I‘m now simulating the fuel-liquid two-period stream in vertical pipe. I have published UDF including adjust purpose and diffusivity perform. When i loaded the modify operate, the case is often calculated.Nonetheless, once i additional the diffusivity purpose, the mistake appeared as revealed beneath:
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The posting describes the experiment of h2o evaporation from fibrous content (cotton). The fabric is placed during the tube and warm air flows via (means of drying).
Error Item: #f" . Am truly fixing melting, evaporation and response trouble concurrently which i can offer much more specifics should you wanna know far more. Your contribution is going to be A lot appreciated. Thank you
My project is temperature Evaluation of a double pipe helical type warmth exchanger utilizing h2o as fluid.
I don't know if at all possible inside your circumstance, but consider operating your challenge without having UDF 1st, So that you'll be confident if the problem is mainly because of the UDF or not.
I need to export the tension at each individual node within the mesh following Every single time action. I wrote a scheme operate to do so. This also functions by itself.
I do think my error arrived due to the fact I established a contour as considered one of my Remedy animations and, permitted fluent to save lots of a file For each and every iteration.
I'm engaged on a flame influenced by exterior magnetic discipline working with MHD module with fluent 14.five . I'm using compiled UDF to supply non-uniform profile for boundary affliction. My configurations are:
Inquire a person to switch link you model and UDF if It is really your very first time to manage stage adjust or meet up with this dialog.
I solved this problem by reinstalling ANSYS. I obtained a clean copy within the consultant in Center East and Africa as my university has an academic license and I finished getting the problem.
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The UDF is offered below, I could not come across The key reason why for that mistake for a long period. Could everyone do me a favor? Thank you a great deal!!!
Good day Saidul, desire i may be of excellent help with regard to your UDF. I will nonetheless advice that prior to deciding to build, load the operate and finally hook the UDF, you fish out each mistake in C file.
Am not basically utilizing UDF in my case. Am resolving a dilemma which requires melting, evaporation and gas stage response. I have enabled multiphase VOF, melt & solidification and species transportation.
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Are you presently employing an UDF? These types of error information displays up only when you are trying to accessibility some interior variables of FLUENT solver during the UDF which aren't essentially accessible from your respective macro plan application.
I used to be capable to get this to work in serial so I believe it has something to perform with working fluent in parallel but I do not understand how to repair it.