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contributor authorH. Mukherjee
contributor authorJ. P. Brill
date accessioned2017-05-08T23:19:52Z
date available2017-05-08T23:19:52Z
date copyrightDecember, 1985
date issued1985
identifier issn0195-0738
identifier otherJERTD2-26408#549_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/99652
description abstractPressure 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.
publisherThe American Society of Mechanical Engineers (ASME)
titlePressure Drop Correlations for Inclined Two-Phase Flow
typeJournal Paper
journal volume107
journal issue4
journal titleJournal of Energy Resources Technology
identifier doi10.1115/1.3231233
journal fristpage549
journal lastpage554
identifier eissn1528-8994
keywordsPressure drop
keywordsTwo-phase flow
keywordsFriction
keywordsFlow (Dynamics)
keywordsMomentum
keywordsBubbles
keywordsPressure gradient
keywordsSlug
keywordsStratified flow
keywordsNorth Sea AND Equations
treeJournal of Energy Resources Technology:;1985:;volume( 107 ):;issue: 004
contenttypeFulltext


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