|
[Sponsors] |
Pessure Drop Incorrectly Decreases When Volume Fraction Increases |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
September 25, 2022, 12:15 |
Pessure Drop Incorrectly Decreases When Volume Fraction Increases
|
#1 |
New Member
Austin
Join Date: Feb 2022
Posts: 2
Rep Power: 0 |
Hello,
I am running a Fluent simulation (laminar flow) with water as phase 1 and aluminum-oxide as phase 2. I have selected Eulerian multiphase approach and have defined the parameters of phase 2 as such. My geometry is 2D and I have selected the axisymmetric condition. Pipe radius is 10 mm and length is 1 m. Inlet velocity is 0.01 m/s. I have ran simulations at 1 through 5% volume fraction of aluminum oxide. When I increase volume fraction, my ansys simulation reports a decrease in pressure drop, which we know should not be the case. I have shared some images of pressure contours. I have compared the velocity profile with the analytical velocity profile and there is very close agreement. The temperature profile and heat transfer coefficient all agree with expectation (both increase as VF increases), so it seems I am doing *most* of the simulation correctly, however the pressure drop is something that I am stuck on. Can anyone offer any help or pointers? |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
multiphaseEulerFoam (OF2.3.0) : Courant number explodes when running in parallel | Mehrez | OpenFOAM Running, Solving & CFD | 10 | May 18, 2016 12:44 |
Stuck in a Rut- interDyMFoam! | xoitx | OpenFOAM Running, Solving & CFD | 14 | March 25, 2016 08:09 |
mpirun interFoam very stable --> then blows up | ghadab | OpenFOAM Running, Solving & CFD | 3 | October 27, 2013 11:34 |
On the damBreak4phaseFine cases | paean | OpenFOAM Running, Solving & CFD | 0 | November 14, 2008 22:14 |
the Eulerian model and the lower volume fraction | hx li | FLUENT | 2 | October 27, 2005 07:17 |