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March 18, 2023, 03:11 |
relative acceleration implementation cfx
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#1 |
New Member
libya
Join Date: Aug 2022
Posts: 15
Rep Power: 3 |
hi everybody,
my issue is implementation of acceleration of droplet or bubble in eulerian multiphase mixture model.the error returned is slip velocity u,w,v does not have a required component prefix.if add phase prefix another error is not allowed to have a phase prefix.i tried all prefixes,components but no luck.i know that the local derivative needs user_getvar but itis not my problem.the problem is how implement it in CFX CEL language Last edited by gyr; March 19, 2023 at 03:28. |
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March 18, 2023, 04:02 |
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#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,703
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Can I ask why do you want the slip velocity acceleration?
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March 18, 2023, 04:14 |
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#3 |
New Member
libya
Join Date: Aug 2022
Posts: 15
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to calculate dispersed phase size
Last edited by gyr; March 21, 2023 at 03:20. |
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March 18, 2023, 04:51 |
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#4 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,703
Rep Power: 143 |
Can you define your terms? What is rmax b, rmax d, Erds, accel delta rho etc?
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Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum. |
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March 18, 2023, 04:58 |
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#5 |
New Member
libya
Join Date: Aug 2022
Posts: 15
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density difference between air and water.for equations rmax b , rmax d ara maximum droplet size and maximum bubble size in metre.sigma is interfacial tension
Last edited by gyr; March 21, 2023 at 03:20. Reason: explanation |
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March 18, 2023, 05:01 |
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#6 |
New Member
libya
Join Date: Aug 2022
Posts: 15
Rep Power: 3 |
Accel is the acceleration to be required
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