Difference between revisions of "Gray correlation"
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:<math> H_g = \frac{1-e^A}{R+1}</math> | :<math> H_g = \frac{1-e^A}{R+1}</math> | ||
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+ | :<math> C_L = \frac{v_{SL}}{v_{SG}+v_{SL}}</math> | ||
== Nomenclature == | == Nomenclature == |
Revision as of 19:00, 4 April 2017
Brief
Math & Physics
Following the law of conservation of energy the basic steady state flow equation is:
where
- , slip mixture density
- , no-slip mixture density
Colebrook–White [2] equation for the Darcy's friction factor:
The pseudo wall roughness [1]:
- , with the limit
Reynolds two phase number:
Discussion
Workflow Hg
Nomenclature
NV velocity number
References
- ↑ 1.0 1.1 1.2 1.3 Gray, H. E. (1974). "Vertical Flow Correlation in Gas Wells". User manual for API 14B, Subsurface controlled safety valve sizing computer program. API.
- ↑ Colebrook, C. F. (1938–1939). "Turbulent Flow in Pipes, With Particular Reference to the Transition Region Between the Smooth and Rough Pipe Laws". Journal of the Institution of Civil Engineers. London, England. 11: 133–156.
- ↑ Moody, L. F. (1944). "Friction factors for pipe flow". Transactions of the ASME. 66 (8): 671–684.