Difference between revisions of "Griffith correlation"
From wiki.pengtools.com
(→Discussion) |
|||
(4 intermediate revisions by the same user not shown) | |||
Line 17: | Line 17: | ||
== Discussion == | == Discussion == | ||
− | [[Griffith correlation]] adds a hook to | + | [[Griffith correlation]] adds a hook to the originally straight [[Hagedorn and Brown]] [[VLP]] curve. |
== Nomenclature == | == Nomenclature == | ||
Line 71: | Line 71: | ||
[[Category:pengtools]] | [[Category:pengtools]] | ||
− | [[Category: | + | [[Category:PQplot]] |
+ | |||
+ | {{#seo: | ||
+ | |title=Griffith correlation | ||
+ | |titlemode= replace | ||
+ | |keywords=Griffith correlation | ||
+ | |description=Griffith correlation is an empirical correlation which defines: the boundary between the bubble and slug flow. | ||
+ | }} |
Latest revision as of 09:27, 6 December 2018
Brief
The Griffith correlation [1] is an empirical correlation which defines:
- The boundary between the bubble and slug flow[2]
- The void fraction of gas in bubble flow - gas hold up Hg[2]
Math & Physics
The bubble flow exist when:
- , with the limit [2]
The gas holdup:
Discussion
Griffith correlation adds a hook to the originally straight Hagedorn and Brown VLP curve.
Nomenclature
- = pipe diameter, ft
- = gas holdup factor, dimensionless
- = bubble-slug boundary, dimensionless
- = gas velocity, ft/sec
- = liquid velocity, ft/sec
- = 0.8, slip velocity (difference between average gas and liquid velocities), ft/sec
References
- ↑ Griffith, P.; Wallis, G. B. (August 1961). "Two-Phase Slug Flow". Journal of Heat Transfer. ASME. 83: 307–320.
- ↑ 2.0 2.1 2.2 2.3 Orkiszewski, J. (June 1967). "Predicting Two-Phase Pressure Drops in Vertical Pipe". Journal of Petroleum Technology. SPE. 19 (SPE-1546-PA).
- ↑ Economides, M.J.; Hill, A.D.; Economides, C.E.; Zhu, D. (2013). Petroleum Production Systems (2 ed.). Westford, Massachusetts: Prentice Hall. ISBN 978-0-13-703158-0.