CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT > Fluent Multiphase

Initial setup for inhomgeneous discrete PBM

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   February 6, 2023, 05:17
Default Initial setup for inhomgeneous discrete PBM
  #1
New Member
 
Join Date: Oct 2022
Posts: 5
Rep Power: 4
whydi is on a distinguished road
Hey,


i am trying to simulate a bubble column via multiphase eulerian-eulerian method in combination with inhomogeneous discrete population balance modeling.

I am using 3 secondary air phases and a primary water phase.

Particle size range: (0.0015 -0.0095 m). 3 bins for every sec. phase.


For the initial BC i wanna check three dfferent superficial velocities: 2.5 mm/s, 12 mm/s and 22 mm/s. I am calculation PSD extern with log. normal distribution to split the inlet velocity to the three phases (its recommendes to use inlet vof = 0.5 for inlet BC).


For vel_1 = 2.5 mm/s the simulation is running as expected.
For higher PSD and sup. velocities i get floating point exception:


turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 4500 cells
122 1.4323e+26 1.0931e+01 5.2766e-03 4.2743e-02 6.5920e-03 4.5624e+01 3.3434e-01 5.2486e-01 7.6019e-01 2.0885e-01 2.1696e-01 4.0172e-02 1.2179e-01 7.4441e-01 1.6435e+05 5.8688e-05 1.9009e-05 7.4979e-02 2.4100e-03 5.9303e-05 7.9606e-02 4.7052e-03 4.6173e-04 7.9623e-02 2.8203e-01 1.5422e-01 5.4670e-05 0:00:04 18
Stabilizing vof-1 to enhance linear solver robustness.
Stabilizing vof-2 to enhance linear solver robustness.
Stabilizing vof-3 to enhance linear solver robustness.


turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 4500 cells


iter continuity u-water u-air u-air2 u-air3 v-water v-air v-air2 v-air3 w-water w-air w-air2 w-air3 k-water eps-water bf-0-air bf-0-air2 bf-0-air3 bf-1-air bf-1-air2 bf-1-air3 bf-2-air bf-2-air2 bf-2-air3 vf-air vf-air2 vf-air3 time/iter
123 1.4392e+29 7.7951e+00 1.0062e+00 1.8510e-01 2.5541e-01 1.5516e+01 5.4141e+00 1.4575e-01 1.0989e-01 2.6501e-01 8.7214e-01 1.4717e-01 3.6959e-01 7.0000e-01 3.1568e+07 4.9373e-05 6.3359e-05 2.3793e-03 2.0245e-03 1.1999e-04 1.8620e-03 3.9379e-03 6.6472e-04 1.8626e-03 3.2295e-01 1.1713e-01 1.7408e-02 0:00:03 17
Stabilizing vof-3 to enhance linear solver robustness.


turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 4500 cells
124 5.4629e+33 1.1591e+01 6.5738e+00 7.5122e+01 2.4389e-01 1.6208e+01 1.0805e-01 2.0149e-01 4.6927e-01 9.2227e-01 1.7691e-02 1.4376e-01 9.6568e-01 7.0153e-01 3.9590e+10 8.5381e-05 2.2232e-04 1.8513e-03 3.4937e-03 2.6036e-04 1.7182e-03 6.7803e-03 6.1951e-04 1.7177e-03 7.9949e-01 6.8334e-01 4.0753e-01 0:00:03 16
Stabilizing mp-x-momentum to enhance linear solver robustness.
Stabilizing mp-y-momentum to enhance linear solver robustness.
Stabilizing mp-z-momentum to enhance linear solver robustness.
Stabilizing k to enhance linear solver robustness.
Stabilizing vof-1 to enhance linear solver robustness.
Stabilizing vof-2 to enhance linear solver robustness.
Stabilizing vof-3 to enhance linear solver robustness.


turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 4500 cells
125 6.2593e+42 2.0201e+02 7.2521e+03 4.8546e+01 3.0622e-02 9.6404e-03 2.2526e-10 5.1150e-04 4.0377e-02 5.7064e-03 3.7114e-10 7.4107e-04 2.4628e-02 1.7421e+10 9.7762e+19 0.0000e+00 1.5961e-05 5.2211e-04 0.0000e+00 7.6861e-05 4.1404e-04 0.0000e+00 6.8129e-04 4.1398e-04 9.9960e-01 2.8941e-01 7.5497e-01 0:00:05 15
Stabilizing k to enhance linear solver robustness.
Stabilizing k using GMRES to enhance linear solver robustness.


Divergence detected in AMG solver: k Stabilizing vof-1 to enhance linear solver robustness.
Stabilizing vof-2 to enhance linear solver robustness.
Stabilizing vof-3 to enhance linear solver robustness.


turbulent viscosity limited to viscosity ratio of 1.000000e+05 in 2743 cells


Error at host: floating point exception


Error at Node 0: floating point exception


Error: floating point exception
Error Object: #f


I am not sure how to nterpret these error nodes. Only difference in simulations are the inlet BC.

Does somebody knows how to debug or how to interpret this error?
whydi is offline   Reply With Quote

Reply

Tags
dqmom, eulerian multiphase, floating point exception, inhomogeneous discrete, population balance model


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Suppress twoPhaseEulerFoam energy AlmostSurelyRob OpenFOAM Running, Solving & CFD 33 September 25, 2018 18:45
Segmentation fault when using reactingFOAM for Fluids Tommy Floessner OpenFOAM Running, Solving & CFD 4 April 22, 2018 13:30
Free surface issues with interDyMFoam for hydroturbine oumnion OpenFOAM Running, Solving & CFD 0 October 6, 2017 15:05
HeatSource BC to the whole region in chtMultiRegionHeater xsa OpenFOAM Running, Solving & CFD 3 November 7, 2016 06:07
Floating point exception error lpz_michele OpenFOAM Running, Solving & CFD 53 October 19, 2015 03:50


All times are GMT -4. The time now is 12:09.