CFD-based analysis of the wall effect on the pressure drop in packed beds with moderate tube/particle diameter ratios in the laminar flow regime

被引:144
作者
Atmakidis, Theodoros [1 ]
Kenig, Eugeny Y. [1 ]
机构
[1] Univ Paderborn, Fac Mech Engn, D-33098 Paderborn, Germany
关键词
Packed beds; Pressure drop; CFD; Channeling effect; EXPERIMENTAL VALIDATION; REACTORS; PROFILES;
D O I
10.1016/j.cej.2009.07.057
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this work, the influence of the confining walls on pressure drop in packed beds is studied numerically for moderate tube/particle diameter ratios. Two different configuration types are investigated, a regular type and an irregular one. The regular configurations follow the atomic body-centered cubic and face-centered cubic structure in ideal crystals, whereas themodifiedballistic depositionmethodis employed to generate the irregular configurations. To validate the simulation results, four experimental pressure drop correlations are used, namely by Ergun (1952) [1], by Carman (1937) [2], by Zhavoronkov et al. (1949) [3] and by Reichelt (1972) [4]. Simulation results for the regular configurations are in a good agreement with the Carman correlation. For the irregular configurations, which are closer to real packed beds, agreement with the correlations of Zhavoronkov et al. (1949) [3] and Reichelt (1972) [4] is better. This is explained by the fact that the latter two correlations take the wall effect into account. CFD simulations provide useful data on the flow field inside packed beds which can be used for the improvement and further optimization of the design and operation of packed bed reactors. (C) 2009 Elsevier B. V. All rights reserved.
引用
收藏
页码:404 / 410
页数:7
相关论文
共 20 条
[1]  
ARAIZA COC, 2008, INT J CHEM REACT ENG, V6, pA1
[2]   Fluid flow through catalyst filled tubes [J].
Bey, O ;
Eigenberger, G .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (08) :1365-1376
[3]   CFD modelling and experimental validation of pressure drop and flow profile in a novel structured catalytic reactor packing [J].
Calis, HPA ;
Nijenhuis, J ;
Paikert, BC ;
Dautzenberg, FM ;
van den Bleek, CM .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (04) :1713-1720
[4]  
Carmen P. E., 1937, AIChE, V15, P150, DOI DOI 10.1016/S0263-8762(97)80003-2
[5]  
COEHLO D, 1997, PHYS REV E, V55, P1959
[6]   Voidage variation in packed beds at small column to particle diameter ratio [J].
de Klerk, A .
AICHE JOURNAL, 2003, 49 (08) :2022-2029
[7]   CFD as a design tool for fixed-bed reactors [J].
Dixon, AG ;
Nijemeisland, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (23) :5246-5254
[8]   The influence of confining walls on the pressure drop in packed beds [J].
Eisfeld, B ;
Schnitzlein, K .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (14) :4321-4329
[9]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89
[10]   Numerical simulations of single phase reacting flows in randomly packed fixed-bed reactors and experimental validation [J].
Freund, H ;
Zeiser, T ;
Huber, F ;
Klemm, E ;
Brenner, G ;
Durst, F ;
Emig, G .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (3-6) :903-910