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#1 |
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Senior Member
Join Date: Mar 2013
Location: Germany
Posts: 357
Rep Power: 15 ![]() |
Hi All
I am doing a simple in-compressible flow (water as medium) inside a twisted pipe/cylinder. Here I am doing an LES computation using CFX and for that I am confused on what basis I should give my mesh size and time step. And can use Hex mesh or Tetrahedrals ? The flow inlet is 5 bar and mass flow rate is 10 l/min The geometry is total lenght of 30 mm, Inlet diameter of the pipe is 7mm after 20mm distance the pipe is twisted and a difuser is connected at the end to act like a nozzle. Based on the flow conditions we can say the Reynolds number is around 10000 So in this case I am confused how to decide the mesh size and the time step. Kindly give me some advice please. Thanks |
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#2 |
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Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 18,010
Rep Power: 146 ![]() ![]() ![]() ![]() |
Hex or tets: Either can work, but hexas have less dissipation providing you can make them high quality. Dissipation is very important in LES models.
For LES you should set your mesh size as a function of the Taylor length scale of the turbulence. With a low Re flow that will hopefully be fairly large which will help. |
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#3 |
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Senior Member
Join Date: Mar 2013
Location: Germany
Posts: 357
Rep Power: 15 ![]() |
Hi Glenn
Thanks a lot for the information. But as I said my Re number at the inlet is around 10000 but there is a diffuser at the outlet side where the velocity is higher compared to the inlet pipe. So in this case the Re will be higher at that region compared to the inlet. But out of all these how can we decide that this is what the minimum (dx) should be : How we can calculate and then when it comes to (dt) based on CFL condition should the ratio be less than or equal to 0.5 ? Then I am facing an issue with the HEX mesh with multizone in Ansys mesh: The mesh doesnt generate an inflation layer and the mesh is clumsy in the central axis along the flow (I can see that when I do the cut sectional view) !! |
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#4 |
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Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 18,010
Rep Power: 146 ![]() ![]() ![]() ![]() |
Estimate the Taylor length scale from the turbulence conditions. That is a good estimate for your mesh size. Then do a mesh sensitivity study to check it.
Rather than using a CFL based time step I recommend you use adaptive time stepping homing in on 3-5 coefficient loops per iteration. Try the geometry and meshing forum for the mesh questions. |
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#5 |
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Senior Member
Join Date: Mar 2013
Location: Germany
Posts: 357
Rep Power: 15 ![]() |
Hi Glenn
Thanks for your message. But as you mentioned to calculate the Taylor Length Scales from Turbulence quantities, could you elaborate the process I could do it ? I am still not sure how to calculate it. And I am doing LES directly and not based on my RANS or URANS. Thanks in advance. |
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#6 |
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Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 18,010
Rep Power: 146 ![]() ![]() ![]() ![]() |
A turbulence textbook like "Turbulence Modelling for CFD" by Wilcox is essential reading before contemplating LES work. It will show the derivations of Taylor length scales and all the other parameters you need.
You need an initial estimate of the turbulence conditions so you know the turbulence properties so you can design the simulation properly to do the simulation. So you should do an initial simulation, preferably URANS, to get an estimate of the turbulence properties, which you can then use to set up your LES simulation. |
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