Difference between revisions of "Gray correlation"
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where | where | ||
− | :<math> \bar \rho_m = \rho_L (1-H_g) + \rho_g H_g</math> slip mixture density | + | :<math> \bar \rho_m = \rho_L (1-H_g) + \rho_g H_g</math>, slip mixture density |
− | :<math> \rho_m = \rho_L C_L + \rho_g (1-C_L) </math> no-slip mixture density | + | :<math> \rho_m = \rho_L C_L + \rho_g (1-C_L) </math>, no-slip mixture density |
Colebrook–White <ref name=Colebrook/> equation for the [http://en.wikipedia.org/wiki/Darcy_friction_factor_formulae Darcy's friction factor]: | Colebrook–White <ref name=Colebrook/> equation for the [http://en.wikipedia.org/wiki/Darcy_friction_factor_formulae Darcy's friction factor]: |
Revision as of 18:21, 4 April 2017
Brief
- The boundary between the bubble and slug flow[1]
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:
Reynolds two phase number:
Discussion
Workflow
To find Hg calculate [1]:
Nomenclature
NV velocity number
References
- ↑ 1.0 1.1 1.2 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.