CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Pre-Processing

turbulent rectangular U-Pipeflow - Velocityproblem

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   November 25, 2016, 18:29
Default turbulent rectangular U-Pipeflow - Velocityproblem
  #1
New Member
 
Join Date: Nov 2016
Posts: 8
Rep Power: 10
Bob! is on a distinguished road
Hey guys,

I'm trying to run an as i think quite simple case - still it ain't working.
I've got a rectangular U-Pipe with an incompressible, turbulent flow of water.
Beside the geometric details i only got the Volume which flows in and with it of course the velocity.
I'm using simpleFoam, k-Epsilon-model, RAS.
blockMesh works, simpleFoam runs without an error.
My Problem is, that the velocity doesn't work well. I've git a fixed "inlet-Velocity" of 0.3339 m/s but when viewing with ParaView, i get a velocity of 0.001 (or something small like this) after the first time step.

I made a lot of suggestions about the correct BCs and tried as much as i could by try and error- still i got this problem.
Another suggestion of mine was, that the "internal faces", which are "connecting"/between the five blocks of which the U-Pipe consists, are false defined- but as i read: there doesn't have to be any special definition, they're flowing through automatically. When viewing "p" in ParaView, it's possible to see the change through the complete Pipe - this is why i think that ain't the problem. (When modelling a straight pipe, out of one Block, there ain't a Problem [same BCs etc])

So there must be something wrong with my BCs- and as i said, i tried a lot of different BCs and ain't got any more ideas. I hope, that someone else can help me out and has a better idea...

I'm posting a version of my case, of which i thought it might have worked.
Thanks in advance for any ideas which even might help!!!


Code:
Code:
     /*--------------------------------*- C++ -*----------------------------------*\
| =========                 |                                                 |
| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |
|  \\    /   O peration     | Version:  4.1                                   |
|   \\  /    A nd           | Web:      www.OpenFOAM.org                      |
|    \\/     M anipulation  |                                                 |
\*---------------------------------------------------------------------------*/
FoamFile
{
    version     2.0;
    format      ascii;
    class       volVectorField;
    object      U;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

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

internalField   uniform (0 0 0);

boundaryField
{

    inlet
    {
        type    fixedValue;
    value    uniform (0 0 -0.3338675216);
    }

    outlet
    {
        type            zeroGradient;
    }

    fixedWalls
    {
        type            noSlip;
    }

}

// ************************************************************************* //
Code:
     /*--------------------------------*- C++ -*----------------------------------*\
| =========                 |                                                 |
| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |
|  \\    /   O peration     | Version:  4.1                                   |
|   \\  /    A nd           | Web:      www.OpenFOAM.org                      |
|    \\/     M anipulation  |                                                 |
\*---------------------------------------------------------------------------*/
FoamFile
{
    version     2.0;
    format      ascii;
    class       volScalarField;
    object      p;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

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

internalField   uniform 0;

boundaryField
{

    inlet
    {
    type        zeroGradient;
    }

    outlet
    {
        type            fixedValue;
        value           uniform 0.2045380588;
    }

    fixedWalls
    {
        type            zeroGradient;
    }

}

// ************************************************************************* //

Code:
     /*--------------------------------*- C++ -*----------------------------------*\
| =========                 |                                                 |
| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |
|  \\    /   O peration     | Version:  4.1                                   |
|   \\  /    A nd           | Web:      www.OpenFOAM.org                      |
|    \\/     M anipulation  |                                                 |
\*---------------------------------------------------------------------------*/
FoamFile
{
    version     2.0;
    format      ascii;
    class       dictionary;
    object      blockMeshDict;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

convertToMeters 0.001;

vertices
(
    (0 0 0) //0
    (26 0 0) //1
    (26 16 0) //2
    (0 16 0) //3
    (0 0 -1938) //4
    (26 0 -1938) //5
    (26 16 -1938) //6
    (0 16 -1938) //7
    (0 0 -1968) //8
    (26 0 -1968) //9
    (26 16 -1968) //10
    (0 16 -1968) //11
    (246 0 -1968) //12
    (274 0 -1968) //13
    (274 16 -1968) //14
    (246 16 -1968) //15
    (246 0 -1938) //16
    (274 0 -1938) //17
    (274 16 -1938) //18
    (246 16 -1938) //19
    (246 0 0) //20
    (274 0 0) //21
    (274 16 0) //22
    (246 16 0) //23
);

blocks
(
    hex (4 5 6 7 0 1 2 3) (10 10 20) simpleGrading (1 1 1)
    hex (8 9 10 11 4 5 6 7) (10 10 20) simpleGrading (1 1 1)
    hex (9 12 15 10 5 16 19 6) (10 10 20) simpleGrading (1 1 1)
    hex (12 13 14 15 16 17 18 19) (10 10 20) simpleGrading (1 1 1)
    hex (16 17 18 19 20 21 22 23) (10 10 20) simpleGrading (1 1 1)
);

edges
(
);

boundary
(

    
    fixedWalls
    {
        type wall;
        faces
        (
            (2 3 7 6)
            (3 0 4 7)
            (0 1 5 4)
            (1 2 6 5)

            (6 7 11 10)
            (7 4 8 11)
            (4 5 9 8)

            (5 6 19 16)
            (19 6 10 15)
            (12 15 10 9)
            (5 16 12 9)

            (15 14 18 19)
            (18 14 13 17)
            (16 17 13 12)

            (22 23 19 18)
            (23 20 16 19)
            (20 21 17 16)
            (21 22 18 17)

        );
    }

    inlet
    {
        type patch;
        faces
        (
            (0 3 2 1)     
        );
    }

    outlet
    {
        type patch;
        faces
        (
            (20 23 22 21)
        );
    }
);

mergePatchPairs
(
);

// ************************************************************************* //

Last edited by Bob!; November 26, 2016 at 06:25.
Bob! is offline   Reply With Quote

Old   November 27, 2016, 06:47
Default
  #2
New Member
 
Jeroen
Join Date: Oct 2016
Posts: 21
Rep Power: 10
verboomj is on a distinguished road
Is your inlet faced towards the -Z direction as your velocity?
Could you try and set the pressure to 0 and leave the velocity?
Try running it with Turbulence off;

Hope you find whats wrong.
verboomj is offline   Reply With Quote

Old   November 28, 2016, 18:17
Default
  #3
New Member
 
Join Date: Nov 2016
Posts: 8
Rep Power: 10
Bob! is on a distinguished road
Hey

thanks a lot for the reply!
The inlet should be fine and - however (because i definitely tried before)- you were right with your pressure assumption! It works and it works well as it seems to me =)
Wouldn't have tried it again without your comment - thanks a lot!
Bob! is offline   Reply With Quote

Reply

Tags
incompressible flow, inlet and outlet, velocity


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
Problem with divergence TDK FLUENT 13 December 14, 2018 07:00
Turbulent flow in smooth rectangular duct - Numerical vs. Literature correlations marluc FLUENT 0 July 7, 2011 10:23
setting value of turbulent intensity and turbulent viscosity ratio in wind tunnel nuimlabib Main CFD Forum 0 August 4, 2009 01:05
Turbulent flow in a rectangular duct foam vs fluent atzaru OpenFOAM Pre-Processing 7 February 13, 2007 15:42
DNS of fully developed turbulent pipeflow Emad khalifa Main CFD Forum 0 October 6, 2001 17:57


All times are GMT -4. The time now is 15:02.