Solution nonuniqueness for separated gas-liquid flow in pipes and wells. I. Occurrence

被引:2
|
作者
Ouyang, LB [1 ]
Aziz, K [1 ]
机构
[1] Stanford Univ, Dept Petr Engn, Stanford, CA 94305 USA
关键词
D O I
10.1081/LFT-120002093
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The Occurrence Of Multiple Solutions has been investigated and discussed in this paper. Multiple Solution regions are displayed by either a U-SL-U-SG map or a X-Y map. It is found that many parameters impose influence on the multiple solution regions, including fluid properties, pipe ID, pipe inclination angle, wall inflow Or Outflow, empirical correlations for wall friction and interfacial friction factors, and so on. For example, the multiple Solution region could change significantly if different interfacial friction factor correlations are applied. Multiple solutions are only possible for upward flow for separated flow in a pipe without wall mass transfer. However, for wellbore flow case, depending on wall inflow or outflow of fluids and their flow rates, multiple solutions may also exist for horizontal and downward flow. More specifically, for wall inflow case (production well), multiple solutions only exist for upward flow for the gas inflow-dominant case, whereas they may exist for upward, horizontal and downward flow for liquid inflow-dominant situations. The opposite is expected for wall Outflow (injection well) case.
引用
收藏
页码:143 / 171
页数:29
相关论文
共 50 条
  • [1] Solution nonuniqueness for separated gas-liquid flow in pipes and wells. II. Analysis
    Ouyang, LB
    Aziz, K
    PETROLEUM SCIENCE AND TECHNOLOGY, 2002, 20 (1-2) : 173 - 190
  • [2] The flow of gas-liquid foams in vertical pipes
    Deshpande, NS
    Barigou, M
    CHEMICAL ENGINEERING SCIENCE, 2000, 55 (19) : 4297 - 4309
  • [3] Gas-liquid flow in slightly inclined pipes
    Grolman, E
    Fortuin, JMH
    CHEMICAL ENGINEERING SCIENCE, 1997, 52 (24) : 4461 - 4471
  • [4] OPTIMAL LIQUID FLOW RATE IN GAS-LIFT WELLS.
    Belogortzev, G.P.
    Vasil'ev, V.A.
    Guzhov, A.I.
    Oil Industry, 1987, (05): : 29 - 31
  • [5] GAS-LIQUID REACTORS .I. THEORY
    BRIDGWAT.J
    CARBERRY, JJ
    BRITISH CHEMICAL ENGINEERING, 1967, 12 (01): : 58 - &
  • [6] INTERMITTENT GAS-LIQUID FLOW IN UPWARD INCLINED PIPES
    STANISLAV, JF
    KOKAL, S
    NICHOLSON, MK
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1986, 12 (03) : 325 - 335
  • [7] New dimensionless number for gas-liquid flow in pipes
    Abdelsalam, Alsarkhi
    Cem, Sarica
    Eduardo, Pereyra
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2016, 81 : 15 - 19
  • [8] STRATIFIED GAS-LIQUID FLOW IN DOWNWARDLY INCLINED PIPES
    ANDREUSSI, P
    PERSEN, LN
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1987, 13 (04) : 565 - 575
  • [9] GAS-LIQUID FLOW IN DOWNWARD AND UPWARD INCLINED PIPES
    STANISLAV, JF
    KOKAL, S
    NICHOLSON, MK
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1986, 64 (06): : 881 - 890
  • [10] A DEFINITION OF GAS-LIQUID PLUG FLOW IN HORIZONTAL PIPES
    RUDER, Z
    HANRATTY, TJ
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1990, 16 (02) : 233 - 242