I‘m now simulating the gasoline-liquid two-section movement in vertical pipe. I have penned UDF like regulate function and diffusivity perform. When i loaded the alter purpose, the case is often calculated.On the other hand, at the time i added the diffusivity function, the mistake appeared as revealed down below:
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I must point out that the combustion with MHD equation was solved with no Lorenz Force and Joule Heating, but as I turned on Lorenz power the answer procedure stopped Performing (with b_0 Scale aspect of 0.1).
I'm engaged on Home windows seven and starting off fluent in parallel. When it really is began I've it go through a journal file which sets up the appropriate configurations and after that proceeds into a do loop. This do loop runs 1 time stage and then create to a control file. This works by alone.
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I wish to export the strain at just about every node inside the mesh immediately after Each individual time stage. I wrote a plan function to do so. This also operates by alone.
Partly 2, I talked about how picking out the proper hard drive can help speed up your analyses. Finite ingredient analyses study and publish huge quantities of knowledge on the disk, so everything we are able to do for making that...
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Check with someone to modify you model and UDF if It is your 1st time to manage period transform or meet up with this dialog.
I solved this problem by reinstalling ANSYS. I bought a contemporary copy from the consultant in Middle East and Africa as my university has a tutorial license and I finished having the issue.
Once i used magnetic industry for chilly move (combustion design is off), the challenge converged without any error. And Once i turned off magnetic issue the combustion is converged. In other word, but I can't Incorporate the two of these.
it not easy to say about this mistake for the reason that this is available in most of the instances when their is some error so i proposed you that be sure to undergo fluent manual and take a look read this post here at to determine you error. you might observe my previously submit that might be help you.
Good day Saidul, desire i may be of fantastic help with regards to your UDF. I will nevertheless advice that before you decide to Develop, load the functionality And at last hook the UDF, you fish out each mistake in C file.
Am not really applying UDF in my case. Am fixing a dilemma which requires melting, evaporation and fuel section reaction. I have enabled multiphase VOF, melt & solidification and species transport.
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Have you been employing an UDF? These types of mistake concept reveals up only when you are trying to entry some interior variables of FLUENT solver within the UDF which are not actually obtainable through the respective macro plan system.
I was capable to get this to work in serial so I think it has something to do with running fluent in parallel but I do not understand how to resolve it.