Power law and composite power law friction factor correlations for laminar and turbulent gas-liquid flow in horizontal pipelines
Power law and composite power law friction factor correlations for laminar and turbulent gas-liquid flow in horizontal pipelines
Data from 2435 gas-liquid flow experiments in horizontal pipelines, taken from different sources, including new data for heavy oil are compiled and processed for power law and composite power law friction factor correlations. To our knowledge this is the largest database so far published in the literature; it includes the widest range of operational conditions and fluid properties for two-phase friction factor correlations. Separate power laws for laminar and turbulent flows are obtained for all flows in the database and also for flows sorted by flow pattern. Composite analytical expressions for the friction factor covering both laminar and turbulent flows are obtained by fitting the transition region between laminar and turbulent flow with logistic dose curves. Logistic dose curves lead to rational fractions of power laws which reduce to the power laws for laminar flow when the Reynolds number is low and to turbulent flow when the Reynolds number is large. The Reynolds number appropriate for gas-liquid flows in horizontal pipes is based on the mixture velocity and the liquid kinematic viscosity. The definition of the Fanning friction factor for gas-liquid flow used in this study is based on the mixture velocity and density. Error estimates for the predicted vs. measured friction factor together with standard deviation for each correlation are presented. The correlations in this study are compared with previous correlations, homogeneous models and mechanistic models most commonly used for gas-liquid flow in pipelines. Since different authors use different definitions for friction factors and Reynolds numbers, comparisons of the predicted pressure drop for each and every data point in the database are presented. Our correlations predict the pressure drop with much greater accuracy than those presented by previous authors.
Flow type, Friction-factor, Gas-liquid, Pipe flow, Power law
1605-1624
García, F.
128461cb-6f7b-499b-93b4-1c7ef774a078
García, R.
655c5cb0-f276-414f-954f-c6e555489885
Padrino, J.C.
961f9d2a-ee9d-4619-a267-2bf098612978
Mata, C.
8fdff2e1-f2ce-4a54-8fb0-ad9ef2d9f9c8
Trallero, J.L.
60eb5aaf-7336-485b-bef9-e93907c745b0
Joseph, D.D.
fda3580e-d34a-488d-b4fb-ba1f10de1020
October 2003
García, F.
128461cb-6f7b-499b-93b4-1c7ef774a078
García, R.
655c5cb0-f276-414f-954f-c6e555489885
Padrino, J.C.
961f9d2a-ee9d-4619-a267-2bf098612978
Mata, C.
8fdff2e1-f2ce-4a54-8fb0-ad9ef2d9f9c8
Trallero, J.L.
60eb5aaf-7336-485b-bef9-e93907c745b0
Joseph, D.D.
fda3580e-d34a-488d-b4fb-ba1f10de1020
García, F., García, R., Padrino, J.C., Mata, C., Trallero, J.L. and Joseph, D.D.
(2003)
Power law and composite power law friction factor correlations for laminar and turbulent gas-liquid flow in horizontal pipelines.
International Journal of Multiphase Flow, 29 (10), .
(doi:10.1016/S0301-9322(03)00139-3).
Abstract
Data from 2435 gas-liquid flow experiments in horizontal pipelines, taken from different sources, including new data for heavy oil are compiled and processed for power law and composite power law friction factor correlations. To our knowledge this is the largest database so far published in the literature; it includes the widest range of operational conditions and fluid properties for two-phase friction factor correlations. Separate power laws for laminar and turbulent flows are obtained for all flows in the database and also for flows sorted by flow pattern. Composite analytical expressions for the friction factor covering both laminar and turbulent flows are obtained by fitting the transition region between laminar and turbulent flow with logistic dose curves. Logistic dose curves lead to rational fractions of power laws which reduce to the power laws for laminar flow when the Reynolds number is low and to turbulent flow when the Reynolds number is large. The Reynolds number appropriate for gas-liquid flows in horizontal pipes is based on the mixture velocity and the liquid kinematic viscosity. The definition of the Fanning friction factor for gas-liquid flow used in this study is based on the mixture velocity and density. Error estimates for the predicted vs. measured friction factor together with standard deviation for each correlation are presented. The correlations in this study are compared with previous correlations, homogeneous models and mechanistic models most commonly used for gas-liquid flow in pipelines. Since different authors use different definitions for friction factors and Reynolds numbers, comparisons of the predicted pressure drop for each and every data point in the database are presented. Our correlations predict the pressure drop with much greater accuracy than those presented by previous authors.
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e-pub ahead of print date: 9 August 2003
Published date: October 2003
Keywords:
Flow type, Friction-factor, Gas-liquid, Pipe flow, Power law
Identifiers
Local EPrints ID: 510673
URI: http://eprints.soton.ac.uk/id/eprint/510673
ISSN: 0301-9322
PURE UUID: 029991bf-bc96-4a85-8ebe-55128ff9a729
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Date deposited: 16 Apr 2026 16:39
Last modified: 17 Apr 2026 02:11
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Contributors
Author:
F. García
Author:
R. García
Author:
J.C. Padrino
Author:
C. Mata
Author:
J.L. Trallero
Author:
D.D. Joseph
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