I‘m now simulating the gas-liquid two-section movement in vertical pipe. I have penned UDF which includes adjust functionality and diffusivity function. After i loaded the regulate functionality, the case can be calculated.Having said that, once i extra the diffusivity function, the error appeared as proven below:
In fact, what sorts of UDF you might be using? Can be I am able to help you out. It is possible to share your UDF and then I'll take a look.
I should point out which the combustion with MHD equation was solved without Lorenz Force and Joule Heating, but as I turned on Lorenz drive the solution procedure stopped Operating (with b_0 Scale element of 0.one).
I am working on Windows seven and commencing fluent in parallel. After it's commenced I've it read through a journal file which sets up the appropriate options after which proceeds to some do loop. This do loop operates one time phase and afterwards compose to a Regulate file. This is effective by itself.
My project is temperature Investigation of the double pipe helical sort heat exchanger working with drinking water as fluid.
I don't know if possible in your scenario, but test operating your issue with out UDF first, So that you'll be confident if the situation is due to UDF or not.
I need to export the strain at each individual node while in the mesh after each time step. I wrote a plan function to take action. This also is effective by alone.
Partly 2, I reviewed how deciding on the proper harddrive can help speed up your analyses. Finite ingredient analyses browse and produce big amounts of information to the disk, so something we can easily do to help make that...
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Question anyone to change you product and UDF if It can be your very first time to deal with phase transform or satisfy this dialog.
Is there any basic approach to introduce a fresh method in ANSYS FLUENT ? I am NOT superior in C++ language... Make sure my explanation you help and guidebook..
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it hard to say about this error because this comes in many of the instances when their is some mistake so i recommended you that be sure to undergo fluent handbook and check out to determine you slip-up. it's possible you'll adhere to my before post That may be help you.
Hello Saidul, wish i can be of wonderful help with regard to your UDF. I'll even so guidance that before you Make, load the function and finally hook the UDF, you fish out every single error in C file.
Am not actually applying UDF in my situation. Am solving a problem which entails melting, evaporation and fuel section reaction. I have enabled multiphase VOF, melt & solidification and species transport.
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Will you be utilizing an UDF? These mistake message shows up only when you are trying to accessibility some inside variables of FLUENT solver during the UDF which aren't actually accessible from your respective macro regime application.
I had been capable to get this to operate in serial so I do think it has a thing to complete with functioning fluent in parallel but I do not learn how to resolve it.