Experimental study of swirling flow pneumatic liquid-carrying characteristics in the vortex tool inserted tube under liquid loading conditions

被引:3
作者
Zhang, Zhao [1 ]
Liu, Jie [2 ]
Liao, Ruiquan [2 ]
Cheng, Fushan [3 ]
机构
[1] Guangdong Univ Petrochem Technol, Sch Petr Engn, Maoming 525000, Peoples R China
[2] Yangtze Univ, Sch Petr Engn, Wuhan 430100, Peoples R China
[3] PetroChina Xinjiang Oilfield Co, Karamay 834000, Peoples R China
关键词
Vortex tool; Gas; liquid swirling flow; Flow pattern; Pressure drop; Friction factor; PRESSURE-DROP; 2-PHASE FLOW; MECHANISTIC MODEL; CONVEYING SYSTEM; ANNULAR-FLOW; PATTERNS; CHURN; DECAY;
D O I
10.1016/j.expthermflusci.2023.110954
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid unloading by vortex tool is one of the most important applications of swirling flow pneumatic conveying. However, due to swirl decay, the evolution of gas-liquid flow patterns and the dynamic characteristics of pressure drop downstream of the vortex tool are much more complex than those in non-swirling flow. In this study, the gas-liquid flow patterns and pressure drop inside the vortex tool inserted tube (ID = 60 mm) under liquid loading conditions were experimentally studied and compared with those of the plain tube. With the superficial gas velocities ranging from 0.5 to 6.0 m/s and superficial liquid velocities of 0.01, 0.02, and 0.04 m/s, the effects of the structural parameters and stages of vortex tools on the pressure drop were discussed. The experimental results reveal that three distinct swirling flow patterns can be identified downstream of the vortex tool, namely swirling gas column flow, swirling churn flow and swirling annular flow. The insertion of vortex tool facilitates an earlier transition of the churn flow to the annular flow, and the induced swirling flow can restrain the liquid from falling back. The helix angle of the corkscrew deflector has a more significant effect on the pressure drop than its length. By reducing the helix angle from 54 degrees to 45 degrees, the total pressure drop and downstream pressure gradient are significantly decreased, even lower than those of the plain tube. But the series combination of 54 degrees and 45 degrees vortex tools results in a significant increase in the downstream pressure gradient. Additionally, at low gas flow rate, negative frictional pressure drop occurs in both plain tube and vortex tool inserted tube. Hence, the new friction factor correlations were established respectively for the positive and negative friction regions in the cases of the tube with and without vortex tool, and most of the frictional pressure gradient predictions are within an error band less than 20%.
引用
收藏
页数:11
相关论文
共 45 条
[1]   Positive frictional pressure gradient in vertical gas-high viscosity oil slug flow [J].
Al-Sarkhi, A. ;
Pereyra, E. ;
Sarica, C. ;
Alruhaimani, E. .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2016, 59 :50-61
[2]   Investigation of a new tool to unload liquids from stripper gas wells [J].
Ali, AJ ;
Scott, SL ;
Fehn, B .
SPE PRODUCTION & FACILITIES, 2005, 20 (04) :306-316
[3]   STUDY OF 2-PHASE FLOW IN INCLINED PIPES [J].
BEGGS, HD ;
BRILL, JP .
JOURNAL OF PETROLEUM TECHNOLOGY, 1973, 25 (MAY) :607-617
[4]  
[陈德春 Chen Dechun], 2015, [天然气地球科学, Natural Gas Geoscience], V26, P2137
[5]  
David A., 2003, ROCKY MOUNTAIN OIL J, V83, P4
[6]   Comparison between rotation swirler and non-rotation swirler in a horizontal swirling flow pneumatic conveying [J].
Dong, Lin ;
Rinoshika, Akira .
POWDER TECHNOLOGY, 2019, 346 :396-402
[7]  
Falcone G., 2003, SPE ANN TECHN C EXH
[8]   Interfacial and wall friction factors of swirling annular flow in a vertical pipe [J].
Funahashi, H. ;
Kirkland, K. Vierow ;
Hayashi, K. ;
Hosokawa, S. ;
Tomiyama, A. .
NUCLEAR ENGINEERING AND DESIGN, 2018, 330 :97-105
[9]   Unified mechanistic model for steady-state two-phase flow: Horizontal to vertical upward flow [J].
Gomez, LE ;
Shoham, O ;
Schmidt, Z ;
Chokshi, RN ;
Northug, T .
SPE JOURNAL, 2000, 5 (03) :339-350
[10]   The effect of pipe diameter on the structure of gas/liquid flow in vertical pipes [J].
Kaji, R. ;
Azzopardi, B. J. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2010, 36 (04) :303-313