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January 18, 2012, 18:19 |
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#21 |
New Member
Athanasios Papadopoulos
Join Date: Jan 2012
Posts: 23
Rep Power: 14 |
Ι upload the pictures as you asked me (PNG files).I hope now they will be readable. I also 've done what you told me above by the problem still the same
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January 18, 2012, 18:20 |
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#22 |
New Member
Athanasios Papadopoulos
Join Date: Jan 2012
Posts: 23
Rep Power: 14 |
And take a look also to this one.I hope I help you enough.If not I am steel here, as me what ever you want
Thanks again |
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January 18, 2012, 18:48 |
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#23 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,703
Rep Power: 143 |
The image problem is that they are being shrunk somewhere.
The problem is the way you have set things up in CFX-Pre, so fix the problem there, not WB. My last post said you used the wrong variable names. Have you fixed that? |
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January 19, 2012, 07:53 |
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#24 |
New Member
Athanasios Papadopoulos
Join Date: Jan 2012
Posts: 23
Rep Power: 14 |
Yes, I fixed that problem and the results are still the same.I thing by the way you see the geometry, you can just send me What would you do if you were in my shoes In a transient state and with one inlet (boundaryressure) and two outlet (boundaries: mass flow rate).I' ve done exactly what I need to do in the function setup according to the file that I found (how to setup a function in 1D interpolation).
The solver not even start.The graph that you see from the solver int the pictures is from a steady state and simple (one inlet "100 kPa" pressure and two outlet 0.035Kg/s each).And after that I change exactly everything and here we are now. |
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January 22, 2012, 06:34 |
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#25 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,703
Rep Power: 143 |
Can you post your CCL file for the current simulation?
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January 22, 2012, 11:51 |
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#26 |
New Member
Athanasios Papadopoulos
Join Date: Jan 2012
Posts: 23
Rep Power: 14 |
I am trying to upload the file,but it doesn't accepted it.Probably because of the size.Is there any other way?
I was trying to upload the file with the simulation, because I don't know exaclty which one is the CCL file where you asked me. Thanks |
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January 22, 2012, 17:49 |
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#27 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,703
Rep Power: 143 |
The CCL file is the top section of the output file. If the output file (with the startup error) is short then just upload that.
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January 22, 2012, 20:23 |
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#28 |
New Member
Athanasios Papadopoulos
Join Date: Jan 2012
Posts: 23
Rep Power: 14 |
Look I finally found some issues to solve my problem, but now duirng the running of the solver, suddenly in the middle it stop and give me the below error:
| The fluid name is: Fluid 1. | | If this situation persists, consider switching | | to an Opening type boundary condition instead. | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | ****** Notice ****** | | A wall has been placed at portion(s) of an OUTLET | | boundary condition (at 2.9% of the faces, 0.9% of the area) | | to prevent fluid from flowing into the domain. | | The boundary condition name is: outlet. | | The fluid name is: Fluid 1. | | If this situation persists, consider switching | | to an Opening type boundary condition instead. | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | ****** Notice ****** | | A wall has been placed at portion(s) of an OUTLET | | boundary condition (at 1.6% of the faces, 0.6% of the area) | | to prevent fluid from flowing into the domain. | | The boundary condition name is: outlet2. | | The fluid name is: Fluid 1. | | If this situation persists, consider switching | | to an Opening type boundary condition instead. | +--------------------------------------------------------------------+ | H-Energy | 0.32 | 5.7E-03 | 2.5E-01 | 5.8 1.2E-03 OK| +----------------------+------+---------+---------+------------------+ +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | Floating point exception: Overflow | | | | | | | | | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | Writing crash recovery file | +--------------------------------------------------------------------+ Details of error:- ---------------- Error detected by routine POPDIR CRESLT = ILEG Any idea? Thanks |
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January 23, 2012, 05:41 |
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#29 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,703
Rep Power: 143 |
Can you please post your entire output file?
The error is a typical one - floating point error means you simulation has diverged. You need to improve the numerical stability. Use smaller time steps, a better initial condition, lower order differencing (but switch to higher order for accuracy later), double precision numerics, check your physics in correct, improve mesh quality.... the list goes on.... |
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January 23, 2012, 16:38 |
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#30 |
New Member
Athanasios Papadopoulos
Join Date: Jan 2012
Posts: 23
Rep Power: 14 |
I am trying to upload the file, but it doesn't me,probably because of the size.Can you gine you email (if it's possible), so I will upload the hall file and you can take from there.Because I can't see any other way. Maybe you know
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February 1, 2012, 17:27 |
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#31 |
New Member
Athanasios Papadopoulos
Join Date: Jan 2012
Posts: 23
Rep Power: 14 |
I upload a foto with the content of the CFX file that is created by the software. Check which file you need exaclty so I can sended to you.
Thanks! |
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