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[Sponsors] |
January 21, 2009, 11:51 |
Hi Gijsbert,
thank you !
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#21 |
New Member
Peter Weinhaus
Join Date: Mar 2009
Posts: 5
Rep Power: 17 |
Hi Gijsbert,
thank you ! Its working (but with k -> 0 2 -1 0 0 0 0) I am using the nonNewtonianIcoFoam solver. Its running but not very stable. |
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October 18, 2010, 06:10 |
very important
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#22 |
Senior Member
Join Date: Sep 2010
Posts: 226
Rep Power: 17 |
Hi Foamers,
i built already my own viscosityModel and all is ok But i face a huge problem now what to do? i need to use two different transportModels in the same solver. How this can be done and compiled? how to call back the two different viscosities from their models inside the solver, let's say icoFoam? thanks a lot |
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March 19, 2013, 05:06 |
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#23 |
Senior Member
Dongyue Li
Join Date: Jun 2012
Location: Beijing, China
Posts: 848
Rep Power: 18 |
Hi,
Does anyonw know what does k and tau0 mean? { transportModel HerschelBulkley; rho rho [ 1 -3 0 0 0 0 0 ] 900; HerschelBulkleyCoeffs { nu0 nu0 [ 0 2 -1 0 0 0 0 ] 11; tau0 tau0 [ 0 2 -2 0 0 0 0 ] 0.01;//m2/s2 k k [ 0 2 -1 0 0 0 0 ] 0.2; n n [ 0 0 0 0 0 0 0 ] 0.12; } tau0 is tau/density? but k's deminsion is the same with nu,which should be pas^n? |
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October 16, 2013, 04:38 |
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#24 | |
Senior Member
Albrecht vBoetticher
Join Date: Aug 2010
Location: Zürich, Swizerland
Posts: 240
Rep Power: 17 |
Quote:
But there is a nice principal problem: When your fluid accelerates and the shear rate rises, you get a high dependency to timestep size, because the error from overestimation of viscosity over the timestep length sums up! Simulating flume experiments with release boxes using interFoam can demonstrate this. |
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