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In the Select Physics tree, select Fluid Flow>Multiphase Flow>Rotating Machinery, Phase Transport Mixture Model>Turbulent Flow>Turbulent Flow, k-ε.
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Click Add.
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Click
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Click
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Click
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Browse to the model’s Application Libraries folder and double-click the file three_phase_mixer.mphbin.
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Select the Cutoff check box.
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In the Model Builder window, under Component 1 (comp1)>Phase Transport (phtr) click Initial Values 1.
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Locate the Dispersed Phase 2 Properties section. From the ρs2 list, choose User defined. In the associated text field, type 1100[kg/m^3].
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Locate the Dispersed Phase 3 Properties section. From the ρs3 list, choose User defined. In the associated text field, type 850[kg/m^3].
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In the Model Builder window, under Study 1>Solver Configurations>Solution 1 (sol1) click Time-Dependent Solver 1.
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In the Model Builder window, expand the Study 1>Solver Configurations>Solution 1 (sol1)>Time-Dependent Solver 1>Segregated 1 node, then click Velocity u, Pressure p.
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In the Model Builder window, under Study 1>Solver Configurations>Solution 1 (sol1)>Time-Dependent Solver 1>Segregated 1 click Volume fractions.
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Click OK.
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Select the Enable check box.
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In the Model Builder window, under Results>2D Plot Group 6 right-click Surface 1 and choose Duplicate.
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In the Model Builder window, under Results>2D Plot Group 6 right-click Surface 1 and choose Duplicate.
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Select the Interactive check box.
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Click OK.
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In the Model Builder window, expand the Results>Volume Fraction (phtr) node, then click Volume Fraction (phtr).
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