Axial development of air-water annular flow with swirl in a vertical pipe

被引:27
作者
Liu, Wen [1 ,2 ]
Lv, Xiaofei [1 ,2 ]
Bai, Bofeng [2 ]
机构
[1] Changzhou Univ, Jiangsu Key Lab Oil Gas Storage & Transportat Tec, Changzhou 213000, Peoples R China
[2] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
Swirl; Annular flow; Gas-liquid two-phase; Pressure drop; Decay; LIQUID 2-PHASE FLOW; PRESSURE-DROP; HEAT-TRANSFER; GAS; DECAY; FRICTION; SURFACE; TUBES; FILM;
D O I
10.1016/j.ijmultiphaseflow.2019.103165
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Annular flow with swirl induced by a swirler has been widely used in industry. Swirl decay which closely related to working performance and length of the flow is significantly important for its application in industry. Axial development of annular flow with and without swirl has been investigated in this work by means of experimentation and modelling. A vertical pipe system with 11 m long and 62 mm inner diameter was carried out to investigate axial development of flow pattern, void fraction and pressure drop in the annular flow with and without swirl. The experimental results show that a swirling annular flow with swirling streak and less disturbed waves is observed downstream of the swirler. Void fraction decreases, total pressure drop increases and the PDF (probability density function) of pressure drop becomes more concentrated in the annular flow with swirl, compared with these in the annular flow without swirl. However, swirling annular flow is gradually transformed to annular flow without swirl along the stream-wise direction. To qualitatively predict the decay in an annular flow with swirl, a simplified theoretical model was developed here. The results calculated with the theoretical model were in agreements with experimental results. The obtained results can be used in predicting working performance and length of devices, such as separators and heat exchangers. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:16
相关论文
共 43 条
[1]  
Ali A.J., 2003, SPE, V84136, P1
[2]   Interfacial friction in upward annular gas-liquid two-phase flow in pipes [J].
Aliyu, Musa Aliyu ;
Baba, Yahaya Danjuma ;
Lao, Liyun ;
Yeung, Hoi ;
Kim, Kyung Chun .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2017, 84 :90-109
[3]  
[Anonymous], 1964, Trans. ASME J. Heat Transfer
[4]   Experimental study and numerical optimization on a vane-type separator for bubble separation in TMSR [J].
Cai, Baowei ;
Wang, Jianjun ;
Sun, Licheng ;
Zhang, Nana ;
Yan, Changqi .
PROGRESS IN NUCLEAR ENERGY, 2014, 74 :1-13
[5]   Non-linear stability characterization of the thin micropolar liquid film flowing down the inner surface of a rotating vertical cylinder [J].
Chen, Chun-I .
COMMUNICATIONS IN NONLINEAR SCIENCE AND NUMERICAL SIMULATION, 2007, 12 (05) :760-775
[6]   Perturbation analysis to the nonlinear characterization of thin condensate falling stability film on the outer surface of a rotating vertical cylinder [J].
Chen, CI ;
Chen, CK ;
Yang, YT .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2004, 47 (8-9) :1937-1951
[7]  
Falcone G, 2003, SPE
[8]   THE EFFECT OF SWIRL ON THE LIQUID DISTRIBUTION IN ANNULAR 2-PHASE FLOW [J].
FRYER, PJ ;
WHALLEY, PB .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1982, 8 (03) :285-289
[9]   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
[10]   Swirling gas-liquid two-phase flow - Experiment and modeling - Part II: Turbulent quantities and core stability [J].
Gomez, L ;
Mohan, R ;
Shoham, O .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2004, 126 (06) :943-959