Filtered models for reacting gas-particle flows

被引:63
作者
Holloway, William [1 ]
Sundaresan, Sankaran [1 ]
机构
[1] Princeton Univ, Dept Chem & Biol Engn, Princeton, NJ 08544 USA
关键词
Reactive flows; Fluidization; Fluid mechanics; Two-fluid model; Gas-solid flow; Multiscale modeling; MASS-TRANSFER MODEL; SOLID RISER FLOWS; SIMULATION; DECOMPOSITION; COEFFICIENTS; COMPUTATION;
D O I
10.1016/j.ces.2012.07.019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Using the kinetic-theory-based two-fluid models as a starting point, we develop filtered two-fluid models for a gas-particle flow in the presence of an isothermal, first-order, solid-catalyzed reaction of a gaseous species. As a consequence of the filtering procedure, terms describing the filtered reaction rate and filtered reactant dispersion need to be constituted in order to close the filtered species balance equation. In this work, a constitutive relation for filtered reaction rate is developed by performing fine-grid, two-fluid model simulations of an isothermal, solid-catalyzed, first-order reaction in a periodic domain. It is observed that the cluster-scale effectiveness factor, defined as the ratio between the reaction rate observed in a fine-grid simulation to that observed in a coarse-grid simulation, can be substantially smaller than unity, and it manifests an inverted bell shape dependence on filtered particle volume fraction in all simulation cases. Moreover, the magnitude of the deviation in the cluster-scale effectiveness factor from unity is a strong function of the meso-scale Thiele modulus and dimensionless filter size. Thus coarse-grid simulations of a reacting gas-particle flow will over-estimate the reaction rate if the cluster-scale effectiveness factor is not accounted for. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:132 / 143
页数:12
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