CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

Pressure drop in packed bed

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   October 15, 2015, 18:11
Default Pressure drop in packed bed
  #1
New Member
 
Join Date: Jul 2015
Posts: 23
Rep Power: 10
nicholas.jones is on a distinguished road
All,

I am trying to investigate the pressure drop in a cylindrical column, packed with 50 spheres. I know the inlet pressure (150 psi, or 1149 m2/s2 with SG 0.9), and I know the outlet flow rate (20 kg/hr). I have been using simpleFoam, defining inlet pressure and outlet flow. However, after trying a bunch of inlet/outlet combinations, I cannot get a reasonable solution to my problem. An image of my system has been attached.

My pressure boundary file is below, followed by my velocity.

Any tips are appreciated!

Quote:
FoamFile
{
version 2.0;
format ascii;
class volScalarField;
object p;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

dimensions [0 2 -2 0 0 0 0];

internalField uniform 1149.13;

boundaryField
{
Inlet
{
type fixedValue;
value uniform 1149.13;
}

Outlet
{
type fixedValue;
value $internalField;
}

Walls
{
type zeroGradient;
}

Balls
{
type zeroGradient;
}
defaultFaces
{
type empty;
}


}
Quote:
FoamFile
{
version 2.0;
format ascii;
class volVectorField;
object U;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

dimensions [0 1 -1 0 0 0 0];

internalField uniform (0 0 0.001947);

boundaryField
{
Inlet
{
type fixedValue;
value $internalField;
}

Outlet
{
type flowRateInletVelocity;
massFlowRate constant 0.005;
rho rho;
rhoInlet 900;
value uniform (0 0 0);

// type inletOutlet;
// inletValue uniform (0 0 0.001947);
// value uniform (0 0 0.001947);
}

Walls
{
type fixedValue;
value uniform (0 0 0);
}

Balls
{
type fixedValue;
value uniform (0 0 0);
}
defaultFaces
{
type empty;
}


}
Attached Images
File Type: jpg Screenshot from 2015-10-15 18:03:07.jpg (78.0 KB, 18 views)
nicholas.jones is offline   Reply With Quote

Old   October 15, 2015, 19:12
Default
  #2
New Member
 
Joseph Urich
Join Date: Mar 2009
Location: Pittsburgh, PA
Posts: 21
Rep Power: 17
jurich is on a distinguished road
For simpleFOAM, generally you want to specify p at the outlet (usually 0) and specify the velocity (or mass flow) at the inlet. For your case try:

P:
internalField uniform 0;
Inlet
{
type zeroGradient;
}
Outlet
{
type fixedValue;
value $internalField;
}

U:
Inlet
{ //what you listed for outlet:
type flowRateInletVelocity;
massFlowRate constant 0.005;
rho rho;
rhoInlet 900;
//type fixedValue; //or you can use fixedValue instead of the above
value uniform (0 0 0.001947);
}
Outlet
{
type zeroGradient;
}


Run it and see if the pressure at the inlet matches up to the value you expect, 150 psi

Also, your geometry looks like it might be a challenge to mesh. Where the spheres contact each other might result in non-orthogonal or poor quality cells. That would make it difficult to converge a solution.

Hope that helps.
jurich is offline   Reply With Quote

Reply


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
help in pressure drop calculation in fluent sinaupdate FLUENT 3 July 10, 2016 05:56
static vs. total pressure auf dem feld FLUENT 17 February 26, 2016 13:04
Multiphase liquid-solid spouted bed: pressure problem ghost82 FLUENT 7 November 10, 2013 12:12
Pressure Drop at entrance of a rotor-stator. Resnick Main CFD Forum 0 November 20, 2007 14:50
what the result is negatif pressure at inlet chong chee nan FLUENT 0 December 29, 2001 05:13


All times are GMT -4. The time now is 06:51.