-
-
November 29, 2018 at 11:01 am
uxsarah
SubscriberI am using Polyflow to simulate the mould filling process of a chemical reaction flow, but the computation failed. I have attached the listing File, can any one help? many thanks.
-
November 29, 2018 at 11:04 am
uxsarah
SubscriberRunning vof for T within [ 0.000E+00 , 2.000E+02 ]
with dT-ini = 1.000E-01,
dT-min = 1.000E-02, dT-max = 2.500E-01,
with up to 2000 successful steps,
===> Starting VOF
at T-ini = 0.000E+00
=================================
**************************************************************************
Initial volume = 1.4103619E-04 / 4.1392274E-02
**************************************************************************
Preprocessors
Convergence assumed : Rel. var. LT 1.00000E-04
F.E.M. Task
Global divergence has occured. Diverg = 0.2000000E+04
**************************************************************************
VOF Step #1 | Progress bar(s) |
Time = 0.0000000E+00 |> |
Volume of fluid = 1.4103619E-04 |> |
Volume filled (%) = 3.4073070E-01 |> |
Step status : KO
Solver divergence occured.
New time step = 5.0000000E-02
**************************************************************************
Preprocessors
Convergence assumed : Rel. var. LT 1.00000E-04
F.E.M. Task
Divergence detected for field Carbondioxide: iterations cancelled by Expert System
Divergence detected for field Urethane: iterations cancelled by Expert System
Global divergence has occured. Diverg = 0.2000000E+04
**************************************************************************
VOF Step #1 | Progress bar(s) |
Time = 0.0000000E+00 |> |
Volume of fluid = 1.4103619E-04 |> |
Volume filled (%) = 3.4073070E-01 |> |
Step status : KO
Solver divergence occured.
New time step = 2.5000000E-02
**************************************************************************
Preprocessors
Convergence assumed : Rel. var. LT 1.00000E-04
F.E.M. Task
*** WARNING *** from [fpow]
Negative local temperature for power law. Stop.
*** WARNING *** from [mat162]
Evaluation of the reaction rate has failed. Stop.
*** WARNING *** from [MATRIX]
Information about the above trouble...
for problem Reaction rate 2D
on domain: SURFACE_BODY.
near location : ( 0.23946E+00 , 0.92221E-01 )
Global divergence has occured. Diverg = 0.2000000E+04
**************************************************************************
VOF Step #1 | Progress bar(s) |
Time = 0.0000000E+00 |> |
Volume of fluid = 1.4103619E-04 |> |
Volume filled (%) = 3.4073070E-01 |> |
Step status : KO
Solver divergence occured.
New time step = 1.2500000E-02
**************************************************************************
Preprocessors
Convergence assumed : Rel. var. LT 1.00000E-04
F.E.M. Task
Divergence detected for field Urea: iterations cancelled by Expert System
Global divergence has occured. Diverg = 0.2000000E+04
**************************************************************************
VOF Step #1 | Progress bar(s) |
Time = 0.0000000E+00 |> |
Volume of fluid = 1.4103619E-04 |> |
Volume filled (%) = 3.4073070E-01 |> |
Step status : KO
Solver divergence occured.
New time step = 6.2500000E-03
**************************************************************************
Preprocessors
Convergence assumed : Rel. var. LT 1.00000E-04
F.E.M. Task
Global divergence has occured. Diverg = 0.2000000E+04
**************************************************************************
VOF Step #1 | Progress bar(s) |
Time = 0.0000000E+00 |> |
Volume of fluid = 1.4103619E-04 |> |
Volume filled (%) = 3.4073070E-01 |> |
Step status : KO
Solver divergence occured.
New time step = 3.1250000E-03
**************************************************************************
*******************************
* Summary of the simulation *
*******************************
The computation failed.
*****************************
* Expert tool diagnostics *
*****************************
Computation can not start, time step becomes too small at the first
step.
Maybe there is a problem is your set up. Please, review it.
*****************************
* Expert tool diagnostics *
*****************************
Out of convergence disk
*****************************
* Expert tool diagnostics *
*****************************
The problem F.E.M. Task has not converged.
*****************************
* Expert tool suggestions *
*****************************
A serious internal error has occured (in printEndOfVof).
Please, contact Ansys Polyflow support, and send us, if possible the
mesh, data and listing files.
We apologize for the inconvenience. -
November 29, 2018 at 11:14 am
uxsarah
Subscriber
Is there anything wrong with my folling settings?
VOF iterative parameters:
Initial time value =0
Upper time limit= 2.000E2
Initial value of the time step= 1.000E-1
Min admissible value of the time-step = 1.000E-2
Max admissible value of the time-step = 2.500E-01
Accuracy of VOF scheme =2.500E-01
Max number of successful steps =2000
Viewing 2 reply threads- The topic ‘“The computation failed” when I use Polyflow to simulate filling process of chemical reaction flow’ is closed to new replies.
-
-
5844
-
1906
-
1420
-
1305
-
1021
© 2026 Copyright ANSYS, Inc. All rights reserved.