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May 30, 2016, 07:34 |
Why mass flow is 0?
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#1 |
New Member
Liang shuai
Join Date: Nov 2015
Posts: 13
Rep Power: 11 |
I built several domains to calculate the an steam impingement from a orifice to a porous media.
But as soon as I finished the calculation. I fond a problem is that the mass flow from inlet is not equal to the out. As it is shown in the picture and it is marked as red. The outlet is 0 and I have checked the settings of CFX and I can not find any error. The other results is just as I expected, such as temperature and viscosity. But I cannot find where is wrong about the mass flow. Thank you for your help! |
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May 30, 2016, 08:00 |
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#2 |
Senior Member
Maxim
Join Date: Aug 2015
Location: Germany
Posts: 413
Rep Power: 13 |
please share more information about your project. Attach screenshots and your out-file.
Do you have defined the interfaces between the domains properly? |
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May 30, 2016, 10:19 |
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#3 | |
New Member
Liang shuai
Join Date: Nov 2015
Posts: 13
Rep Power: 11 |
Quote:
I have defined the interfaces between the domains, but I am not sure about if it is properly. I have some supplementary information in the attachment. The first pic shows the interface I set up. The yellow circle is the interface domain, which is the end of the orifice (orifice outlet). The second pic is the set up of inlet conditions. |
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May 30, 2016, 10:23 |
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#4 |
Senior Member
Maxim
Join Date: Aug 2015
Location: Germany
Posts: 413
Rep Power: 13 |
your ccl and/or out file would help us more The out-file is generated by the solver manager and has the same name as your res file.
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May 30, 2016, 10:48 |
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#5 | |
New Member
Liang shuai
Join Date: Nov 2015
Posts: 13
Rep Power: 11 |
Quote:
Thank you! |
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May 31, 2016, 11:57 |
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#6 | |
Senior Member
Join Date: Jun 2009
Posts: 1,873
Rep Power: 33 |
Your solution has not converged yet.. Far from it.
You can check the mass imbalance for the domain "fabric backside" and "fabric front", and the continuity equation has not been fully satisfied. In addition, the message for stopping the run says: Quote:
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May 31, 2016, 13:07 |
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#7 | |
New Member
Liang shuai
Join Date: Nov 2015
Posts: 13
Rep Power: 11 |
Quote:
The file I uploaded is a pilot test with a low number of mesh to obtain the results quickly. So the the residuals did not converge. But I think it is enough to have a preliminary result. Further more, I have another calculation with a quite ideal convergence with 10^-5 residual. The problem I met, is that I set the orifice inlet a mass flow rate(1.333e-3), and at the end of orifice, where is the interface with another domain, whose mass flow rate is 0! Other results is just as I expected, for example, the temperatture. I have checked all the settings of my CFX Pre. But I cannot find the reason. Very gloomy. |
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May 31, 2016, 13:27 |
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#8 |
Senior Member
Join Date: Jun 2009
Posts: 1,873
Rep Power: 33 |
It is very difficult to help w/o looking at some diagnostics, and with limited information.
Have you looked at the flow near the interface of concern ? If you have 50% flow in one direction, and 50% in the opposite, the net mass flow is still 0. Have you look at the mass imbalances throughout the system? i.e. look at every interface downstream. What do the streamlines from the inlet look like ? |
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June 1, 2016, 03:10 |
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#9 | ||
Senior Member
Maxim
Join Date: Aug 2015
Location: Germany
Posts: 413
Rep Power: 13 |
Quote:
Otherwise Opaque is right: your residuals are still too high and your imbalances are not under 1% yet. Especially Quote:
Maybe the number of iterations are not enough for the flow to "reach" the outlet. Streamlines can show you more |
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June 16, 2016, 03:28 |
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#10 |
New Member
Liang shuai
Join Date: Nov 2015
Posts: 13
Rep Power: 11 |
Thank you all!
I have solved the problem. Actually, it is not solved, but searched in the site and I find a similar problem in: http://www.cfd-online.com/Forums/cfx...-rate-cfx.html The mass flow can not be observed at a certain point and it is have to be in a face at least. |
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Tags |
impingement, mass flow rate |
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