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Click Add.
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In the Select Physics tree, select Electrochemistry > Primary and Secondary Current Distribution > Secondary Current Distribution (cd).
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Browse to the model’s Application Libraries folder and double-click the file fountain_flow_parameters.txt.
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Select the Swirl flow checkbox.
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In the Model Builder window, under Component 1 (comp1) > Laminar Flow (spf) click Fluid Properties 1.
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Select the Sliding wall checkbox.
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Specify the u vector as
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In the Model Builder window, under Component 1 (comp1) > Secondary Current Distribution (cd) click Electrolyte 1.
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Locate the Electrode Kinetics section. From the Kinetics expression type list, choose Butler–Volmer.
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In the Model Builder window, under Component 1 (comp1) > Transport of Diluted Species (tds) click Species Charges.
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In the Model Builder window, expand the Electrode Surface Coupling 1 node, then click Reaction Coefficients 1.
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Locate the Normal Current Density section. From the in list, choose Local current density, Electrode Reaction 1 (cd/es1/er1).
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Locate the Element Size Parameters section.
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In the Settings window for Transport of Diluted Species, click to expand the Discretization section.
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In the Settings window for Secondary Current Distribution, click to expand the Discretization section.
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In the Solve for column of the table, under Component 1 (comp1), clear the checkboxes for Transport of Diluted Species (tds), Secondary Current Distribution (cd), and Electrode, Shell (els).
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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 Streamline, click Replace Expression in the upper-right corner of the Expression section. From the menu, choose Component 1 (comp1) > Laminar Flow > Velocity and pressure > u,w - Velocity field.
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Click Replace Expression in the upper-right corner of the y-Axis Data section. From the menu, choose Component 1 (comp1) > Secondary Current Distribution > Electrode kinetics > cd.iloc_er1 - Local current density - A/m².
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