Effect of gas compressibility on a slug tracking model

被引:50
作者
Taitel, Y [1 ]
Barnea, D [1 ]
机构
[1] Tel Aviv Univ, Fac Engn, Dept Fluid Mech & Heat Transfer, IL-69978 Ramat Aviv, Israel
关键词
two-phase; slug flow; slug tracking; transient slug flow;
D O I
10.1016/S0009-2509(98)00007-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Slug flow is a very common occurrence in gas-liquid two-phase how. Usually, it is an unfavorable flow pattern due to its unsteady nature, intermittency and high-pressure drop. For the calculation of the pressure drop and void fraction the commonly used approach is to treat an average slug unit with the assumption that all slug units are identical. This approach may be adequate for many engineering calculations but it fails to predict the true nature of slug movement in a pipeline. In many cases the information as to the length distribution and, in particular, the maximum possible slug length is of major interest. Recent efforts, to address this; problem, are based on a calculation scheme that can follow each slug and predict its evolution, growth or decay, as it moves along the pipe. Some success was reported for the case where the gas compressibility is neglected. In this work the effect of compressibility an the slug length evolution and inlet pressure is computed. Some initial results and numerical approaches are discussed. (C) 1998 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:2089 / 2097
页数:9
相关论文
共 22 条
[1]   EFFECT OF BUBBLE SHAPE ON PRESSURE-DROP CALCULATIONS IN VERTICAL SLUG FLOW [J].
BARNEA, D .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1990, 16 (01) :79-89
[2]   A MODEL FOR SLUG LENGTH DISTRIBUTION IN GAS-LIQUID SLUG FLOW [J].
BARNEA, D ;
TAITEL, Y .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1993, 19 (05) :829-838
[3]   EFFECT OF GAS-EXPANSION ON SLUG LENGTH [J].
BENDIKSEN, K ;
HOYER, N ;
MALNES, D .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1988, 14 (05) :653-654
[4]  
Bendlksen K.H., 1991, SPE Prod. Oper., V6, P171, DOI DOI 10.2118/19451-PA
[5]   EFFECT OF WAVES AT A GAS-LIQUID INTERFACE ON A TURBULENT AIR FLOW [J].
COHEN, LS ;
HANRATTY, TJ .
JOURNAL OF FLUID MECHANICS, 1968, 31 :467-&
[6]   A TRANSIENT 2-FLUID MODEL FOR THE SIMULATION OF SLUG FLOW IN PIPELINES .1. THEORY [J].
DEHENAU, V ;
RAITHBY, GD .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1995, 21 (03) :335-349
[7]   A TRANSIENT 2-FLUID MODEL FOR THE SIMULATION OF SLUG FLOW IN PIPELINES .2. VALIDATION [J].
DEHENAU, V ;
RAITHBY, GD .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1995, 21 (03) :351-363
[8]   MODEL FOR GAS-LIQUID SLUG FLOW IN HORIZONTAL AND NEAR HORIZONTAL TUBES [J].
DUKLER, AE ;
HUBBARD, MG .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1975, 14 (04) :337-347
[9]  
FABRE J, 1992, ANNU REV FLUID MECH, V24, P21, DOI 10.1146/annurev.fl.24.010192.000321
[10]   HYDRODYNAMIC MODEL FOR GAS-LIQUID SLUG FLOW IN VERTICAL TUBES [J].
FERNANDES, RC ;
SEMIAT, R ;
DUKLER, AE .
AICHE JOURNAL, 1983, 29 (06) :981-989