Difference between revisions of "Hagedorn and Brown correlation"
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:<math> M =SG_o\ 350.52\ \frac{1}{1+WOR}+SG_w\ 350.52\ \frac{WOR}{1+WOR}+SG_g\ 0.0764\ GLR</math> | :<math> M =SG_o\ 350.52\ \frac{1}{1+WOR}+SG_w\ 350.52\ \frac{WOR}{1+WOR}+SG_g\ 0.0764\ GLR</math> | ||
− | :<math> \bar rho_L= \frac{62.4\ SG_o + \frac{Rs\ 0.0764\ SG_g}{5.614}}{B_o} \frac{1}{1+WOR} + 62.4\ SG_w\ \frac{WOR}{1 + WOR}</math> | + | :<math> \bar \rho_L= \frac{62.4\ SG_o + \frac{Rs\ 0.0764\ SG_g}{5.614}}{B_o} \frac{1}{1+WOR} + 62.4\ SG_w\ \frac{WOR}{1 + WOR}</math> |
− | :<math> \bar roh_g = \frac{28.967\ SG_g\ p}{z\ 10.732\ T} </math> | + | :<math> \bar \roh_g = \frac{28.967\ SG_g\ p}{z\ 10.732\ T} </math> |
== Block Diagram == | == Block Diagram == |
Revision as of 16:02, 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
- Failed to parse (unknown function "\roh"): \bar \roh_g = \frac{28.967\ SG_g\ p}{z\ 10.732\ T}