TECHNICAL PAPERS
May 1, 1998

Pressure Loss Equations for Laminar and Turbulent Non-Newtonian Pipe Flow

Publication: Journal of Hydraulic Engineering
Volume 124, Issue 5

Abstract

The equations that define Newtonian pipe flow are well established and used routinely by engineers and scientists throughout the world. The same cannot be said for non-Newtonian flows, which have a higher degree of complexity. This paper presents a coherent set of equations for the laminar and turbulent flow of Herschel-Bulkley fluids. These equations are consistent with those used for Newtonian fluids and previous work on the behavior of generalized non-Newtonian fluids. A numerical model for non-Newtonian flows is discussed and has been compared with experimental measurements from different sources. This model has been used to run a series of simulations to find the coefficients required for a new turbulent friction factor correlation. A new Reynolds number has been defined that represents the conditions in turbulent flows more realistically than the existing Metzner-Reed Reynolds number.

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Go to Journal of Hydraulic Engineering
Journal of Hydraulic Engineering
Volume 124Issue 5May 1998
Pages: 522 - 529

History

Published online: May 1, 1998
Published in print: May 1998

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Authors

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Richard A. Chilton
Chf. Engr., Bechtel Water Technology Ltd., Chadwick House, Warrington, WA3 6AE U.K.
Richard Stainsby
Princ. Engr., AEA Technology PLC, Thomson House, Risley, Warrington, WA3 6AT U.K.

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