9.92·10-4
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1.00·10-2
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Click Add.
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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 beer_fermentation_parameters.txt.
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In the Model Builder window, under Component 1 (comp1) right-click Definitions and choose Variables.
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Browse to the model’s Application Libraries folder and double-click the file beer_fermentation_variables1.txt.
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From the list, choose Include.
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Locate the Reaction Thermodynamic Properties section. From the Enthalpy of reaction list, choose User defined.
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In the text field, type C2H5OH.
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In the text field, type C4H8O2.
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In the text field, type C2H4O.
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Click Apply.
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Locate the Reaction Thermodynamic Properties section. From the Enthalpy of reaction list, choose User defined.
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Click Apply.
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Locate the Reaction Thermodynamic Properties section. From the Enthalpy of reaction list, choose User defined.
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In the text field, type CO2(g).
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Click
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In the Settings window for Global, click Replace Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1)>Reaction Engineering>re.c_G - Concentration - mol/m³.
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Click Add Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1)>Reaction Engineering>re.c_M - Concentration - mol/m³.
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Click Add Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1)>Reaction Engineering>re.c_N - Concentration - mol/m³.
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In the Settings window for Global, click Replace Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1)>Definitions>Variables>Evol - vol% alcohol.
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Locate the Plot Settings section. In the y-axis label text field, type Concentration (mol/m<sup>3</sup>).
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In the Settings window for Global, click Replace Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1)>Reaction Engineering>re.c_X - Concentration - mol/m³.
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In the Settings window for Global, click Replace Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1)>Reaction Engineering>re.c_EtAc - Concentration - mol/m³.
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Click Add Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1)>Reaction Engineering>re.c_AcA - Concentration - mol/m³.
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Locate the Legends section. In the table, enter the following settings:
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Locate the Physics Interfaces section. Find the Fluid flow subsection. From the list, choose Laminar Flow: New.
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In the Model Builder window, under Component 2 (comp2)>Multiphysics click Nonisothermal Flow 1 (nitf1).
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Click
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In the tree, select Built-in>Air.
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In the tree, select Built-in>Copper.
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In the Model Builder window, under Component 2 (comp2) right-click Definitions and choose Variables.
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Browse to the model’s Application Libraries folder and double-click the file beer_fermentation_variables2.txt.
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In the Model Builder window, expand the Transport of Diluted Species (tds) node, then click Component 2 (comp2)>Heat Transfer in Fluids 1 (ht).
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In the Model Builder window, under Component 2 (comp2)>Heat Transfer in Fluids 1 (ht) click Heat Source 1.
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Locate the Model Input section. Click Make All Model Inputs Editable in the upper-right corner of the section.
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Locate the Physics and Variables Selection section. In the table, clear the Solve for check boxes for Chemistry 1 (chem) and Transport of Diluted Species (tds).
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In the table, select the Solve for check boxes for Chemistry 1 (chem) and Transport of Diluted Species (tds).
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In the Model Builder window, expand the Study 2>Solver Configurations>Solution 2 (sol2)>Dependent Variables 1 node, then click Concentration (comp2.cAcA).
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In the Model Builder window, under Study 2>Solver Configurations>Solution 2 (sol2)>Dependent Variables 1 click Concentration (comp2.cEtAc).
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In the Model Builder window, under Study 2>Solver Configurations>Solution 2 (sol2)>Dependent Variables 1 click Concentration (comp2.cM).
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In the Model Builder window, under Study 2>Solver Configurations>Solution 2 (sol2)>Dependent Variables 1 click Concentration (comp2.cN).
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In the Model Builder window, under Study 2>Solver Configurations>Solution 2 (sol2)>Dependent Variables 1 click Concentration (comp2.cX).
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In the Model Builder window, under Study 2>Solver Configurations>Solution 2 (sol2)>Dependent Variables 1 click Pressure (comp2.p).
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In the Model Builder window, under Study 2>Solver Configurations>Solution 2 (sol2)>Dependent Variables 1 click Temperature (comp2.T).
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In the Model Builder window, under Study 2>Solver Configurations>Solution 2 (sol2) click Time-Dependent Solver 1.
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In the Model Builder window, under Results>Datasets right-click Revolution 2D 1 and choose Duplicate.
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In the Model Builder window, under Results>Datasets, Ctrl-click to select Study 2/Wort (sol2) and Revolution 2D - Wort.
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Right-click and choose Duplicate.
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In the Model Builder window, expand the Results>Datasets>Study 2/Tank (sol2) node, then click Selection.
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In the Settings window for 2D Plot Group, type Velocity Field and Temperature in the Label text field.
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Click Define custom colors.
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Click Add to custom colors.
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Click Define custom colors.
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Click Add to custom colors.
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Locate the Arrow Positioning section. Find the r grid points subsection. In the Points text field, type 10.
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In the Model Builder window, expand the Results>Concentration, AcA, 3D (tds) node, then click Concentration, AcA, 3D (tds).
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In the Model Builder window, under Results>Concentration, AcA, 3D (tds) right-click Surface 1 and choose Duplicate.
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In the Settings window for 3D Plot Group, type Concentration, AcA (Acetaldehyde) in the Label text field.
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Click Replace Expression in the upper-right corner of the Expression section. From the menu, choose Component 2 (comp2)>Heat Transfer in Fluids 1>Domain fluxes>ht.tefluxr,...,ht.tefluxz - Total energy flux.
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Clear the Point check box.
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Locate the Legends section. Find the Prefix and suffix subsection. In the Suffix text field, type , Bottom.
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Select the Plot check box.
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