Analysis, Comparison, and Discussion on the Utilization of the Existing Slug Liquid Holdup Models to Predict the Horizontal Gas-Liquid Plug-to-Slug Flow Transition

被引:2
|
作者
Boutaghane, Ayoub [1 ]
Arabi, Abderraouf [2 ]
Ibrahim-Rassoul, Nouara [1 ]
Al-sarkhi, Abdelsalam [3 ]
Azzi, Abdelwahid [4 ]
机构
[1] Univ Sci & Technol Houari Boumediene USTHB, Phys Fac, Lab Theoret & Appl Fluid Mech, LMFTA, BP 32 El Alia, Algiers 16111, Algeria
[2] SONATRACH, Direct Cent Rech & Dev, Ave 1er Novembre, Boumerdes 35000, Algeria
[3] King Fahd Univ Petr & Minerals, Dept Mech Engn, Dhahran 31261, Saudi Arabia
[4] Univ Sci & Technol Houari Boumediene USTHB, FGMGP, LTPMP, BP 32 Alia, Algiers 16111, Algeria
关键词
petroleum engineering; petroleum transport/pipelines/ multiphase flow; petroleum wells-drilling/production/construction; INTERMITTENT FLOW; 2-PHASE FLOW; INCLINED PIPES; VOID FRACTION; SUB-REGIMES;
D O I
10.1115/1.4056889
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In horizontal configuration, the gas-liquid intermittent flow can be plug flow or slug flow. Different works have demonstrated that the two flow patterns, despite their similarity, are differents. Thus, it is important to differentiate between them in order to develop more robust predictive models. The limit of the existing model to predict the plug-to-slug flow transition was demonstrated first. After that, 11 existing slug liquid holdup (H-LS) models were used in order to test their potential utilization for predicting the plug-to-slug flow transition. Using H-LS = 0.9 as the criterion to distinguish between the two regimes, the relationship between the superficial velocities of the two phases was generated. The obtained transition lines were compared with visual observations collected from several published works in order to test the predictions of each model, and for different operating conditions. It was concluded in this paper that the slug liquid holdup models can be easily used for this purpose. Meanwhile, the prediction level of each model depends on the pipe diameter and the viscosity of the liquid phase.
引用
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页数:8
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