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June 27, 2018, 16:36 |
Pump - CFX
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#1 |
New Member
MGE_CFD
Join Date: Jun 2018
Posts: 8
Rep Power: 8 |
Dear,
I am finishing an academic paper and I use CFX. I am simulating a centrifugal pump rotor with the diffuser, the rotor being a rotating domain and the diffuser stationary, the interface is Stage. I am simulating only the blades (rotor with 6 blades and diffuser with 8 blades) using periodicity. With input condition I inform the pressure 0 Pa and the output mass flow, without problems in the setup! The problem is that I did some tests modifying the pitch of the diffuser blades and the result does not change, alias the difference is around 0.5 mca in the pressure and 100 W in the power. I inserted totally divergent angles of the theoretical, almost blocking the passage of the fluid and the result does not change. Could you give me a tip? Thanks |
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June 27, 2018, 18:48 |
Pump CFX
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#2 |
New Member
MGE_CFD
Join Date: Jun 2018
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I do not know if I was clear on the question, but someone could point me some way to try to have differences in the simulation. Example: mesh, setup, etc ...
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June 27, 2018, 19:40 |
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#3 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
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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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June 27, 2018, 20:04 |
Pump CFX
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#4 |
New Member
MGE_CFD
Join Date: Jun 2018
Posts: 8
Rep Power: 8 |
Thanks for the feedback.
I have already made the following changes: mesh refinement, k-epsilon simulation and SST, biphasic simulation with Rayleigh-Plesset model activated and values do not change. I do not know if I could be wrong in the interface with the care of the mesh, but also had no result. |
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June 28, 2018, 02:08 |
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#5 |
Senior Member
urosgrivc
Join Date: Dec 2015
Location: Slovenija
Posts: 365
Rep Power: 12 |
maybe a picture or a bit more info, like are you monitoring Torque on the rotor or what?
it is not posible that the result would stay the same unless something else is set that way. maybe it is the stage interface. Always remember that if something fishy is going on with the simulation it is more than 99% probability that it is the users fault, computers just turn numbers around. |
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June 28, 2018, 10:10 |
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#6 |
Senior Member
Jiri
Join Date: Mar 2014
Posts: 221
Rep Power: 13 |
Send the expressions you use for the evaluation.
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June 30, 2018, 14:09 |
Pump CFX
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#7 |
New Member
MGE_CFD
Join Date: Jun 2018
Posts: 8
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Hi
Pe = massFlow(TotalPressure in Stn Frame)@Inlet Ps = massFlow(TotalPressure in Stn Frame)@Outlet Head = (Ps-Pe)/(998 [kg m^-3]*g) Qo = massFlow |
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June 30, 2018, 14:16 |
Pump CFX
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#8 |
New Member
MGE_CFD
Join Date: Jun 2018
Posts: 8
Rep Power: 8 |
I made this post in the meshing and had no answer, I know that here is not the correct forum, but come on:
The centrifugal pump simulation, I have a rotating (rotor) domain and a stationary (diffuser), but I'm not sure of the mesh of the interface region. I'm using Stage in setup, and the two domains are not in a single body in design modeler, for the reason I'm out of control on the node of each interface. How do I check if the interface region has no influence on my result? |
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July 1, 2018, 07:33 |
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#9 | |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,871
Rep Power: 144 |
Quote:
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum. |
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July 24, 2018, 21:49 |
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#10 |
Member
Join Date: Jan 2015
Posts: 62
Rep Power: 11 |
I think the expression needs to be “massFlowAve” not massFlow
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