Prediction of Turbulent-Turbulent Stratified Gas-Liquid Flow in Horizontal Pipe Using CFD-Generated Specified Shear Wall Method

被引:1
作者
Zheng, Ping [1 ]
Zhao, Liang [2 ]
Chen, Xu [1 ]
机构
[1] Liaoning Shihua Univ, Coll Petr Engn, Fushun, Liaoning, Peoples R China
[2] Sichuan Univ, Coll Water Resource & Hydropower, State Key Lab Hydraul & Mt River Engn, Chengdu, Sichuan, Peoples R China
基金
中国国家自然科学基金;
关键词
Stratified Gas-Liquid Flow; CFD Modeling; Specified Shear Wall Method; Shear Stress; Friction Factor; PRESSURE-DROP; 2-PHASE FLOW; MODEL; STRESS; TRANSITION;
D O I
10.1252/jcej.17we236
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The prediction of interface shear stress is one of the great challenges of stratified gas-liquid flow in a horizontal pipe. In this work, a new method is proposed to predict interface shear stress, in which the gas-liquid interface is regarded as a flat specified shear wall (SSW). The gas flow is numerically simulated under the same conditions as those in Strand's experiments, the gas-wall and interface shear stress correlations are then modified, and a new Kowalski-type equation of liquid-wall shear stress is presented. Different models are adopted to obtain the gas flow velocity and gas-wall, interface, and liquid-wall shear stresses, and the results are compared with the experimental data and analyzed. The results show that the gas-wall shear stress is well predicted by the SSW k-omega model, the interface shear stress is well predicted by the SSW k-epsilon model, and the liquid-wall shear stress is well predicted by both the two-fluid model and the Kowalski-type equation. The predictions of liquid holdup and pressure drop of the SSW method improved and agreed better with the experimental data when the gas Reynolds numbers were 9000 <= Re-G <= 50000 and the liquid Reynolds numbers were 15000 <= Re-L <= 30000.
引用
收藏
页码:8 / 18
页数:11
相关论文
共 32 条
[1]   STATISTICAL-ANALYSIS OF WAVES IN HORIZONTAL STRATIFIED GAS-LIQUID FLOW [J].
ANDRITSOS, N .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1992, 18 (03) :465-473
[2]   A PIV investigation of stratified gas-liquid flow in a horizontal pipe [J].
Ayati, A. A. ;
Kolaas, J. ;
Jensen, A. ;
Johnson, G. W. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2014, 61 :129-143
[3]   VALIDATION OF A ONE-DIMENSIONAL WAVE MODEL FOR THE STRATIFIED-TO-SLUG FLOW REGIME TRANSITION, WITH CONSEQUENCES FOR WAVE GROWTH AND SLUG FREQUENCY [J].
CROWLEY, CJ ;
WALLIS, GB ;
BARRY, JJ .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1992, 18 (02) :249-271
[4]   Modelling of stratified gas-liquid two-phase flow in horizontal circular pipes [J].
de Sampaio, Paulo A. B. ;
Faccini, Jose L. H. ;
Su, Jian .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2008, 51 (11-12) :2752-2761
[5]  
Fluent A, 2011, Ansys fluent theory guide, V15317, P724
[6]  
Hand N. P, 1991, GAS LIQUID COCURRENT
[7]   LIQUID HOLD-UP, PRESSURE-DROP, AND VELOCITY PROFILES IN STEADY UNIFORM STRATIFIED FLOW [J].
HANSEN, EA ;
VESTED, HJ .
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 1991, 113 (02) :87-93
[8]   CORRELATIONS PREDICTING FRICTIONAL PRESSURE-DROP AND LIQUID HOLDUP DURING HORIZONTAL GAS-LIQUID PIPE-FLOW WITH A SMALL LIQUID HOLDUP [J].
HART, J ;
HAMERSMA, PJ ;
FORTUIN, JMH .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1989, 15 (06) :947-964
[9]   PREDICTION OF TURBULENT, STRATIFIED, 2-PHASE FLOW IN INCLINED PIPES AND CHANNELS [J].
ISSA, RI .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1988, 14 (02) :141-154
[10]   THE RELATION BETWEEN THE INTERFACIAL SHEAR-STRESS AND THE WAVE MOTION IN A STRATIFIED FLOW [J].
KANG, HC ;
KIM, MH .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1993, 19 (01) :35-49