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Conjugated heat transfer

    • mehdiyahia1
      Subscriber

      Hello, I'm trying to do a simulation of conjugated heat transfer, the source is a 10*10 m2 cube located in a building of 50*50*20 m2, the building is in the atmosphere, my study is stable,realizable k-epsilon, when I checked the results I see that I do not have a semmytey around my cube, if there is an idea to improve the result, I would be very grateful.

    • mehdiyahia1
      Subscriber

    • mehdiyahia1
      Subscriber

    • mehdiyahia1
      Subscriber

    • Rob
      Forum Moderator

      Why do you expect to see a symmetrical result? 

    • mehdiyahia1
      Subscriber

      Thank you for the reply Rwoolhou


      I have unconvincing results when I use the symmetrical. 

    • Rob
      Forum Moderator

      Have a look at von Karman vortex street on Google: you may not have a symmetric flow. 

    • mehdiyahia1
      Subscriber

      I think  Von Karman vortex street, is only for the transient state regime

    • Rob
      Forum Moderator

      Yes and no. How good is your convergence? 

    • mehdiyahia1
      Subscriber

      For the convergence i have 0.1 for all except  epsilon

    • mehdiyahia1
      Subscriber

      Yes and no.  what does that mean?

    • Rob
      Forum Moderator

      It means we can have a transient effect in the results when using the steady solver: it's usually identified by the way the residuals behave.  Just curious, are you using the University licence? 

    • mehdiyahia1
      Subscriber

      Yes i used the university licence . Are you have  some advice explains this phenomenon ?

    • Rob
      Forum Moderator

      Can you post the residuals plot as it's easier to explain if I can see that. We're very limited on here due to export laws, so the more images the less trouble I can get into! 

    • mehdiyahia1
      Subscriber

    • Rob
      Forum Moderator

      Perfect, thanks. 


      I'd be more concerned with the temperature limits if you're not expecting 5000K in the domain, 1K may also be a concern. Open up Solution Controls > Limits and increase the turbulent viscosity ratio by about 4 orders of magnitude.  


      You've also not run anything like enough iterations to converge the solution: run another 500-1000 and let's see how it looks then. 

    • mehdiyahia1
      Subscriber

      I already have a turbulent viscosity 1.

    • Rob
      Forum Moderator

      No, the viscosity ratio limit, not the boundary condition. 

    • mehdiyahia1
      Subscriber

    • Rob
      Forum Moderator

      Yes, that's showing a transient result: or more precisely that the solver is seeing many correct steady state results. Now compare the result from this solution with the plot you added earlier on. 


      I think there's a good solution on our (customer side) system and add the first 10-ish lines of the licence file here so I can find the local ANSYS contact. 


       

    • mehdiyahia1
      Subscriber

      It' s impossible to obtain the university license.

    • mehdiyahia1
      Subscriber

      I don't know if there's any other way you can help me.

    • Rob
      Forum Moderator

      Very simply, you have a solution that's not steady state. You can either use monitors to check the values of interest are fairly stable or switch to transient and use monitors to see how the values of interest change with time. 


      I can't advise on which approach is suitable as I don't know exactly what you're doing and what you need from the results. 

    • mehdiyahia1
      Subscriber

      I want to know the temperature distribution in my domain.

    • mehdiyahia1
      Subscriber

      And the height that reaches the plume.

    • Rob
      Forum Moderator

      And if you monitor those values do they fluctuate?

    • mehdiyahia1
      Subscriber

      Excuse me, but what you mean by monitor?

    • Rob
      Forum Moderator

      In Fluent we can monitor (look through the list of commands in the tree - left side of the interface) data from within the solution. This is often done to check convergence (steady state calculations) or trends in transient. Since you're using 2019Rx click on "Help" and it'll take you to the documentation, from there you'll find the Fluent tutorials. Do the first few as one of those will have monitors as part of the set-up. 

    • mehdiyahia1
      Subscriber

      I have tried all your advice but I am still far from good results.
      Here's my job. https://yadi.sk/d/OkivnVFPTUVtIw


      Can you help me?

    • Rob
      Forum Moderator

      I'm not permitted to open/download attachments. Please post images, and explain why they're not what you're expecting. 

    • mehdiyahia1
      Subscriber

      Now, I use the method of symmetry.
      In the first image, I have a discontinuity in the temperature values.
      In the second image this discontinuity, nor that the temperature is 290, is physically inexplicable.


      if I'm right, how can I explain it? 

    • mehdiyahia1
      Subscriber

    • mehdiyahia1
      Subscriber

    • mehdiyahia1
      Subscriber

      350 K


       


    • mehdiyahia1
      Subscriber

      290 K


    • mehdiyahia1
      Subscriber

      The temperature in the cube is 2000 k

    • Rob
      Forum Moderator

      The surface looks like you're picking up the mesh facets, have you checked you're fully resolving the flow? 

    • mehdiyahia1
      Subscriber

      How can i do it?

    • mehdiyahia1
      Subscriber

      "The surface looks like you're picking up the mesh facets" I don't understand what you mean?

    • Rob
      Forum Moderator

      If you look at the isosurface there are hard edges/features in the shape. This tends to imply the surface is following the mesh, or that the mesh isn't well refined. 


      To check the flow is resolved you either need to know what to look for or do a mesh dependency study.  Note, using symmetry will prevent/alter eddy shedding so you may find you don't get as good agreement with the experiment. 

    • mehdiyahia1
      Subscriber

      This is my mesh.


    • mehdiyahia1
      Subscriber

      As I understand it, work with the symmetry it doesn't recommend in my case.

    • Rob
      Forum Moderator

      That'll explain some/most of the problems. None of the zones are connected (you will have contacts which is OK, just not ideal given how simple the geometry is), and more critically the jump is cell size is awful. Have a look in the documentation tutorials and remesh the model. I suspect the results will be a lot better once you've fixed the mesh. 


      Note, having all good mesh metrics usually means the cells are OK. It does not mean the mesh (ie all the cells) is any good. 

    • mehdiyahia1
      Subscriber

      You're advising me to use ICEM for the mesh (my knowledge is very weak in the mesh).

    • Rob
      Forum Moderator

      No, I'd stick (unite) the volumes together and use Workbench or Fluent Meshing with the watertight geometry workflow. 


      https://www.youtube.com/watch?v=zFsa1Ezot8Y


      ICEM CFD is very good for hex meshes, but not so straightforward to use. 


       

    • mehdiyahia1
      Subscriber

      Thank you very much sir for this helpful video,
      I used Fluent Watertight geometry for the mesh, but I have a problem, I don't have my source in cell zone conditions, in return iin Workbench after DM and Mesh , this problem doesn't exist.

    • mehdiyahia1
      Subscriber

      With Fluent Watertight geometry


       


    • mehdiyahia1
      Subscriber

      With Workbench


       


    • Rob
      Forum Moderator

      Check the zone definitions in Fluent Meshing: they may need defining during the meshing process. 

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