Particle-to-fluid heat transfer coefficients in miniporous media

被引:54
作者
Jiang, Pei-Xue [1 ]
Xu, Rui-Na [1 ]
Gong, Wei [1 ]
机构
[1] Tsinghua Univ, Dept Thermal Engn, Minist Educ, Key Lab Thermal Sci & Power Engn, Beijing 100084, Peoples R China
关键词
particle-to-fluid heat transfer coefficients; porous media; experiment; numerical simulation;
D O I
10.1016/j.ces.2006.08.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The heat transfer between the solid particles and the fluid in a miniporous media was studied experimentally and numerically. The experimental test section was a sintered bronze porous media with an average particle diameter of 0.2 mm. Particle-to-fluid heat transfer coefficients in the miniporous media were determined experimentally using a transient single-blow technique. A Jumped capacitance method (method 1) was used to calculate the particle-to-fluid heat transfer coefficients from the experimental data. The particle-to-fluid heat transfer coefficients were also calculated from a one-dimensional numerical analysis of the experimental data (method 2) which has been used by many researchers. The experimental results for h(sf) using the two methods agreed very well. Therefore, method I is also deemed acceptable and much simpler than method 2. Three-dimensional numerical simulations using the CFD code FLUENT was also used to predict the particle-to-fluid heat transfer coefficients and to provide details of the fluid flow inside the miniporous media. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:7213 / 7222
页数:10
相关论文
共 29 条
[1]   CFD as a design tool for fixed-bed reactors [J].
Dixon, AG ;
Nijemeisland, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (23) :5246-5254
[2]   Porous materials as open volumetric solar receivers: Experimental determination of thermophysical and heat transfer properties [J].
Fend, T ;
Hoffschmidt, B ;
Pitz-Paal, R ;
Reutter, O ;
Rietbrock, P .
ENERGY, 2004, 29 (5-6) :823-833
[3]  
FUKDADA K, 1990, T JSME B, V56, P2729
[4]   GAS SOLID HEAT-EXCHANGE IN A FIBROUS METALLIC MATERIAL MEASURED BY A HEAT REGENERATOR TECHNIQUE [J].
GOLOMBOK, M ;
JARIWALA, H ;
SHIRVILL, LC .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1990, 33 (02) :243-252
[5]   CFD study on particle-to-fluid heat transfer in fixed bed reactors: Convective heat transfer at low and high pressure [J].
Guardo, A. ;
Coussirat, M. ;
Recasens, F. ;
Larrayoz, M. A. ;
Escaler, X. .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (13) :4341-4353
[6]   Influence of the turbulence model in CFD modeling of wall-to-fluid heat transfer in packed beds [J].
Guardo, A ;
Coussirat, M ;
Larrayoz, MA ;
Recasens, F ;
Egusquiza, E .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (06) :1733-1742
[7]  
Hamaguchi K., 1983, T JPN SOC MECH ENG, V49, P1991
[8]   Measurement of interstitial convective heat transfer and frictional drag for flow across metal foams [J].
Hwang, JJ ;
Hwang, GJ ;
Yeh, RH ;
Chao, CH .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 2002, 124 (01) :120-129
[9]   A new method for evaluation of heat transfer between solid material and fluid in a porous medium [J].
Ichimiya, K .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1999, 121 (04) :978-983
[10]  
Incropera F. P., 1996, FUNDAMENTALS HEAT MA