Prediction of entrained droplet fraction in co-current annular gas-liquid flow in vertical pipes

被引:34
作者
Aliyu, Aliyu M. [1 ]
Almabrok, Almabrok A. [2 ]
Baba, Yahaya D. [3 ]
Archibong, Archibong-Eso [4 ]
Lao, Liyun [4 ]
Yeung, Hoi [4 ]
Kim, Kyung Chun [1 ]
机构
[1] Pusan Natl Univ, Sch Mech Engn, Busan 609735, South Korea
[2] Sirte Univ, Fac Engn, Dept Petr Engn, Sirte, Libya
[3] Afe Babalola Univ, Dept Chem & Petr Engn, PMB 5454, Ado Ekiti, Nigeria
[4] Cranfield Univ, Oil & Gas Engn Ctr, Cranfield MK43 0AL, Beds, England
基金
新加坡国家研究基金会;
关键词
Droplet entrainment; Large diameter pipes; Two-phase flow; Sauter mean diameter; Wire Mesh Sensor; 2-PHASE FLOW; MODEL; PHASE; DIAMETER; TRANSITIONS; DEPOSITION; STEADY; WAVES; ONSET; RATES;
D O I
10.1016/j.expthermflusci.2017.03.012
中图分类号
O414.1 [热力学];
学科分类号
摘要
The entrained droplet fraction is an important parameter in annular two-phase flow, as its correlations are key inputs in flow simulation codes for the prediction of pressure drop and critical heat flux or dryout. Investigators have stressed the importance of extending the validity range of current correlations so that more conditions are covered. This could be achieved for example by including fluids with higher viscosities, a wider range of operating pressures, and increase in the size of pipes used for experiments (most of the data in the literature are from pipes of 50 mm diameter and below). In attempt to improve the latter, experiments were conducted in a 101.6 mm gas liquid flow loop at Cranfield University's Oil and Gas Engineering Laboratory and data on the fraction of droplets were collected in the annular flow regime by measuring the film velocity, from which the droplet fraction was calculated. Comparison of the film velocity by this method and by a mass balance showed close agreement. A capacitance Wire Mesh Sensor was used for flow visualisation in order to distinguish between annular and churn flow. In order to arrive at an improved correlation, over 1300 data points were gathered from other published works. These include air water studies where large pipes of up to 127 mm in diameter were used. The others were from small-diameter pipes and for refrigerant, steam water, air water, and air glycerine flows. Since in the annular regime, the gas flow entrains liquid droplets into the core, their presence alters the properties of the gas core. Therefore, accurate predictions are pivotal for the energy efficient design and operation of facilities in the petroleum and nuclear power industry. The correlation obtained here showed good agreement with the collected databank. (C) 2017 Elsevier Inc. All rights reserved.
引用
收藏
页码:287 / 304
页数:18
相关论文
共 50 条
  • [41] Hydrodynamics of gas-liquid slug flow along vertical pipes in turbulent regime - An experimental study
    Mayor, T. S.
    Ferreira, V.
    Pinto, A. M. F. R.
    Campos, J. B. L. M.
    [J]. INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2008, 29 (04) : 1039 - 1053
  • [42] Prediction of mono-disperse gas-liquid turbulent flow in a vertical pipe
    Islam, A. S. M. Atiqul
    Adoo, N. A.
    Bergstrom, D. J.
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2016, 85 : 236 - 244
  • [43] Flow pattern transition and void fraction prediction of gas-liquid flow in helically coiled tubes
    Liu, Li
    Zhang, Jiarong
    Hu, Bing
    Dai, Juntao
    Wang, Ke
    Gu, Hanyang
    [J]. CHEMICAL ENGINEERING SCIENCE, 2022, 258
  • [44] Dynamics of a finite-width liquid film in a co-current microchannel gas flow
    M. V. Bartashevich
    O. A. Kabov
    V. V. Kuznetsov
    [J]. Fluid Dynamics, 2010, 45 : 924 - 929
  • [45] Dynamics of a Finite-Width Liquid Film in a Co-Current Microchannel Gas Flow
    Bartashevich, M. V.
    Kabov, O. A.
    Kuznetsov, V. V.
    [J]. FLUID DYNAMICS, 2010, 45 (06) : 924 - 929
  • [46] An optimize empirical correlations for liquid film thickness and interfacial friction factor in vertical gas-liquid annular flow
    Ghafouri, Arash
    Ghafouri, Ashkan
    Kosarineia, Abbas
    Daneh-Dezfuli, Alireza
    [J]. JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2023, 148
  • [47] Transition to entrainment in downward annular gas-liquid flow: Study through flow control
    Cherdantsev, Andrey
    Isaenkov, Sergey
    Markovich, Dmitry
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2025, 184
  • [48] Experimental Study of Vertical Gas-Liquid Pipe Flow for Annular and Liquid Loading Conditions using Dual Wire-Mesh Sensors
    Vieira, R. E.
    Parsi, M.
    Torres, C. F.
    Shirazi, S. A.
    McLaury, B. S.
    Schleicher, E.
    Hampel, U.
    [J]. ASME FLUIDS ENGINEERING DIVISION SUMMER MEETING - 2014, VOL 2: FORA, 2014,
  • [49] The effect of the liquid physical properties on the wave frequency and wave velocity of co-current gas-liquid stratified two-phase flow in a horizontal pipe
    Wijayanta, Setya
    Deendarlianto
    Indarto
    Prasetyo, Ari
    Hudaya, Akhmad Zidni
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2023, 158
  • [50] Correlations predicting liquid hold-up and pressure gradient in steady-state (nearly) horizontal co-current gas-liquid pipe flow
    Ottens, M
    Hoefsloot, HCJ
    Hamersma, PJ
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2001, 79 (A5) : 581 - 592