Holdup predictions for wet-gas pipelines compared

Oil and Gas Journal

Volumn 95, Issue 20, 1997, Pages 73-75

  Shea, Richard H ^a   Rasmussen, Jon ^b   Hedne, Paal ^c   Malnes, Dag ^d  

^a Scandpower Petroleum Technology Inc   (United States)

^b Scandpower AB Kjeller ^*  (Norway)

^c SINTEF   (Norway)

^d Consultant ^*  (Norway)

Author keywords

[No Author keywords available]

Indexed keywords

CORRELATION METHODS; FLOW OF FLUIDS; MATHEMATICAL MODELS; PETROLEUM PRODUCTS; PRESSURE DROP;

HOLDUP PREDICTIONS; LIQUID HOLDUP; MECHANISTIC MODELS; WET GAS PIPELINES;

GAS PIPELINES;

ERRORS; HOLD-UP; MODELLING-MATHEMATICAL; PIPELINES-GAS;

EID: 0031147969     PISSN: 00301388     EISSN: None     Source Type: Journal    
DOI: None     Document Type: Article

References (4)

1. Bendiksen, K.H., Malnes, D., Moe, R., Nuland, S., "The Dynamic Two-Fluid Model OLGA: Theory and Application," SPE Production Engineering, May 1991, p. 171.
2. Oliemans, R.V.A., "Modelling of Gas Condensate Flow in Horizontal and Inclined Tubes," 1987 ASME Pipeline Engineering Symposium, Dallas, p. 73.
3. Beggs, H.D., and Brill J.P., "A study of Two-Phase Flow in Inclined Pipes," J. Pet. Technology. May 1973, p. 607.
4. Eaton, B.A., et al., "The Prediction of Flow Patterns, Liquid Holdup and Pressure Losses Occurring During Continuous Two-Phase Flow in Horizontal Pipelines," Trans. AIME (1967), p. 815.