1967
DOI: 10.2118/1525-pa
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The Prediction of Flow Patterns, Liquid Holdup and Pressure Losses Occurring During Continuous Two-Phase Flow In Horizontal Pipelines

Abstract: This paper presents the resu[ts of an investigation ofIwo-phase, gas-liquid flow in horizontal pipelines. Experimental data were taken in three field-size, horizontal pipelines, two of which were constructed for this purpose. The data were obtained using water, distillate and crude oi! separately as the liquid phase, and natural gas as~he second phase. Experimental pressure-length traverse, liquid holdup and f?ow-pattern data were collected jor each set of flow rates, These data were used to deve[op three corr… Show more

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Cited by 109 publications
(72 citation statements)
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“…Marcano compared five correlations; Lockhart and Martinelli (1949), Hughmark (1962), Dukler et al (1969), Eaton et al (1967), Guzhov et al (1967) and Beggs (1972) correlations using the data of Eaton (1966) and Beggs (1972). The total data points consisted of 238 natural gas-water (Eaton) and 58 air-water (Beggs).…”
Section: Marcano (1973) Horizontal Pipe Comparisonmentioning
confidence: 99%
See 1 more Smart Citation
“…Marcano compared five correlations; Lockhart and Martinelli (1949), Hughmark (1962), Dukler et al (1969), Eaton et al (1967), Guzhov et al (1967) and Beggs (1972) correlations using the data of Eaton (1966) and Beggs (1972). The total data points consisted of 238 natural gas-water (Eaton) and 58 air-water (Beggs).…”
Section: Marcano (1973) Horizontal Pipe Comparisonmentioning
confidence: 99%
“…After the initial screening process that primarily considered the completeness of the data set, the data of Eaton (1966), Beggs (1972), Spedding and Nguyen (1976), Mukherjee (1979), Minami and Brill (1987), Franca and Lahey (1992), Abdulmajeed (1996) and Sujumnong (1997) were selected with which the performance of the void fraction correlations are to be compared. The range of diameters, inclination angles, number of data points and fluids covered by the data is summarized in Table 2.…”
Section: Experimental Database and Fluid Propertiesmentioning
confidence: 99%
“…Five pressure drop formulas are also included in the TGNET such as ''AGA,'' ''Colebrook,'' ''Pan (A),'' and ''Pan (B).'' [13][14][15][16][17][18][19] State equations …”
Section: Equations In Tgnet Softwarementioning
confidence: 99%
“…In this thesis study, the Eaton, Knowles and Silberbrg (1967) and Reynolds number, then friction pressure drop in two-phase flow would be calculated through similarity analysis approach (Dukler, Wicks and Cleveland, 1964). Liquid holdup was obtained through a trial and error calculation procedure (Dukler et al, 1969).…”
Section: Dukler Et Al (1969) Correlationmentioning
confidence: 99%