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Volumetric Heat generation in cylinder with natural convection conjugate heat transfe |
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August 8, 2017, 08:35 |
Volumetric Heat generation in cylinder with natural conv & conjugate heat transfer
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#1 |
New Member
Texas
Join Date: Apr 2017
Posts: 4
Rep Power: 9 |
Hi to All OpenFoam Users,
I am new to OpenFoam. I am trying to setup case where it involves conjugate heat transfer with volumetric heat generation in solid cylinder and heat is exchanged with fluid through natural convection. I have already set up case and you can find in given tar file. The problem is centreline of solid cylinder always shows minimum temperature as compared to domain. Result file picture is shown in attached picture. I am not sure, where I am going wrong. You all are kindly requested to help me in this regard. Thanks in advance! Last edited by sandymech; August 12, 2017 at 19:03. |
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December 1, 2017, 11:57 |
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#2 |
New Member
Andrew Stubblefield
Join Date: Aug 2016
Posts: 3
Rep Power: 10 |
Hello,
I am also new to OpenFOAM. Your case is interesting to me, and I would like to duplicate it on my own system for analysis. However, I am unable to successfully execute the case as is. Possibly, I am making some mistake, but I wonder if the issue could be due to differing versions of OpenFOAM. Can you please provide your OpenFOAM version as well as what post-processor you are using and its version? Thank you. |
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December 1, 2017, 12:03 |
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#3 |
New Member
Sandy
Join Date: Aug 2017
Posts: 8
Rep Power: 9 |
Hi Andrew,
Openfoam version - 4.1 Paraview - 5.4.1 If you can send me error message, I can help you out. If you are using Openfoam 5.0 then you may have to change in fvOptions file for Tmin and Tmax , you may have to write min and max respectively. Thanks, Sandeep |
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December 1, 2017, 12:22 |
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#4 | ||
New Member
Andrew Stubblefield
Join Date: Aug 2016
Posts: 3
Rep Power: 10 |
Sandeep,
Thank you for the reply. I am using OpenFOAM 2.4 - perhaps I need to upgrade.... I have actually encountered a couple of errors already, the first having to do with decomposing and reconstructing the case. I only have 2 processors, so I modified the appropriate lines in the deconstructPar files. My system seems to be decomposing the case correctly between the 2 processors, but I get the following error in log.reconstructPar: Code: Quote:
Code: Quote:
Thanks, Andrew |
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December 2, 2017, 15:20 |
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#5 |
New Member
Sandy
Join Date: Aug 2017
Posts: 8
Rep Power: 9 |
Try to upgrade OPENFOAM4.0 and let me know if there is any problem.
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December 5, 2017, 12:55 |
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#6 | ||||
New Member
Andrew Stubblefield
Join Date: Aug 2016
Posts: 3
Rep Power: 10 |
Hi Sandeep,
I have upgraded to OpenFOAM 4.1, and Paraview 5.0.1. I am also using a different machine now that has 4 processors, so I have not made any changes to your original case files. Now when I run the case, I am getting the following errors: Error in log.changeDictionary.fluid: Code: Quote:
Code: Quote:
When I attempt to open "cylnatural_send.OpenFOAM" in Paraview, I can't see any data, and I get the following error messages: Code: Quote:
Code: Quote:
My end result in Paraview looks very similar to the original picture you posted - maximum temp is on the outside of the cylinder and the center of the cylinder has minimum temperature of 300K. There is one notable exception though - the maximum temperature is only 302K instead of 556K as shown in your picture. Any advice you can offer on what is going wrong would be greatly appreciated. Thanks, Andrew |
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December 6, 2017, 04:48 |
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#7 |
Senior Member
Agustín Villa
Join Date: Apr 2013
Location: Alcorcón
Posts: 314
Rep Power: 15 |
Hi. I saw in your 0/solid/T:
Code:
dimensions [ 0 0 0 1 0 0 0 ]; internalField uniform 300; boundaryField {solid_to_fluid {}type compressible::turbulentTemperatureCoupledBaffleMixed; value uniform 300; kappaMethod solidThermo; kappaName none; Tnbr T;} |
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December 9, 2017, 08:29 |
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#8 |
New Member
Sandy
Join Date: Aug 2017
Posts: 8
Rep Power: 9 |
Hi Andrew,
To reach 500K or more temperature, you may have run the case for end time like 2000. For error in changedictionary file, you may have to copy epsilon and k file from any other case file to 0/fluid e.g. Assuming working directory is case directory, you can use following commands cp ../heatExchanger/0.orig/air/k 0/fluid/ cp ../heatExchanger/0.orig/air/epsilon 0/fluid/ Thanks, Sandeep |
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December 10, 2017, 08:34 |
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#9 |
Senior Member
Join Date: Sep 2013
Posts: 353
Rep Power: 21 |
I have not tested it, but this seems mesh related. Try changing your cylinder mesh from a wedge type at the center to something else.
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January 9, 2018, 07:12 |
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#10 |
Member
Çağatay Emre Ayhan
Join Date: Sep 2017
Location: Istanbul, Turkey
Posts: 31
Rep Power: 9 |
Hello Sandy, I am a graduate student and I need to solve a similar problem by using openFOAM as my computational methods class project. Is it possible to solve this problem unsteady by using chtMultiRegionSimpleFoam. I want to solve it unsteady because I need to validate the results with results in the literature. Results in the litearature are unsteady. Or do you have any steady results. I need to compare my results with them. Thank you very much.
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Tags |
conjugate heat transfer, cylinder, heat generation, natural circulation, openfoam |
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