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4·104 (J/mol)
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-1.1·105 (J/mol)
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6·104 (J/mol)
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-1·106 (J/mol)
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Click Add.
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Click Add.
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Click Add.
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Click Add.
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In the Concentrations (mol/m³) table, enter the following settings:
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Click
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Browse to the model’s Application Libraries folder and double-click the file plate_reactor_parameters.txt.
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Browse to the model’s Application Libraries folder and double-click the file plate_reactor_geom_sequence.mph.
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Clear the Automatic detection of small details checkbox.
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Locate the Output Entities section. From the Include entity if list, choose Entity intersects cylinder.
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In the Add dialog, in the Selections to add list, choose Cylinder 1, Cylinder 2, Cylinder 3, Cylinder 4, Cylinder 5, and Explicit 1.
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Click OK.
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Go to the Add Material window.
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Click the Add to Component button in the window toolbar.
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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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Clear the Enable formula checkbox.
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Find the Bulk species subsection. From the Species solved for list, choose Transport of Diluted Species.
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In the Model Builder window, under Component 1 (comp1) > Heat Transfer in Fluids (ht) click Initial Values 1.
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In the Model Builder window, under Component 1 (comp1) > Transport of Diluted Species (tds) click Fluid 1.
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Click the Custom button.
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In the Model Builder window, under Component 1 (comp1) > Mesh 1 right-click Free Triangular 1 and choose Duplicate.
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Locate the Physics and Variables Selection section. In the Solve for column of the table, under Component 1 (comp1), clear the checkboxes for Chemistry (chem), Heat Transfer in Fluids (ht), and Transport of Diluted Species (tds).
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In the Solve for column of the table, under Component 1 (comp1) > Multiphysics, clear the checkbox for Reacting Flow, Diluted Species 1 (rfd1).
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In the Settings window for Stationary, type Stationary - Heat and Mass Transfer in the Label text field.
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Locate the Physics and Variables Selection section. In the Solve for column of the table, under Component 1 (comp1), clear the checkbox for Laminar Flow (spf).
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In the Settings window for Color Expression, click Replace Expression in the upper-right corner of the Expression section. From the menu, choose Component 1 (comp1) > Transport of Diluted Species > Species cA > cA - Molar concentration, cA - mol/m³.
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In the Settings window for Slice, click Replace Expression in the upper-right corner of the Expression section. From the menu, choose Component 1 (comp1) > Heat Transfer in Fluids > Temperature > T - Temperature - K.
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Click Replace Expression in the upper-right corner of the Expression section. From the menu, choose Component 1 (comp1) > Heat Transfer in Fluids > Temperature > T - Temperature - K.
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In the Settings window for Isosurface, click Replace Expression in the upper-right corner of the Expression section. From the menu, choose Component 1 (comp1) > Transport of Diluted Species > Species cB > cB - Molar concentration, cB - mol/m³.
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Clear the Plot dataset edges checkbox.
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Go to the Result Templates window.
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In the tree, select Study 1/Solution 1 (sol1) > Transport of Diluted Species > Mole Balance, A (tds), Study 1/Solution 1 (sol1) > Transport of Diluted Species > Mole Balance, B (tds), Study 1/Solution 1 (sol1) > Transport of Diluted Species > Mole Balance, D (tds), and Study 1/Solution 1 (sol1) > Transport of Diluted Species > Mole Balance, U (tds).
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Click the Add Result Template button in the window toolbar.
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Locate the Selections of Resulting Entities section. Find the Cumulative selection subsection. Click New.
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Click OK.
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Select the Keep input objects checkbox.
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Locate the Selections of Resulting Entities section. Select the Resulting objects selection checkbox.
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Locate the Selections of Resulting Entities section. Find the Cumulative selection subsection. From the Contribute to list, choose Object to subtract.
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Locate the Selections of Resulting Entities section. Find the Cumulative selection subsection. From the Contribute to list, choose Object to subtract.
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Select the object blk1 only.
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On the object dif1, select Domain 1 only.
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On the object dif1, select Boundaries 6 and 54 only.
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In the tree, select dif1.
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Select the object pard1 only.
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On the object mir2(1), select Boundary 63 only.
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On the object mir2(2), select Boundary 63 only.
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Click
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On the object arr2(1,1,1), select Boundary 2 only.
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On the object fin, select Boundary 35 only.
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On the object fin, select Boundary 34 only.
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On the object fin, select Boundary 2 only.
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In the Settings window for Box Selection, type Box Selection - Heat Exchanger 1 in the Label text field.
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In the Settings window for Box Selection, type Box Selection - Heat Exchanger 2 in the Label text field.
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In the Settings window for Box Selection, type Box Selection - Heat Exchanger Connection in the Label text field.
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Click
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In the Settings window for Adjacent Selection, type Adjacent Selection - Heat Exchanger 1 in the Label text field.
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Click OK.
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In the Settings window for Adjacent Selection, type Adjacent Selection - Heat Exchanger 2 in the Label text field.
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Click OK.
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Click OK.
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Click OK.
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Click OK.
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Click OK.
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In the Add dialog, in the Selections to add list, choose Box Selection - Heat Exchanger Connection, Heat Exchanger 1, and Heat Exchanger 2.
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Click OK.
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Click
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Click OK.
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Select the Interior boundaries checkbox.
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Click
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In the Settings window for Adjacent Selection, type Interior boundaries Heat Exchanger 2 in the Label text field.
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Locate the Input Entities section. In the Input selections list box, select Box Selection - Heat Exchanger 1.
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Click
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Click
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Click OK.
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In the Add dialog, in the Selections to add list, choose Interior boundaries Heat Exchanger 1 and Interior boundaries Heat Exchanger 2.
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7
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Click OK.
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Click
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