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May 15, 2010, 03:07 |
Stable Boundary Conditions
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#1 |
Member
Join Date: Feb 2010
Posts: 33
Rep Power: 16 |
Hi,
i'm trying to simulate a 1-1/5 stage turbine. I want to use a profile BC at inlet. But when I use T_tot, velocity x, velocity r, velocity theta, k and epsilon as an inlet profile and average static pressure as an outlet, the solver crashes: "Fatal bounds error detected variable: absolute pressure" how can i use the velocities? because when i use them, i cant specify total pressure at inlet (which i would also have as a profiel data) anymore... what is the way if i want to use T_tot, Velocity -x,-r,-theta, k and epsilon as an inlet profile BC?? Thank you very much!!! |
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May 15, 2010, 08:01 |
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#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,848
Rep Power: 144 |
Have you set the correct reference pressure? Is your boundary pressure correct relative to the reference pressure?
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May 15, 2010, 12:15 |
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#3 |
Member
Join Date: Feb 2010
Posts: 33
Rep Power: 16 |
I set the reference pressure of the domain to "0 atm".
For the inlet I can't specify any pressure (i'm using velocity u, r, theta). There is no option where I can specify for egsample total pressure at inlet. If I use unit velocity direction, than I can specify the pressure at inlet. but not withe the absolut values of the velocity.... At outlet I set 1.1 bar average static pressure... but the solver crashes due to the BC... What can I do? |
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May 16, 2010, 13:37 |
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#4 |
Senior Member
Attesz
Join Date: Mar 2009
Location: Munich
Posts: 368
Rep Power: 17 |
Hi,
the referece pressure should be set near your operating pressures. I think 0 atm is low for a turbine. You should set at least 1 atm. The relative pressure will be (1.1bar-1atm) of course. And I think, you can not set total pressure and velocity at the inlet together, because the equations will be overconstrained. |
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May 17, 2010, 10:35 |
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#5 |
Member
Join Date: Feb 2010
Posts: 33
Rep Power: 16 |
so is this a correct way of setting BC:
inlet: velocity -u, -r, -theta, T_tot, k, epsilon outlet: average static pressure ??? but when i use this, the solver crashes..... what is wrong? |
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May 17, 2010, 10:38 |
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#6 |
Senior Member
Attesz
Join Date: Mar 2009
Location: Munich
Posts: 368
Rep Power: 17 |
The crash can caused by many other problems! what is the error message?
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May 17, 2010, 10:45 |
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#7 |
Member
Join Date: Feb 2010
Posts: 33
Rep Power: 16 |
i tried a lot of different BC setups with the same model, and they all worked..
now i wanted to use velocity components (from measurement) for the inlet. when i use velocity components, no pressure at inlet can be deffined anymore... 1st try: inlet: velocity components, t_tot, k, epsilon (profile BC) outlet: massflow -> error! 2nd try: inlet: velocity components, t_tot, k, epsilon (profile BC) outlet: average static pressure -> same error message: "Fatal bounds error detected variable: absolute pressure" what can i do if i want to use velocity componets at inlet? thank you |
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May 17, 2010, 10:49 |
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#8 |
Senior Member
Attesz
Join Date: Mar 2009
Location: Munich
Posts: 368
Rep Power: 17 |
The BC setting seems to be OK. Check your values, units etc. I have no more idea.
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May 17, 2010, 19:46 |
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#9 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,848
Rep Power: 144 |
The error message is simply saying you are trying to get a negative absolute pressure somehow. Based on the sketchy information you have provided I have no idea where, but somewhere in your setup you are asking for a negative absolute pressure.
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May 18, 2010, 14:03 |
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#10 |
Member
Join Date: Feb 2010
Posts: 33
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I set the reference pressure now to 1bar and the outlet average static pressure to 1.1-1=0.1 bar and it worked...
but don't really know why... anyhow, thank you guys! |
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May 18, 2010, 20:14 |
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#11 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,848
Rep Power: 144 |
Numerical round-off. If you ran using double precision it probably would have worked. But the better solution is to set a reference pressure more representative of the flow average pressure, which is what you have done.
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May 18, 2010, 20:23 |
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#12 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,848
Rep Power: 144 |
Trust me, the problem is caused by numerical round off leading to a convergence problem.
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