Difference between revisions of "Hagedorn and Brown correlation"
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:<math> v_{SG} </math> | :<math> v_{SG} </math> | ||
− | :<math> N_{LV} = 1.938 v_{SL} \sqrt[4]{\frac{\rho_L}{\sigma} </math> | + | :<math> N_{LV} = 1.938 v_{SL} \sqrt[4]{\frac{\rho_L}{\sigma}} </math> |
− | :<math> N_{GV} = 1.938 v_{SG} \sqrt[4]{\frac{\rho_L}{\sigma} </math> | + | :<math> N_{GV} = 1.938 v_{SG} \sqrt[4]{\frac{\rho_L}{\sigma}} </math> |
:<math> N_D </math> | :<math> N_D </math> |
Revision as of 16:29, 20 March 2017
Brief
Hagedorn and Brown is an empirical two-phase flow correlation published in 1965.
It doesn't distinguish between the flow regimes.
The heart of the Hagedorn and Brown method is a correlation for the liquid holdup :.
Math & Physics
Following the law of conservation of energy the basic steady state flow equation is:
where
Colebrook–White equation for the Darcy's friction factor:
Reynolds two phase number:
Workflow
corr p1
corr p2