Difference between revisions of "Contrib/CompressibleMixingPhaseChangeFoam"
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Mkraposhin (Talk | contribs) (→Model Equations) |
Mkraposhin (Talk | contribs) (→Model Equations) |
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By converting to volume fluxes we get: | By converting to volume fluxes we get: | ||
+ | |||
<math> | <math> | ||
\frac {\partial \alpha_l}{\partial t} + \nabla \cdot | \frac {\partial \alpha_l}{\partial t} + \nabla \cdot | ||
Line 22: | Line 23: | ||
\alpha_l \mathbf{U} | \alpha_l \mathbf{U} | ||
\right ) | \right ) | ||
− | = \frac {\alpha_l}{\rho_l} \frac {d \rho_l}{dt} + \frac { | + | = \frac {\alpha_l}{\rho_l} \frac {d \rho_l}{dt} + \frac {\dot m_l}{\rho_l} |
</math> | </math> | ||
Revision as of 20:05, 28 December 2012
Solver for two fluids with phase change (for example - water <---> steam), pressure and temperature density dependence
Model Equations
- Equation of state
- Liquid volume transport
Let us consider transport of liquid (heavy phase) volume fraction :
By converting to volume fluxes we get:
* Phase change model * Momentum equation * Energy equation