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The porous media models for one phase flows and multiphase flows use the Superficial Velocity Porous Formulation given that the default. ANSYS FLUENT calculates the the superficial stage or mixture velocities dependant on the volumetric move amount inside a porous area.

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When modeling laminar stream via a packed mattress, the second expression in the above mentioned equation could possibly be dropped, resulting in the Blake-Kozeny equation

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I agree the velocity profile is transforming , but then just isn't the average velocity usually exact at every cross section.

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You need to be considering total strain. And dynamic strain is not going to continue being consistent as being the movement will shift with the pipe. The velocity profile is shifting the dynamic stress will change. At outlet we specify static stress.

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