i am encountering some problems with my simulation, hopefully someone can help me sorting things out
I am modeling a multi phase eulerian flow through a porous zone, with velocity inlet, pressure outlet, SIMPLE algo and UDFs controlling the fluid flow.
(2 liquid, 1 gas)
the UDF descrbies e.g. viscouse resistance and the masstransfer between the 2 liquid zones,
which results in volumefractions of those 2 liquids 'mixing' over the porous zone
Now i would like to track some particles through the domain and view their distribution.
Therefore i used DPM, particle tracking, with injection from the inlet durface.
The result indicates the particles go through the porous media - but they do not seem to 'mix' as heavily as the volumefraction of the phases.
So my question is:
In this case, do i need to
a) somehow assain those UDF to the injection?
Where as liquid 1 and 2 enter the porous zone through (surface) inlet - at first i thought this would "make" the injected particles follow accordingly
[from 184.108.40.206. Limitations on Using the Discrete Phase Model with Other ANSYS Fluent Models
[" ... When using the DPM model with the Eulerian multiphase model, the tracked particles rely only on the primary phase to compute drag, heat, and mass transfer.
Also, any DPM related source terms are applied to the primary phase. Particle tracking relative to a secondary phase is not provided. ... "]
If adding UDFs is nessecary, what is the recommended way of doing so?
(ecspecially, as there are UDFs for each luiqid phase)
b) use an other type of particle?
e.g. inert ones?
I hope i was able to describe the problem, even without any pictures atm.
Thanks in advace for your help!