Numerical simulation and analysis of gas flow field in serrated valve column

被引:19
作者
Wang Lianghua [1 ]
Cui Juejian [1 ]
Yao Kejian [1 ]
机构
[1] Zhejiang Univ Technol, Coll Chem Engn & Mat Sci, State Key Lab Breeding Base Green Chem Synth Tech, Hangzhou 310032, Zhejiang, Peoples R China
关键词
serrated valve; numerical simulation; pressure drop; RNG k-epsilon turbulent model;
D O I
10.1016/S1004-9541(08)60118-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A three-dimensional computational fluid dynamics (CFD) model for gas flow through a serrated valve tray was presented. The flow field, as well as the dry-pressure drop of the valve under the full-opening condition was simulated based on the proposed model by using FLUENT 6.0 software. Compared with the values of dry-pressure drop in different turbulent models, the simulated results using RNG k-epsilon model are in reasonable agreement with experimental data, indicating that RNG k-epsilon model is suitable in simulating gas flow through the serrated valve tray. Then the CFD model combining RNG k-epsilon model was used to study the three-dimensional gas flow through the considered serrated valve tray. The simulated results showed that various eddies existed on the serrated valve tray, and both the eddy and the non-eddy areas were nearly equal. The existence of addendum can decrease the eddy area caused by gas passing through the lateral outlet slots. The size of eddies can be reduced by optimizing the distance between valves.
引用
收藏
页码:541 / 546
页数:6
相关论文
共 33 条
[1]  
BILLET R, 1992, ICHEME S SERIES, pA361
[2]  
BILLET R, 1969, BRIT CHEM ENG, V14, P489
[3]   Dynamics of gas-liquid flow in a rectangular bubble column: experiments and single/multi-group CFD simulations [J].
Buwa, VV ;
Ranade, VV .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (22-23) :4715-4736
[4]  
CHENG F, 1995, PETROCHEMICAL TECHNO, V24, P118
[5]   Large eddy simulation of the gas-liquid flow in a square cross-sectioned bubble column [J].
Deen, NG ;
Solberg, T ;
Hjertager, BH .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (21-22) :6341-6349
[6]   A three-dimensional CFD model for gas-liquid bubble columns [J].
Delnoij, E ;
Kuipers, JAM ;
van Swaaij, WPM .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) :2217-2226
[7]  
*FLUENT INC, 2003, FLUENT 6 0 US GUID
[8]  
GESIT G, 2004, THESIS EDMONTON
[9]  
KISTER HZ, 1992, DISTILLATION DESIGN, P382
[10]  
LAUNDER BE, 1974, COMPUT METHODS APPL, V3, P289