Difference between revisions of "Contrib/CompressibleMixingPhaseChangeFoam"
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Mkraposhin (Talk | contribs) (→Model Equations) |
Mkraposhin (Talk | contribs) (→Model Equations) |
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* Equation of state | * Equation of state | ||
* Liquid volume transport | * Liquid volume transport | ||
| + | Let us consider transport of liquid (heavy phase) volume fraction <math>\alpha_l</math>: | ||
| + | |||
| + | The solver is based on turbFoam, with the transport of a scalar ''T'' having a mass diffusion coefficient <math>D_T</math>: | ||
| + | |||
| + | |||
* Phase change model | * Phase change model | ||
* Momentum equation | * Momentum equation | ||
* Energy equation | * Energy equation | ||
[http://www.os-cfd.ru/compressibleMixingPhaseChangeFoam/Solver.tgz Solver sources and tutorials located here] | [http://www.os-cfd.ru/compressibleMixingPhaseChangeFoam/Solver.tgz Solver sources and tutorials located here] | ||
Revision as of 19:48, 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 
:
The solver is based on turbFoam, with the transport of a scalar T having a mass diffusion coefficient 
:
* Phase change model * Momentum equation * Energy equation
