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Boundary condition for transient natural convection |
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June 2, 2013, 09:03 |
Boundary condition for transient natural convection
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Eshita Pal
Join Date: Mar 2012
Posts: 6
Rep Power: 14 |
Hello,
I am using Openfoam 2.2 and trying to simulate natural circulation in a tank with multiple inlets at the bottom and multiple outlets at the top. As I run the transient buoyantBoussinesqPimpleFoam solver, the flow reverses very quickly, and the water starts flowing out of the inlet. Are my boundary conditions appropriate? Thanks. U file dimensions [0 1 -1 0 0 0 0]; internalField uniform (0 0 0); boundaryField { pipe { type fixedValue; value uniform (0 0 0); } inlet1 { type pressureInletOutletVelocity; value uniform (-0.1414 0 0); } inlet2 { type pressureInletOutletVelocity; value uniform (-0.130636565 -0.054111437 0); } inlet3 { type pressureInletOutletVelocity; value uniform (-0.099984898 -0.099984898 0); } outlet { type zeroGradient; } symmetry { type symmetryPlane; } wall { type fixedValue; value uniform (0 0 0); } } p_rgh file dimensions [0 2 -2 0 0 0 0]; internalField uniform 0; boundaryField { pipe { type buoyantPressure; rho rhok; value uniform 0; } inlet1 { type totalPressure; p0 uniform 51.993; // this is equal to g*(height of the tank) U U; phi phi; rho rhok; psi none; gamma 1; value uniform 0; } inlet2 { type totalPressure; p0 uniform 51.993; U U; phi phi; rho rhok; psi none; gamma 1; value uniform 0; } inlet3 { type totalPressure; p0 uniform 51.993; U U; phi phi; rho rhok; psi none; gamma 1; value uniform 0; } outlet { type buoyantPressure; rho rhok; value uniform 0; } symmetry { type symmetryPlane; } wall { type buoyantPressure; rho rhok; value uniform 0; } } |
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boundary condition, natural convection, p_rgh |
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