An Approach for Drag Correction Based on the Local Heterogeneity for Gas-Solid Flows

被引:51
作者
Li, Tingwen [1 ,2 ]
Wang, Limin [3 ]
Rogers, William [1 ]
Zhou, Guofeng [3 ]
Ge, Wei [3 ]
机构
[1] US DOE, Natl Energy Technol Lab, Morgantown, WV 26505 USA
[2] AECOM, Morgantown, WV 26505 USA
[3] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
基金
中国国家自然科学基金;
关键词
computational fluid dynamics; gas-solid flow; drag model; direct numerical simulation; heterogeneous structure; sub-grid model; DIRECT NUMERICAL-SIMULATION; STRUCTURE-DEPENDENT DRAG; FLUIDIZED-BEDS; CFD SIMULATION; MODEL; SYSTEMS; SPHERES;
D O I
10.1002/aic.15507
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The drag models typically used for gas-solids interaction are mainly developed based on homogeneous systems of flow passing fixed particle assembly. It has been shown that the heterogeneous structures, i.e., clusters and bubbles in fluidized beds, need to be resolved to account for their effect in the numerical simulations. Since the heterogeneity is essentially captured through the local concentration gradient in the computational cells, this study proposes a simple approach to account for the non-uniformity of solids spatial distribution inside a computational cell and its effect on the interaction between gas and solid phases. To validate this approach, the predicted drag coefficient has been compared to the results from direct numerical simulations. In addition, the need to account for this type of heterogeneity is discussed for a periodic riser flow simulation with highly resolved numerical grids and the impact of the proposed correction for drag is demonstrated. (C) 2016 American Institute of Chemical Engineers AIChE J, 63: 1203-1212, 2017
引用
收藏
页码:1203 / 1212
页数:10
相关论文
共 36 条
[1]   The role of meso-scale structures in rapid gas-solid flows [J].
Agrawal, K ;
Loezos, PN ;
Syamlal, M ;
Sundaresan, S .
JOURNAL OF FLUID MECHANICS, 2001, 445 :151-185
[2]  
Benyahia S., 2012, Summary of MFIX Equations 2012-1
[3]  
Box PO, 2005, J FLUID MECH, V528, P233
[4]   Grid independence behaviour of fluidized bed reactor simulations using the Two Fluid Model: Effect of particle size [J].
Cloete, Schalk ;
Johansen, Stein Tore ;
Amini, Shahriar .
POWDER TECHNOLOGY, 2015, 269 :153-165
[5]   Review of discrete particle modeling of fluidized beds [J].
Deen, N. G. ;
Annaland, M. Van Sint ;
Van der Hoef, M. A. ;
Kuipers, J. A. M. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :28-44
[6]  
Fan L.-S., 2005, PRINCIPLES GAS SOLID, P557
[7]   Quantitative Assessment of Fine-Grid Kinetic-Theory-Based Predictions of Mean-Slip in Unbounded Fluidization [J].
Fullmer, William D. ;
Hrenya, Christine M. .
AICHE JOURNAL, 2016, 62 (01) :11-17
[8]   Physical mapping of fluidization regimes - the EMMS approach [J].
Ge, W ;
Li, JH .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (18) :3993-4004
[9]  
Ge W., 2008, 9 INT C CIRCULATING
[10]  
Gidaspow D., 1994, MULTIPHASE FLOW FLUI, P467