CFD simulation of transient gas to particle heat transfer for fluidized and spouted regimes

被引:37
作者
Fattahi, Mohsen [1 ]
Hosseini, Seyyed Hossein [2 ]
Ahmadi, Goodarz [3 ]
机构
[1] Univ Kurdistan, Dept Chem Engn, Fac Engn, Sanandaj 66177, Iran
[2] Ilam Univ, Dept Chem Engn, Ilam 69315516, Iran
[3] Clarkson Univ, Dept Mech & Aeronaut Engn, Potsdam, NY 13699 USA
关键词
CFD; Spouted bed; Transient heat transfer; Temperature distribution; Fluidized regime; EULER-LAGRANGE APPROACH; GRANULAR FLOW; KINETIC-THEORY; SOLID FLOW; DISCRETE ELEMENT; DEM SIMULATION; BED REACTOR; DYNAMICS; TUBE; HYDRODYNAMICS;
D O I
10.1016/j.applthermaleng.2015.05.071
中图分类号
O414.1 [热力学];
学科分类号
摘要
The transient gas to particle heat transfer for fluidized and spouted regimes was studied using a Eulerian Eulerian two-fluid model (TFM) in conjunction with the kinetic theory of granular flows (KTGF). The inlet gas temperature was transient which increased with time. Effect of modelling parameter of specularity coefficient on the simulation results was studied. It was found that specularity coefficient is a critical parameter which affects on the particles behaviour and the value of 0.025 leads to creation of incoherent spouting similar to the measurements. The temporal variation of particles concentration and temperature distribution in the spouted and fluidized regimes were compared with the corresponding experimental data for three distinct regions of spout, fountain and annulus. It was shown that the CFD model predicted the particles distribution properly for both regimes. In addition, the CFD predictions for particle temperature distribution for the spouted regime were in a better agreement with the measurements, when compared with that for the fluidized regime. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:385 / 396
页数:12
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[1]   Modeling oxy-fuel combustion in a 3D circulating fluidized bed using the hybrid Euler-Lagrange approach [J].
Adamczyk, Wojciech P. ;
Kozolub, Pawel ;
Wecel, Gabriel ;
Klimanek, Adam ;
Bialecki, Ryszard A. ;
Czakiert, Tomasz .
APPLIED THERMAL ENGINEERING, 2014, 71 (01) :266-275
[2]   Modeling of particle transport and combustion phenomena in a large-scale circulating fluidized bed boiler using a hybrid Euler-Lagrange approach [J].
Adamczyk, Wojciech P. ;
Wecel, Gabriel ;
Klajny, Marcin ;
Kozolub, Pawel ;
Klimanek, Adam ;
Bialecki, Ryszard A. .
PARTICUOLOGY, 2014, 16 :29-40
[3]   Catalytic cracking of gas oils in electromagnetic fields: reactor design and performance [J].
Al-Mayman, SI ;
Al-Zahrani, SM .
FUEL PROCESSING TECHNOLOGY, 2003, 80 (02) :169-182
[4]   Study of wall-to-bed heat transfer in a bubbling fluidised bed using the kinetic theory of granular flow [J].
Armstrong, L. M. ;
Gu, S. ;
Luo, K. H. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2010, 53 (21-22) :4949-4959
[5]   CFD modeling of a spouted bed with a porous draft tube [J].
Azizi, Salar ;
Hosseini, Seyyed Hossein ;
Moraveji, M. ;
Ahmadi, Goodarz .
PARTICUOLOGY, 2010, 8 (05) :415-424
[6]   CFD modeling of hydrodynamic and heat transfer in fluidized bed reactors [J].
Behjat, Yaghoub ;
Shahhosseini, Shahrokh ;
Hashemabadi, S. Hassan .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2008, 35 (03) :357-368
[7]  
Brown S.W., 2012, Honors College, V41
[8]   Transient gas-to-particle heat transfer measurements in a spouted bed [J].
Brown, Steven L. ;
Lattimer, Brian Y. .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2013, 44 :883-892
[9]   CFD simulation of hydrodynamics and heat transfer in gas phase ethylene polymerization reactors [J].
Dehnavi, Mohammad A. ;
Shahhosseini, Shahrokh ;
Hashemabadi, S. Hassan ;
Ghafelebashi, S. Mehdi .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2010, 37 (04) :437-442
[10]   Effect of tube shape on the hydrodynamics and tube-to-bed heat transfer in fluidized beds [J].
Dong, N. H. ;
Armstrong, L. M. ;
Gu, S. ;
Luo, K. H. .
APPLIED THERMAL ENGINEERING, 2013, 60 (1-2) :472-479