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Centrifugal compressor impeller+vanless diffuser simulation problem.

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Old   March 22, 2017, 12:36
Post Centrifugal compressor impeller+vanless diffuser simulation problem.
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Hi to All

I'm doing the steady state analysis of an Centrifugal compressor with vaneless diffuser. I've done the simulation with solving the entire domain in rotating reference frame and set the shroud and hub of diffuser as counter rotating wall.

Here my problem is, the results indicated that the Total Temperature and enthalpy decrease form the impeller TE Cut to the diffuser outlet, the Tt difference is above 5K. And since the Tt decrease, the polytropic efficiency of impeller &diffuser is even higher than the impeller alone. So the results is definitely inaccurate.

The turbulence model is SST and wall yplus is around 3. Inlet boundary is Pt and Tt, Outlet boundary is average static pressure(results of mass flow rate outlet still have the problem).Alternate Rotating Model is on. I have change the grid and turbulence model, but the phenomenon still exist. I'm stuck here several weeks, wish somebody can help me. Any suggestion? Thank you~
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Old   March 22, 2017, 16:00
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Hello, Do you use TurboGrid and CFX?
Thanks
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Old   March 22, 2017, 20:37
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Quote:
Originally Posted by Ahmed Saeed Mansour View Post
Hello, Do you use TurboGrid and CFX?
Thanks
Yes, V15.0
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Old   March 22, 2017, 21:01
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I have tutorials about a radial turbine..I am not sure if they will help you or not..but you can contact me on 12317@eng.asu.edu.eg to send me the details of your problem...Thanks
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Old   March 24, 2017, 13:27
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Quote:
Originally Posted by MaoZM View Post
Hi to All

I'm doing the steady state analysis of an Centrifugal compressor with vaneless diffuser. I've done the simulation with solving the entire domain in rotating reference frame and set the shroud and hub of diffuser as counter rotating wall.

Here my problem is, the results indicated that the Total Temperature and enthalpy decrease form the impeller TE Cut to the diffuser outlet, the Tt difference is above 5K. And since the Tt decrease, the polytropic efficiency of impeller &diffuser is even higher than the impeller alone. So the results is definitely inaccurate.

The turbulence model is SST and wall yplus is around 3. Inlet boundary is Pt and Tt, Outlet boundary is average static pressure(results of mass flow rate outlet still have the problem).Alternate Rotating Model is on. I have change the grid and turbulence model, but the phenomenon still exist. I'm stuck here several weeks, wish somebody can help me. Any suggestion? Thank you~
Please post the inlet-to-exit averaged plot of your concern.
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Old   March 26, 2017, 23:10
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Have you tried KE model? What turbulence model have you tried? How is the setup of heat transfer? Are you using the option of Total Energy?
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Old   March 27, 2017, 13:10
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Please post the inlet-to-exit averaged plot of your concern.
Here is the Tt and T of 50% spanwise. About 0.7 of streamwise location, is the TE cut, and the Tt decrease in the diffuser.
Chart.png
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Old   March 27, 2017, 13:16
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Originally Posted by doublestrong View Post
Have you tried KE model? What turbulence model have you tried? How is the setup of heat transfer? Are you using the option of Total Energy?
Tried k-e and RNG k-e, still the similar results. Total Energy is used and all the wall are adiabatic.
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Old   March 27, 2017, 20:12
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Try (R1+S1) domains with the impeller rotating up to an immediate downstream of the trailing edge. What you simulated is "the rotating diffuser" case.
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