Review of direct numerical simulation of fluid-particle mass, momentum and heat transfer in dense gas-solid flows

被引：149

作者：

Deen, Niels G. ^{[1
]}

Peters, E. A. J. F. ^{[1
]}

Padding, Johan T. ^{[1
]}

Kuipers, J. A. M. ^{[1
]}

机构：

[1] Eindhoven Univ Technol, Dept Chem Engn & Chem, Multiphase Reactors Grp, NL-5600 MB Eindhoven, Netherlands

来源：

CHEMICAL ENGINEERING SCIENCE | 2014年 / 116卷

基金：

欧洲研究理事会;

关键词：

Direct numerical simulation; Immersed boundary method; Fluidization; Fluid-particle momentum; mass and heat transfer; Multi-scale modeling; IMMERSED BOUNDARY METHOD; FICTITIOUS DOMAIN METHOD; FINITE-VOLUME METHOD; MULTISCALE MODELING STRATEGY; PARTICULATE FLOWS; COMPLEX GEOMETRIES; CFD SIMULATIONS; REYNOLDS-NUMBER; PACKED-BEDS; DRAG FORCE;

D O I：

10.1016/j.ces.2014.05.039

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

This paper reviews the use of direct numerical simulation (DNS) models for the study of mass, momentum and heat transfer phenomena prevailing in dense gas-solid flows. In particular, we consider the DNS models as the first important step in a multiscale modeling strategy. Both the merits and the limitations of different DNS methods are discussed, in particular for the field of fluidized bed modeling. The importance of the closures for interfacial transfer of mass, momentum and heat, obtained from DNS and applied in coarser scale models, is demonstrated with illustrative examples. Finally, we present our view on required future developments of DNS models for the investigation of various chemical engineering problems. (C) 2014 Elsevier Ltd. All rights reserved.

引用

页码：710 / 724

页数：15

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