An Improved Pressure Drop Prediction Model Based on Okiszewski's Model for Low Gasliquid Ratio Two-Phase Upward Flow in Vertical Pipe

被引:2
|
作者
Dong, Yong [1 ]
Liao, Ruiquan [2 ,3 ,4 ]
Luo, Wei [2 ,3 ,4 ]
Li, Mengxia [2 ,3 ,5 ]
机构
[1] Yangtze Univ, Sch Informat & Math, Jingzhou 434023, Peoples R China
[2] Yangtze Univ, Branch Key Lab CNPC Oil & Gas Prod, Jingzhou 434023, Peoples R China
[3] Yangtze Univ, Lab Multiphase Pipe Flow, Gas Lift Innovat Ctr, CNPC, Wuhan 430100, Peoples R China
[4] Yangtze Univ, Petr Engn Coll, Wuhan 430100, Peoples R China
[5] Yangtze Univ, Sch Comp Sci, Jingzhou 434023, Peoples R China
基金
中国国家自然科学基金;
关键词
gas-liquid two-phase upward flow; vertical pipe; low gas-liquid ratio; pressure drop prediction; Orkiszewski's model; liquid distribution coefficient;
D O I
10.18280/ijht.400103
中图分类号
O414.1 [热力学];
学科分类号
摘要
Compared with experimental data of pressure drop of gas-liquid two-phase upward flow with low gas-liquid ratio in vertical pipe, the mean relative error of pressure drop predicted by Orkiszewski's model is 63.62%, the maximum relative error of the model is 98.07%. This paper first introduces the process of acquiring experimental data, then, combined with the experimental data, it is pointed out that the Orkiszewski's model has a small error in predicting the annular-mist flow pattern, but a large error in predicting the slug flow pattern and annular-slug transition flow pattern. The author analyzes the structure of Orkiszewski's model and points out that the formula of liquid distribution coefficient in slug flow pattern is complex and very important. In this paper, a new threshold value of liquid distribution coefficient is proposed and an improved Orkiszewski's model is obtained by particle swarm optimization. The calculated results of experimental data show that the average relative error of the new model is reduced to 25.28%, and the average relative error of the new model can be reduced from 76.17% to 17.21% for the slug flow pattern with continuous oil phase and total flow velocity greater than or equal to 3.048m/s.
引用
收藏
页码:17 / 22
页数:6
相关论文
共 50 条
  • [31] A two-phase, two-component model for vertical upward gas-liquid annular flow
    Liu, Y.
    Cui, J.
    Li, W. Z.
    INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2011, 32 (04) : 796 - 804
  • [32] The phenomenon of negative frictional pressure drop in vertical two-phase flow
    Liu, Lei
    INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2014, 45 : 72 - 80
  • [33] Vertical two-phase flow. Part III: Pressure drop
    Chemical Engineering Research & Design, Transactions of the Institute of Chemical Engineers, Part A, 1998, 76 (A5): : 628 - 634
  • [34] Calculation of two-phase pressure drop for vertical upflow in narrow passages by means of a flow pattern specific model
    Holt, AJ
    Azzopardi, BJ
    Biddulph, MW
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 1999, 77 (A1): : 7 - 15
  • [35] Pressure drop prediction in two-phase flow of refrigerants, and other working fluids, in pipes and pipe components
    Paliwoda, A
    RESEARCH, DESIGN AND CONSTRUCTION OF REFRIGERATION AND AIR CONDITIONING EQUIPMENTS IN EASTERN EUROPEAN COUNTRIES, 1996, : 275 - 281
  • [36] MODELING OF LOW AND HIGH VOID FRACTION TWO-PHASE FLOW IN A VERTICAL PIPE BY USING THE TWO-FLUID MODEL
    Yu, Shimo
    Yan, Xiao
    Zhang, Junyi
    PROCEEDINGS OF THE 26TH INTERNATIONAL CONFERENCE ON NUCLEAR ENGINEERING, 2018, VOL 8, 2018,
  • [37] Effect of solid particles on the hydrodynamics of vertical upward gas-liquid two-phase flow: Pressure drop analysis
    Hohn, Ronaldo Luis
    Arabi, Abderraouf
    Ballesta, Sylvana Veronica Varela
    Sassi, Paolo Juan
    Pallares, Jordi
    Stiriba, Youssef
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2025, 214 : 234 - 250
  • [38] Flow patterns and heat transfer of oil-water two-phase upward flow in vertical pipe
    Hamidi, Mohammad J.
    Karimi, Hajir
    Boostani, Milad
    INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2018, 127 : 173 - 180
  • [39] A MECHANISTIC MODEL OF TWO-PHASE PRESSURE DROP IN MICROCHANNELS
    Field, Brandon S.
    Hrnjak, Pega
    PROCEEDINGS OF THE ASME INTERNATIONAL MECHANICAL ENGINEERING CONGRESS AND EXPOSITION, 2011, VOL 6, PTS A AND B, 2012, : 411 - 419
  • [40] Effect of pipe rotation on flow pattern and pressure drop of horizontal two-phase flow
    Baghernejad, Yosef
    Hajidavalloo, Ebrahim
    Zadeh, Seyed Mohsen Hashem
    Behbahani-Nejad, Morteza
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2019, 111 : 101 - 111