Intermittent gas-liquid two-phase flow in helically coiled tubes

被引:12
作者
Zhu, Guangyu [1 ]
Yang, Xingtuan [1 ]
Jiang, Shengyao [1 ]
Zhu, Hongye [1 ]
机构
[1] Tsinghua Univ, Key Lab Adv Reactor Engn & Safety, Collaborat Innovat Ctr Adv Nucl Energy Technol, Inst Nucl & New Energy Technol,Minist Educ, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Intermittent flow; Helically coiled tube; Void fraction; Drift flux model; Slug frequency; VOID FRACTION CORRELATIONS; PRESSURE-DROP; SLUG FLOW; STATISTICAL PARAMETERS; PATTERNS;
D O I
10.1016/j.ijmultiphaseflow.2019.04.013
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
This paper experimentally investigated the air-water intermittent flow in four helically coiled tubes with inner diameter of 0.016m, coil diameters of 0.24, 0.43 and 0.80m, and inclination angles of 5 degrees and 15 degrees A double conductivity probe was used to measure the hydrodynamic parameters at 48 points in the outlet cross section. The results showed that centrifugal force and Dean Vortices were the major mechanisms that influenced the void fraction distribution, elongated bubble length, slug length and slug frequency. Because of centrifugal force, the void fraction profile rotated an angle which approached to 90 degrees as liquid superficial velocity increased and coil diameter decreased. Due to the Dean Vortices, the elongated bubble length and slug length decreased as the coil diameter decreased, leading to an increase of slug frequency. A dimensionless parameter Z representing the ratio of the centrifugal force to the gravity was presented, which provides a quantitative criterion to evaluate the influence of centrifugal force. In terms of Z, correlations predicting the deviation angle, elongated bubble length and slug frequency were built, which met the experimental data well when the coil diameter is between 0.24 and 0.80m and the inclination angle between 5 and 15. Moreover, a drift flux model for HCTs was presented. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:113 / 124
页数:12
相关论文
共 27 条
[1]   Experimental study of the hydrodynamic behaviour of slug flow in a horizontal pipe [J].
Abdulkadir, M. ;
Hernandez-Perez, V. ;
Lowndes, I. S. ;
Azzopardi, B. J. ;
Sam-Mbomah, E. .
CHEMICAL ENGINEERING SCIENCE, 2016, 156 :147-161
[2]   VOID DISTRIBUTION IN SLUG FLOW [J].
ANDREUSSI, P ;
BENDIKSEN, KH ;
NYDAL, OJ .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1993, 19 (05) :817-828
[3]   MEASUREMENT AND CORRELATION OF THE PRESSURE-DROP IN AIR-WATER 2-PHASE FLOW IN HORIZONTAL HELICOIDAL PIPES [J].
AWWAD, A ;
XIN, RC ;
DONG, ZF ;
EBADIAN, MA ;
SOLIMAN, HM .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1995, 21 (04) :607-619
[4]   AN EXPERIMENTAL INVESTIGATION OF THE MOTION OF LONG BUBBLES IN INCLINED TUBES [J].
BENDIKSEN, KH .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1984, 10 (04) :467-483
[5]  
Bonnecaze R.H., 1974, AICHE J, V17, P1109
[6]   An experimental study of flow pattern and pressure drop for flow boiling inside microfinned helically coiled tube [J].
Cui, Wenzhi ;
Li, Longjian ;
Xin, Mingdao ;
Jen, Tien-Chien ;
Liao, Quan ;
Chen, Qinghua .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2008, 51 (1-2) :169-175
[7]   PRESSURE-DROP, VOID FRACTION AND SHEAR-STRESS MEASUREMENTS IN AN ADIABATIC 2-PHASE FLOW IN A COILED TUBE [J].
CZOP, V ;
BARBIER, D ;
DONG, S .
NUCLEAR ENGINEERING AND DESIGN, 1994, 149 (1-3) :323-333
[8]   Image processing techniques for high-speed videometry in horizontal two-phase slug flows [J].
do Amaral, C. E. F. ;
Alves, R. F. ;
da Silva, M. J. ;
Arruda, L. V. R. ;
Dorini, L. ;
Morales, R. E. M. ;
Pipa, D. R. .
FLOW MEASUREMENT AND INSTRUMENTATION, 2013, 33 :257-264
[9]   Intermittent flow parameters from void fraction analysis [J].
Fossa, M ;
Guglielmini, G ;
Marchitto, A .
FLOW MEASUREMENT AND INSTRUMENTATION, 2003, 14 (4-5) :161-168
[10]   SINGLE-PHASE AND 2-PHASE FLOW THROUGH HELICALLY COILED TUBES [J].
HART, J ;
ELLENBERGER, J ;
HAMERSMA, PJ .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (04) :775-783