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July 22, 2020, 14:30 |
How to set the thermal conductivity?
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#1 |
Member
Alex
Join Date: May 2019
Posts: 36
Rep Power: 7 |
I need to know what is the thermal conductivity value of my simulation. I am simulating a natural convection problem using buoyantPimpleFoam, but I do not know where to read k (thermal conductivity).
Is it somewhere in the thermophysical properties? Code:
/*--------------------------------*- C++ -*----------------------------------*\ ========= | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox \\ / O peration | Website: https://openfoam.org \\ / A nd | Version: 6 \\/ M anipulation | \*---------------------------------------------------------------------------*/ FoamFile { version 2.0; format ascii; class dictionary; location "constant"; object thermophysicalProperties; } // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // thermoType { type heRhoThermo; mixture pureMixture; transport const; thermo hConst; equationOfState perfectGas; specie specie; energy sensibleEnthalpy; } pRef 101325; mixture { specie { nMoles 1; molWeight 28.9; } thermodynamics { Cp 1006.591; Hf 0; } transport { mu 1.85e-5; Pr 0.7; } } // ****************************** |
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July 22, 2020, 23:27 |
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#2 |
Senior Member
Fumiya Nozaki
Join Date: Jun 2010
Location: Yokohama, Japan
Posts: 266
Blog Entries: 1
Rep Power: 19 |
Hi,
You might want to check the definition of the Prandtl number (Pr): https://en.wikipedia.org/wiki/Prandtl_number The thermal conductivity k is uniquely identified because the values of mu, Cp and Pr are specified. Hope this helps, Fumiya
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July 23, 2020, 07:05 |
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#3 | |
Member
Alex
Join Date: May 2019
Posts: 36
Rep Power: 7 |
Quote:
That was so helpful! I understood that the value of k that I was using was wrong because I changed mu in my simulation. Then I have another question, what about the Thermal Expansion (Beta)? what are the parameter which affect the value? I ask that because I need it to calculate the Grashof number |
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July 23, 2020, 10:04 |
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#4 |
Senior Member
Fumiya Nozaki
Join Date: Jun 2010
Location: Yokohama, Japan
Posts: 266
Blog Entries: 1
Rep Power: 19 |
Hi Sedullo,
For a perfect gas, the thermal expansion is a inverse of the absolute temperature: https://en.m.wikipedia.org/wiki/Thermal_expansion Hope this helps, Fumiya
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August 28, 2020, 05:27 |
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#5 | |
Senior Member
Huynh Phong Thanh
Join Date: Aug 2013
Location: Ho Chi Minh City
Posts: 105
Rep Power: 13 |
Quote:
If the vicous is sutherland law, does it has relation between k, As, Ts? |
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August 12, 2024, 17:53 |
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#6 |
New Member
John Mary
Join Date: May 2024
Posts: 1
Rep Power: 0 |
Hello,
I am newbie to OpenFOAM and as part of my course I am simulating a gas - solid fluidised bed. I copied the fluidised bed tutorial of the reactingTwoPhaseEulerFoam and modified the geometry to add a horizontal cylindrical heating element close to the inlet. I added the heater patch name to all files in the 0 repository and the simulation is running well. Right now my aim is to modifiy the conductivity model in the energy equation. From all I have read, the thermal conductivity is implicitly defined in the Prandtl number but the problem with this approach is that it sets a uniform thermal conductivity in the bed whereas the conductivity in the bed is not uniform and highly dependent on the volume fraction of the solid particles. I have found some suitable models of effective thermal conductivity but I find it difficult to integrate them in the solver, as OpenFOAM does not perform calculations in the transportProperties file. That is why I have reached out to find if you can help. Kind regards, John |
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thermal conductivity |
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