Difference between revisions of "Hagedorn and Brown correlation"

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(Math & Physics)
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friction factor the Colebrook–White equation:
 
friction factor the Colebrook–White equation:
 
:<math> \frac{1}{\sqrt{f}}= -2 \log \left( \frac { \varepsilon} {3.7 D} + \frac {2.51} {\mathrm{Re} \sqrt{f}} \right)</math>
 
:<math> \frac{1}{\sqrt{f}}= -2 \log \left( \frac { \varepsilon} {3.7 D} + \frac {2.51} {\mathrm{Re} \sqrt{f}} \right)</math>
 +
 +
Reynolds two phase number:
 +
:<math> Re = 2.2 \times 10^-2 \frac {q_L M}{D \mu^H_L \mu^(1-H_L)}</math>
  
 
== Workflow ==
 
== Workflow ==

Revision as of 08:05, 15 March 2017

Info

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 :H_L.

Math & Physics

The basic steady state flow equation is:

 144 \frac{\Delta p}{\Delta h} = \bar \rho_m + \frac{f q_L^2 M^2}{2.9652 \times 10^{11} D^5 \bar \rho_m} + \bar \rho_m \frac{\Delta{(\frac{v_m^2}{2g_c}})}{\Delta h}

where

 \bar \rho_m = \bar \rho_L H_L + \bar \rho_g (1 - H_L)

friction factor the Colebrook–White equation:

 \frac{1}{\sqrt{f}}= -2 \log \left( \frac { \varepsilon} {3.7 D} + \frac {2.51} {\mathrm{Re} \sqrt{f}} \right)

Reynolds two phase number:

 Re = 2.2 \times 10^-2 \frac {q_L M}{D \mu^H_L \mu^(1-H_L)}

Workflow

For each pipe segment find:

Block Diagram

References