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solidificationMeltingSource: Improved documentation
Patch contributed by Lorenzo Trevisan Resolves patch request https://bugs.openfoam.org/view.php?id=2932
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@ -31,10 +31,28 @@ Description
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The isotherm phase change occurs at the melting temperature, \c Tsol (= \c
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Tliq). The not isotherm phase change occurs between solidus and liquidus
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temperature, \c Tsol < \c Tliq respectively, as long as the melt fraction is
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greater than the max eutectic melt fraction, \c alpha1e (0 =
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pure_substance, 1 = eutectic_mixture is not permitted) , i.e. eutectic to
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initial solvent concentration difference, where a linear eutectic melt
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fraction to temperature relation is considered - lever rule.
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greater than the max eutectic melt fraction, \c alpha1e (0 = pure_substance,
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1 = eutectic_mixture is not permitted), where a linear eutectic melt
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fraction to temperature relation is considered; e.g. given a specific
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quantity of a binary system, \c alpha1 is its melt fraction and \c alpha0 is
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its solid fraction, such that \c alpha0 = 1 - \c alpha1 therefore, assuming
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infinite solute diffusion, the quantity of a component in solid phase is (1
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- \c alpha1) * \c CS where \c CS is the solid concentration of the
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considered component and the quantity of a component in liquid phase is \c
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alpha1 * \c CL where \c CL is the melt concentration of the considered
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component; considering that the total quantity of a component must be equal
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to the sum of the quantities of the considered component in the liquid and
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solid phases, if \c C0 is the initial concentration of the considered
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component before the phase change, then:
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\c C0 = (1 - \c alpha1) * \c CS + \c alpha1 * \c CL (lever rule)
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from which: \c alpha1 = (\c C0 - \c CS) / (\c CL - \c CS)
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and thus:
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- for a miscible binary system \c alpha1e = 0;
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- for a binary system not miscible at solid state
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\c alpha1e = \c C0 / \c CLE where \c CLE is eutectic melt concentration;
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- for a binary system partially-miscible at solid state
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\c alpha1e = (\c C0 - \c CSE) / (\c CLE - \c CSE) where CSE is eutectic
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solid concentration of the relative solid solution.
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The presence of the solid phase in the flow field is incorporated into the
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model as a momentum porosity contribution; the energy associated with the
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