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Newtons method failed to converge in 100 iterations |
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September 2, 2011, 13:21 |
Newtons method failed to converge in 100 iterations
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#1 |
New Member
Bostjan
Join Date: Apr 2009
Posts: 24
Rep Power: 17 |
hey all, after giving all boundary condition for gas combustion, i got following error during solver. Please help me to understand this error.
Anybody are experienced in this? any suggestion on this problem? Parallel run: Received message from slave ----------------------------------------- Slave partition : 3 Slave routine : NEWT_FIT Master location : End of Continuity Loop Message label : 009100013 Message follows below - : +--------------------------------------------------------------------+ | ****** Notice ****** | | Newtons method failed to converge in 100 iterations. This | | occurred while computing the following variable: | | | | Variable Name : Temperature | | Location Name : Default Domain | | Mesh location : VERTICES | | Mesh entity : | | Last 3 Changes : 1.64457E-01 1.64457E-01 1.64457E-01 | | Tolerance : 1.0000E-02 | | | | The Newton iteration was either slowly converging or has stalled. | | The solver will continue with the variable set as it was on the | | final iteration. If this situation continues you might try | | increasing the number of iterations allowed for Newtons method. | | This can be changed by setting one of the parameters: | | | | Temperature : "Constitutive Relation Iteration Limit" | | Pressure : "Newton Pressure Iteration Limit" | | | | for your mixture using the definition file editor. | +--------------------------------------------------------------------+ |
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September 2, 2011, 19:37 |
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#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
What type of material properties are you using?
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September 3, 2011, 04:10 |
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#3 |
New Member
Bostjan
Join Date: Apr 2009
Posts: 24
Rep Power: 17 |
For Gas Air mixture i used reacting mixture, material group: gas phase combustion, mixture properties: ideal mixture
For O2, CO2, H20,...material properties: ideal gas, NASA format This problem has appeared when i increased heat transfer (heat flux) for 1000- times (from -300 W/m2 to -30 000 W/m2) for wall boundary conditions... Last edited by brajh11; September 3, 2011 at 04:35. |
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September 3, 2011, 06:56 |
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#4 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
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Combustion models are always hard to keep stable. I suspect you will need smaller timesteps to resolve the combustion transient. But that's only a guess.
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September 3, 2011, 07:24 |
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#5 |
New Member
Bostjan
Join Date: Apr 2009
Posts: 24
Rep Power: 17 |
i solved my problem steady state not transient.
For Timescale Control i have changed from Auto Timescale to Physical Timescale 0.008s but now the solver said: +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | Floating point exception: Overflow | | | | | | | | | | | +--------------------------------------------------------------------+ Parallel run: Received message from slave ----------------------------------------- Slave partition : 4 Slave routine : ErrAction Master location : RCVBUF,MSGTAG=1033 Message label : 001100279 Message follows below - : +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | Stopped in routine FPX: C_FPX_HANDLER | | | | | | | | | | | +--------------------------------------------------------------------+ |
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September 3, 2011, 07:29 |
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#6 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
OK, that error message means you have improved things but it still cannot converge. You need smaller time steps.
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