|
[Sponsors] |
July 16, 2017, 14:24 |
Density driven flow
|
#1 |
New Member
abi
Join Date: Jul 2016
Posts: 7
Rep Power: 10 |
Hi there
I've doing some work on density induced flow. My problem contains a single phase fluid with 2 components (water and a solute). I'm solving the continuity equation along with the advection diffusion, darcy, equation of state (links between the concentration and density) and a viscosity function. Currently i'm trying to figure out whether the Boussinesq approximation is valid in my case. I've scaled the equations and while doing so, revealed a gap in my Understanding of the physics involved. The continuity-mass conservation for the fluid phase: φ∂(ρ)/∂t+∇∙(ρq)=0 scaling it using characteristic diffusive time scale, flux and density: (x0^2)/D, q0, rho0. The scaling produced: ε/Pe(∂ρ/∂t)+ε∙ρ∇∙q+∇∙q+ε∙q∇ρ=0 where ε<<1 and Pe<<ε For that case i can see that the accumulation term has the largest magnitude and therefore (∂ρ/∂t)=0. But i have diffusion in my system and density does change in respect to time. what's going on? Thanks a lot! Avi |
|
Tags |
density driven flow, mass transfer, mass transport, porous media flow |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Pressure driven flow in 2D LES channelFoam | sheaker | OpenFOAM Running, Solving & CFD | 0 | June 26, 2017 15:44 |
internal flow BCs: pressure driven versus velocity driven | mihaipruna | OpenFOAM Running, Solving & CFD | 22 | March 6, 2014 11:06 |
LTSInterFoam and pressure driven flow | Andrea_85 | OpenFOAM | 3 | August 21, 2012 09:44 |
Different flow patterns in CFX and Fluent | avi@lpsc | FLUENT | 4 | April 8, 2012 07:12 |
Wrong Pressure countors for channel flow driven by mass flow rate or press gradient | ash-khan | FLUENT | 0 | June 21, 2009 11:02 |