubbling fluidized bed: I. Modeling and validation

被引:12
作者
Li, Wenbin [1 ]
Zhang, Yawen [1 ]
Shao, Yuanyuan [1 ]
Zhu, Jesse [1 ,2 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin 300072, Peoples R China
[2] Univ Western Ontario, Dept Chem & Biochem Engn, Particle Technol Res Ctr, London, ON, Canada
关键词
Chemical reaction; Bubbling fluidized bed (BFB); Simulation; Turbulent mass diffusivity; Computational mass transfer; FLOW; HYDRODYNAMICS; TURBULENCE; GASIFIER; REACTORS; DOWNER; RISER;
D O I
10.1016/j.powtec.2017.12.086
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A rigorous model is presented for simulating the gas-particle two phase flow and the involved chemical reaction in bubbling fluidized beds (BFB). The present model employs the recently developed (c(2)) over bar-epsilon(c) closures for the turbulent mass transfer equation, thus enables the prediction of species concentration distributions without relying on empirical turbulent Schmidt number. The Two-Fluid model (TMF) is used to represent the fluid mechanics and the coupled chemical reaction. In mathematical expressions, the k(g) - epsilon(g) - k(p) - epsilon(p) - Theta equations for the description of phases turbulence is adopted. To test the validity of the present model, simulations are conducted for reactive multiphase flow in a BFB. The model predictions show good agreement with the experimental data in literatures. Part II of these serial works will further extend the application of this model to simulating a gas combustion process with strong heat effect in BFB. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:399 / 407
页数:9
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