Difference between revisions of "Gray correlation"
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== Discussion == | == Discussion == | ||
− | == Workflow | + | == Workflow H<sub>g</sub == |
:<math> N_V = 453.592\ \frac{{\rho_m}^2 {v_m}^4}{g_c \sigma_L (\rho_L - \rho_g)} </math><ref name= Gray/> | :<math> N_V = 453.592\ \frac{{\rho_m}^2 {v_m}^4}{g_c \sigma_L (\rho_L - \rho_g)} </math><ref name= Gray/> |
Revision as of 18:34, 4 April 2017
Contents
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 Hg</sub
Workflow ε'
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.