Difference between revisions of "Hagedorn and Brown correlation"
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:<math> CN_L = 0.061\ N_L^3 - 0.0929\ N_L^2 + 0.0505\ N_L + 0.0019 </math> | :<math> CN_L = 0.061\ N_L^3 - 0.0929\ N_L^2 + 0.0505\ N_L + 0.0019 </math> | ||
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+ | :<math> v_{SL} </math> | ||
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+ | :<math> v_{SG} </math> | ||
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+ | :<math> N_{LV} </math> | ||
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+ | :<math> N_{GV} </math> | ||
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+ | :<math> N_D </math> | ||
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+ | corr p1 | ||
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+ | :<math> H_L \psi </math> | ||
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+ | corr p2 | ||
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+ | :<math> \psi </math> | ||
== Block Diagram == | == Block Diagram == |
Revision as of 16:23, 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