|
[Sponsors] |
VoF Model, miscible fluids, mass transfer rate |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
May 12, 2017, 08:50 |
VoF Model, miscible fluids, mass transfer rate
|
#1 |
New Member
Yu Lu
Join Date: Jul 2015
Location: England
Posts: 26
Rep Power: 11 |
I'm simulating a situation where a channel is filled with one static fluid (fluid 1) and another fluid (fluid 2) (which is miscible to the one filling the channel) is injected into the channel to displace the first one.
I care about the interfacial phenomena at between these two fluids So I'm planning using laminar VoF model (which works fine for my immiscible cases). For simple fluids, for example a glycerol solution (Say 86% wt.) as Fluid 1 and water as fluid 2. The only place I found to put the diffusion/mass transfer between these two fluid is the "mass" tab in the phase interaction. What exactly is this value I should put in? I was guessing a constant mass transfer rate but in the Fluent manual it says constant rate is not available for VoF model. Some suggestions on how to work out this value for my situation or the actual value I should use and its source will be much appreciated! Thanks a lot! |
|
March 24, 2018, 11:59 |
|
#2 |
Senior Member
Hamed Abdul Majeed
Join Date: May 2012
Location: New Orleans, LA, US
Posts: 147
Rep Power: 14 |
You can add a variable source term through a UDF.
|
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
mass flow in is not equal to mass flow out | saii | CFX | 12 | March 19, 2018 06:21 |
Error - Solar absorber - Solar Thermal Radiation | MichaelK | CFX | 12 | September 1, 2016 06:15 |
Basic Nozzle-Expander Design | karmavatar | CFX | 20 | March 20, 2016 09:44 |
Solver for Multispecies Mass Transfer induced Domain growth/shrinkage | MonoC | OpenFOAM Running, Solving & CFD | 1 | March 13, 2016 08:41 |
Convective Heat Transfer - Heat Exchanger | Mark | CFX | 6 | November 15, 2004 16:55 |