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Calculating Pressure Drop in Pipe at High Velocities |
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November 23, 2024, 23:07 |
Calculating Pressure Drop in Pipe at High Velocities
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Hello,
I am working in OpenFoam trying to compute the pressure drop in a piping system. The fluid is air, flowing at ~mach 0.5. I did write my own Python code to analytically solve this, but I want to validate it using CFD. When I try to solve this problem for a short length of pipe (~5 feet), the solver runs all night, and the residuals do not drop at all. What am I missing here? When I open the results in Paraview all I get is the same values for the pressure everywhere. Physics model: Steady-state single phase non-isothermal viscous RANS k-epsilon Fluid: air Pipe size: 76mm Inlet volume flow rate: 1.055 m^3/sec Inlet turbulence intensity: 2.92% inlet length scale: 7mm Outlet boundary: 100,000 Pa Mesh: Snappyhex mesh 8mm base size, prism layers near boundary, 15mm total thickness, 15 cells, 1.1 expansion factor I am a noob at cfd. I am probably missing something simple here. |
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compressible, openfoam |
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