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Using sprayFOAM on cyclic problem with wedge boundaries |
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May 28, 2013, 08:08
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Using sprayFOAM on cyclic problem with wedge boundaries
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#1 |
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New Member
Join Date: Dec 2012
Posts: 12
Rep Power: 13  |
Hello,
I’m working on a Spray Jet Flame Project, trying to validate experimental data. My first idea was to solve this Problem with cyclic boundary conditions on a wedge shaped Mesh (original case has a cylindrical shape). In building my case step by step I adopted the aachenBomb tutorial, which does the job so far. But here is my Problem: The injector is located right on the line of symmetry of the wedge, solving works just fine without any errors but the injected mass of the fuel just doesn't reach the defined amount. My questions are: Does the sprayFOAM solver even work correctly with wedge boundaries? If yes, how can I fix this Problem? Thanks in advance! Code:
/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 2.2.0 |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format binary;
class dictionary;
location "constant";
object SprayCloudProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
solution
{
active true;
coupled true;
transient yes;
cellValueSourceCorrection on;
sourceTerms
{
schemes
{
rho explicit 1;
U explicit 1;
Yi explicit 1;
h explicit 1;
radiation explicit 1;
}
}
interpolationSchemes
{
rho cell;
U cellPoint;
thermo:mu cell;
T cell;
Cp cell;
p cell;
}
integrationSchemes
{
U Euler;
T analytical;
}
}
constantProperties
{
T0 320;
// place holders for rho0 and Cp0 - reset from liquid props using T0
rho0 1000;
Cp0 4187;
youngsModulus 1e9;
poissonsRatio 0.35;
epsilon0 1;
f0 0.5;
Pr 0.7;
Tvap 273;
Tbp 373;
constantVolume false;
}
subModels
{
particleForces
{
sphereDrag;
}
injectionModels
{
model1
{
type coneNozzleInjection;
SOI 0;
massTotal 6.0e-6;
parcelBasisType mass;
injectionMethod disc;
flowType flowRateAndDischarge;
outerDiameter 1.9e-4;
innerDiameter 0;
duration 1.25e-3;
position ( 0.07495 0 0 );
direction ( -1 0 0 );
parcelsPerSecond 20000000;
flowRateProfile table
(
(0 0.1272)
(4.16667e-05 6.1634)
(8.33333e-05 9.4778)
(0.000125 9.5806)
(0.000166667 9.4184)
(0.000208333 9.0926)
(0.00025 8.7011)
(0.000291667 8.2239)
(0.000333333 8.0401)
(0.000375 8.845)
(0.000416667 8.9174)
(0.000458333 8.8688)
(0.0005 8.8882)
(0.000541667 8.6923)
(0.000583333 8.0014)
(0.000625 7.2582)
(0.000666667 7.2757)
(0.000708333 6.968)
(0.00075 6.7608)
(0.000791667 6.6502)
(0.000833333 6.7695)
(0.000875 5.5774)
(0.000916667 4.8649)
(0.000958333 5.0805)
(0.001 4.9547)
(0.00104167 4.5613)
(0.00108333 4.4536)
(0.001125 5.2651)
(0.00116667 5.256)
(0.00120833 5.1737)
(0.00125 3.9213)
);
Cd constant 0.9;
thetaInner constant 0.0;
thetaOuter constant 10.0;
sizeDistribution
{
type RosinRammler;
RosinRammlerDistribution
{
minValue 1e-06;
maxValue 0.00015;
d 0.00015;
n 3;
}
}
}
}
dispersionModel none;
patchInteractionModel standardWallInteraction;
heatTransferModel RanzMarshall;
compositionModel singlePhaseMixture;
phaseChangeModel liquidEvaporationBoil;
surfaceFilmModel none;
atomizationModel none;
breakupModel ReitzDiwakar; // ReitzKHRT;
stochasticCollisionModel none;
radiation off;
standardWallInteractionCoeffs
{
type rebound;
}
RanzMarshallCoeffs
{
BirdCorrection true;
}
singlePhaseMixtureCoeffs
{
phases
(
liquid
{
C7H16 1;
}
);
}
liquidEvaporationBoilCoeffs
{
enthalpyTransfer enthalpyDifference;
activeLiquids ( C7H16 );
}
ReitzDiwakarCoeffs
{
solveOscillationEq yes;
Cbag 6;
Cb 0.785;
Cstrip 0.5;
Cs 10;
}
/*
ReitzKHRTCoeffs
{
solveOscillationEq yes;
B0 0.61;
B1 40;
Ctau 1;
CRT 0.1;
msLimit 0.2;
WeberLimit 6;
}
*/
TABCoeffs
{
y0 0;
yDot0 0;
Cmu 10;
Comega 8;
WeCrit 12;
}
}
cloudFunctions
{}
// ************************************************************************* //
Code:
Solving cloud sprayCloud
Cloud: sprayCloud
Current number of parcels = 0
Current mass in system = 0
Linear momentum = (0 0 0)
|Linear momentum| = 0
Linear kinetic energy = 0
Rotational kinetic energy = 0
model1:
number of parcels added = 108
mass introduced = 2.89519e-08
Parcels absorbed into film = 0
New film detached parcels = 0
Parcel fate (number, mass)
- escape = 0, 0
- stick = 0, 0
Temperature min/max = 0, 0
Mass transfer phase change = 2.89521e-08
D10, D32, Dmax (mu) = 0, 0, 0
Liquid penetration 95% mass (m) = 0
Last edited by Mentalo; May 28, 2013 at 09:11. |
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August 13, 2013, 12:15
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#2 |
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New Member
Pang
Join Date: Mar 2011
Location: Denmark
Posts: 25
Rep Power: 15 |
Hi Mentalo,
Did you manage to solve your problem?  Pang |
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August 16, 2013, 03:36
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#3 |
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New Member
Join Date: Dec 2012
Posts: 12
Rep Power: 13 |
Hi Pang,
unfortunately not. I guess with the injector on the line of symmetry sprayFoam isn't working properly. At the moment I'm using a full size mesh. But there are some problems with the value of the injected mass as well.  http://www.cfd-online.com/Forums/ope...sprayfoam.html Best regards, Mentalo |
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August 16, 2013, 03:50
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#4 | |
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New Member
Pang
Join Date: Mar 2011
Location: Denmark
Posts: 25
Rep Power: 15 |
Quote:
May I ask what was the angle when you revolve the 2-D grid? ~2 degree? Regards, Pang |
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August 16, 2013, 03:53
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#5 |
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New Member
Join Date: Dec 2012
Posts: 12
Rep Power: 13 |
I'm not sure but I guess I used an overall wedge-angle of less than 5°
Edit: I found my old case set-up, checkMesh says: Code:
Create time
Create polyMesh for time = 0
Time = 0
Mesh stats
points: 60601
internal points: 0
faces: 120200
internal faces: 59600
cells: 30000
faces per cell: 5.99333
boundary patches: 4
point zones: 0
face zones: 0
cell zones: 0
Overall number of cells of each type:
hexahedra: 29800
prisms: 200
wedges: 0
pyramids: 0
tet wedges: 0
tetrahedra: 0
polyhedra: 0
Checking topology...
Boundary definition OK.
Cell to face addressing OK.
Point usage OK.
Upper triangular ordering OK.
Face vertices OK.
Number of regions: 1 (OK).
Checking patch topology for multiply connected surfaces...
Patch Faces Points Surface topology
symmetry 0 0 ok (empty)
walls 600 1200 ok (non-closed singly connected)
rotper1 30000 30401 ok (non-closed singly connected)
rotper2 30000 30401 ok (non-closed singly connected)
Checking geometry...
Overall domain bounding box (0 0 -0.022922) (0.75 0.525 0.022922)
Mesh (non-empty, non-wedge) directions (1 1 0)
Mesh (non-empty) directions (1 1 1)
Wedge rotper1 with angle 2.5 degrees
Wedge rotper2 with angle 2.5 degrees
All edges aligned with or perpendicular to non-empty directions.
Boundary openness (1.11405e-18 9.56709e-15 -4.48611e-13) OK.
Max cell openness = 3.05315e-16 OK.
Max aspect ratio = 4 OK.
Minimum face area = 2.72881e-07. Maximum face area = 0.00022922. Face area magnitudes OK.
Min volume = 6.82202e-10. Max volume = 6.28704e-07. Total volume = 0.00669923. Cell volumes OK.
Mesh non-orthogonality Max: 0 average: 0
Non-orthogonality check OK.
Face pyramids OK.
Max skewness = 0.330796 OK.
Coupled point location match (average 0) OK.
Mesh OK.
End
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September 7, 2018, 02:12
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#6 |
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New Member
bima
Join Date: Jun 2016
Posts: 3
Rep Power: 9 |
anybody has solved this problem? I am running sprayFoam in a tubular geometry where I apply cyclic boundary condition in my domain (45deg slice). The main problem is my coneNozzleInjection model injects particles from a full disc (360 deg slice)surface, so the solver gives me an error of "Cannot find parcel injection cell" in the zone outside domain. Please help me to find a way to modify the injection surface from full disc to 45 deg arc.
thank you and best regards, Bima |
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