Empirical Modelization of Intermittent Gas/Liquid Flow Hydrodynamic Parameters: The Importance of Distinguishing between Plug and Slug Flows

被引:19
作者
Arabi, A. [1 ,2 ]
Azzi, A. [2 ]
Kadi, R. [1 ]
Al-Sarkhi, A. [3 ]
Hewakandamby, B. [4 ]
机构
[1] SONATRACH, Direct Cent Rech & Dev, Hydra, Algeria
[2] Univ Sci & Technol Houari Boumediene USTHB, Bab Ezzouar, Algeria
[3] King Fahd Univ Petr & Minerals, Dhahran, Saudi Arabia
[4] Univ Nottingham, Nottingham, England
来源
SPE PRODUCTION & OPERATIONS | 2021年 / 36卷 / 03期
关键词
GAS-LIQUID FLOW; 2-PHASE FLOW; VOID FRACTION; PRESSURE-DROP; LONG BUBBLES; MULTIPHASE FLOW; INCLINED PIPES; TRANSITION; FREQUENCY; PREDICTION;
D O I
10.2118/205481-PA
中图分类号
TE [石油、天然气工业];
学科分类号
0820 ;
摘要
Intermittent flow is one of the most complex flow regimes in horizontal pipes. Various studies have classified this regime as two distinct subregimes: plug and slug flow. This classification has been made based on flow observations. In this work, the behavior of several flow parameters that characterize plug and slug flow are presented. Data from eight published works in the open literature were collected and studied to explain the behavior of both regimes. These data include pressure drop, void fraction, and slug frequency, as well as the lengths of liquid slugs and elongated bubbles for slug and plug regimes. It is observed from the evolution and analysis of these parameters that plug and slug flows have several different distinct features and should be considered as two separate regimes for the empirical modelization of the hydrodynamic parameters. The mixture Froude number, and to a lesser extent the liquid superficial velocity to gas superficial velocity ratio, seem to have significant impacts on the plug-to-slug flow transition.
引用
收藏
页码:703 / 720
页数:18
相关论文
共 105 条
[71]   Advanced simulation of transient multiphase flow & flow assurance in the oil & gas industry [J].
Lakehal, Djamel .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2013, 91 (07) :1201-1214
[72]  
Lamari M. L., 2001, THESIS CARLETON U OT
[73]  
Le Prin K., 2019, OFFSH TECHN C HOUST, DOI [10.4043/29306-MS, DOI 10.4043/29306-MS]
[74]   Frictional pressure drop analysis for horizontal and vertical air-water two-phase flows in different pipe sizes [J].
Lu, Cihang ;
Kong, Ran ;
Qiao, Shouxu ;
Larimer, Joshua ;
Kim, Seungjin ;
Bajorek, Stephen ;
Tien, Kirk ;
Hoxie, Chris .
NUCLEAR ENGINEERING AND DESIGN, 2018, 332 :147-161
[75]  
Mandhane J. M., 1974, International Journal of Multiphase Flow, V1, P537, DOI 10.1016/0301-9322(74)90006-8
[76]  
Netto JRF, 1999, INT J MULTIPHAS FLOW, V25, P1129, DOI 10.1016/S0301-9322(99)00041-5
[77]  
Norris L., 1982, CORRELATION PRUDHOE
[78]   Experimental validation of a simple model for gas-liquid slug flow in horizontal pipes [J].
Orell, A .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (05) :1371-1381
[79]   Do huge waves exist in horizontal gas-liquid pipe flow? [J].
Parsi, Mazdak ;
Azzopardi, Barry J. ;
Al-Sarkhi, Abdelsalam ;
Kesana, Netaji R. ;
Vieira, Ronald E. ;
Torres, Carlos F. ;
McLaury, Brenton S. ;
Shirazi, Siamack A. ;
Schleicher, Eckhard ;
Hampel, Uwe .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2017, 96 :1-23
[80]   Elongated bubble centring in horizontal gas-liquid slug flow [J].
Perkins, Sean J. ;
Li, Huazhou A. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2020, 123