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RESEARCH PAPERS: Petroleum Fluid Mechanics

Pressure Drop Correlations for Inclined Two-Phase Flow

[+] Author and Article Information
H. Mukherjee

Flopetrol-Johnston/Schlumberger, Anchorage, Alaska

J. P. Brill

The University of Tulsa, Tulsa, Okla. 74104

J. Energy Resour. Technol 107(4), 549-554 (Dec 01, 1985) (6 pages) doi:10.1115/1.3231233 History: Received September 25, 1984; Revised August 26, 1985; Online October 22, 2009

Abstract

Pressure drop behavior in two-phase inclined flow was studied. For bubble and slug flow, a no-slip friction factor calculated from the Moody diagram was found adequate for friction head loss calculations. In downhill stratified flow, the friction pressure gradient is calculated based on a momentum balance equation for either phase assuming a smooth gas-liquid interface. For this calculation, a prior knowledge of the liquid holdup is needed. For annular-mist flow, a friction factor correlation is presented that is a function of holdup ratio and no-slip Moody friction factor. Results agree well with the experimental data and correlations were further verified with Prudhoe Bay and North Sea data.

Copyright © 1985 by ASME
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