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

pressure in incompressible solvers e.g. simpleFoam

Register Blogs Community New Posts Updated Threads Search

Like Tree2Likes
  • 1 Post By Bjw
  • 1 Post By piu58

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 23, 2010, 08:45
Default pressure in incompressible solvers e.g. simpleFoam
  #1
New Member
 
Christian Graurock
Join Date: Jul 2010
Location: Berlin, Germany
Posts: 6
Rep Power: 15
chrizzl is on a distinguished road
Dear All,

I have a general question about the setup of the pressure in an incompressible solver like the simpleFoam-solver.

As we all know in simpleFoam the "strange" pressure units are a result of the partition by the density. This is reasonable, because the density will not change in an incompressible flow. Hence the only property of the fluid which can be changed by the user is the kinematic viscosity.

In my opinion in a pressure driven flow (pressure difference between inlet and outlet are known from an experiment) you have to normalise the fixed pressure values at inlet and outlet by the density.

In common commercial flow solvers you have to define a reference density. That is not possible in simpleFoam and why I wrote down my thoughts in this forum. It would be gald if someone could help me in this open discussion.

Regards,
Christian
chrizzl is offline   Reply With Quote

Old   August 24, 2010, 03:23
Default
  #2
New Member
 
Christian Graurock
Join Date: Jul 2010
Location: Berlin, Germany
Posts: 6
Rep Power: 15
chrizzl is on a distinguished road
Another reason for posting this massage is, that I have seen many users who don't care about the normalization of the pressure. I just want to make it clear (for me) in this forum.
There are experimental data like:
Inlet: 1,013,250 Pa
Outlet: 101,325 Pa
--> Delta p: 911,925 Pa


With a density of air round about 1,2 kg/m³ you've got:
Inlet: 844,375 m²/s²
Outlet: 84,437.5 m²/s²
--> Delta p: 759,937.5 m²/s²

Which setup is the correct one? In my opinion it's the second one
Thanks,
Christian
chrizzl is offline   Reply With Quote

Old   August 24, 2010, 05:41
Default
  #3
Bjw
New Member
 
Björn Westendorf
Join Date: Oct 2009
Location: Stuttgart, Germany
Posts: 9
Rep Power: 16
Bjw is on a distinguished road
Changing the scale and/or the unit of pressure should not change the physics of your problem.
Bjw is offline   Reply With Quote

Old   August 24, 2010, 06:02
Default
  #4
Senior Member
 
Join Date: Mar 2009
Location: Norway
Posts: 137
Rep Power: 17
kjetil is on a distinguished road
Well, you could just have a look at the units atop in the p-file. From there it should be very clear if your normalization is correct.
kjetil is offline   Reply With Quote

Old   August 24, 2010, 06:07
Default
  #5
New Member
 
Christian Graurock
Join Date: Jul 2010
Location: Berlin, Germany
Posts: 6
Rep Power: 15
chrizzl is on a distinguished road
Thank you for your reply.

I know, that the physics are the same, but the first setup only make sense in a compressible simulation, the second one in an incompressible simulation.
If you set your pressure difference, which is known from an experiment without density-normalization to your simpleFoam-setup you will get a setup, which is different to the experiment (factor in this case 1.2).
--> The setup does not mirror your experiment. Is this correct?

From your reply I guess, that my thoughts are correct. Thanks a lot.
chrizzl is offline   Reply With Quote

Old   August 24, 2010, 08:08
Default
  #6
Member
 
Sven Degner
Join Date: Mar 2009
Location: Zürich
Posts: 55
Rep Power: 17
sven82 is on a distinguished road
Hi everyone,

I'm with Cristian, was your experimental data's initialization with a pressure difference,
you must dived the pressure through the density ("for a normalization"). After this the results should look like the experimental data's. A other opportunity is the work with a post processor.

best regards
Sven
sven82 is offline   Reply With Quote

Old   August 24, 2010, 08:41
Default
  #7
Bjw
New Member
 
Björn Westendorf
Join Date: Oct 2009
Location: Stuttgart, Germany
Posts: 9
Rep Power: 16
Bjw is on a distinguished road
Christian, sorry that I misunderstood your Question.

Quote:
If you set your pressure difference, which is known from an experiment without density-normalization to your simpleFoam-setup you will get a setup, which is different to the experiment (factor in this case 1.2).
--> The setup does not mirror your experiment. Is this correct?
Yes, absolutely. You must divide the pressure (Unit Pa) by density first when using an incompressible solver.
EddySouth likes this.
Bjw is offline   Reply With Quote

Old   August 24, 2010, 11:19
Default
  #8
New Member
 
Christian Graurock
Join Date: Jul 2010
Location: Berlin, Germany
Posts: 6
Rep Power: 15
chrizzl is on a distinguished road
Quote:
Originally Posted by Bjw View Post
Yes, absolutely. You must divide the pressure (Unit Pa) by density first when using an incompressible solver.
Thanks, that's exactly what I was looking for.
chrizzl is offline   Reply With Quote

Old   April 8, 2016, 03:47
Default
  #9
New Member
 
Prasanna Welahettige
Join Date: Jan 2016
Location: Norway
Posts: 28
Rep Power: 10
prasa is on a distinguished road
Quote:
Originally Posted by chrizzl View Post
Dear All,

I have a general question about the setup of the pressure in an incompressible solver like the simpleFoam-solver.

As we all know in simpleFoam the "strange" pressure units are a result of the partition by the density. This is reasonable, because the density will not change in an incompressible flow. Hence the only property of the fluid which can be changed by the user is the kinematic viscosity.

In my opinion in a pressure driven flow (pressure difference between inlet and outlet are known from an experiment) you have to normalise the fixed pressure values at inlet and outlet by the density.

In common commercial flow solvers you have to define a reference density. That is not possible in simpleFoam and why I wrote down my thoughts in this forum. It would be gald if someone could help me in this open discussion.

Regards,
Christian


Hi,

I was reading this thread these days. And I found this will help to future readers. Like to add a comment.

In simplefoam continuity equation doesn't include the density because incompressible fluid. But in momentum equation density is a parameter(constant). Therefore pressure has introduced as pressure/density.

units [pressure/density] = m2/s3

cheers.
prasa is offline   Reply With Quote

Old   June 9, 2016, 11:01
Default
  #10
New Member
 
Join Date: May 2016
Posts: 1
Rep Power: 0
Jan Brunner is on a distinguished road
Quote:
Originally Posted by prasa View Post
units [pressure/density] = m2/s3
Hi Prasa

Thanks for wanting to clarify this but the unit should be m2/s2, right?

All the best,
Jan
Jan Brunner is offline   Reply With Quote

Old   June 9, 2016, 12:30
Default
  #11
New Member
 
Prasanna Welahettige
Join Date: Jan 2016
Location: Norway
Posts: 28
Rep Power: 10
prasa is on a distinguished road
Quote:
Originally Posted by Jan Brunner View Post
Hi Prasa

Thanks for wanting to clarify this but the unit should be m2/s2, right?

All the best,
Jan
Hi Jan,

Yes it should be m2/s2.

Regards,
Prasa.
prasa is offline   Reply With Quote

Old   March 27, 2017, 09:42
Default For Hydrogen ??
  #12
New Member
 
cfdRocker
Join Date: Jun 2011
Posts: 5
Rep Power: 14
Manojmech is on a distinguished road
Sorry for reopening this thread.

I would like to know if the fluid is hydrogen. Density of Hydrogen is very less compared to Air. its around 0.0899 kg/m3 and Inlet pressure shoots up and I am getting divergence in simpleFoam.


Can anyone clarify this ??

Regards,
Manoj
Manojmech is offline   Reply With Quote

Old   March 27, 2017, 11:49
Default
  #13
Senior Member
 
piu58's Avatar
 
Uwe Pilz
Join Date: Feb 2017
Location: Leipzig, Germany
Posts: 744
Rep Power: 15
piu58 is on a distinguished road
Dear Manoj,

you get stabilisation problems not for the density but for the much larger Renolds number which results from it. It is well known that larger Re numbers may arise destabilisation. But can be solved, of course. It depends on the solver you use, which arrangements are possible. in simpleFoam you may chose a lesser value for relaxationFactors in fvSolution.
Teresa.Z likes this.
__________________
Uwe Pilz
--
Die der Hauptbewegung überlagerte Schwankungsbewegung ist in ihren Einzelheiten so hoffnungslos kompliziert, daß ihre theoretische Berechnung aussichtslos erscheint. (Hermann Schlichting, 1950)
piu58 is offline   Reply With Quote

Old   March 28, 2017, 05:49
Default
  #14
New Member
 
cfdRocker
Join Date: Jun 2011
Posts: 5
Rep Power: 14
Manojmech is on a distinguished road
Hello Uwe Pilz,

Thank you for your response. I tried reducing the relaxationFactors as low as 0.1 for U but did not work .

My simulation residuals are as below :-

Create mesh for time = 0


SIMPLE: convergence criteria
field p tolerance 1e-06
field U tolerance 1e-06
field "(k|epsilon|omega|f|v2)" tolerance 1e-06

Reading field p

Reading field U

Reading/calculating face flux field phi

Selecting incompressible transport model Newtonian
Selecting turbulence model type laminar
No MRF models present

No finite volume options present


Starting time loop

Time = 1

smoothSolver: Solving for Ux, Initial residual = 1, Final residual = 0.00189998, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 1, Final residual = 0.00172237, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 1, Final residual = 0.0025047, No Iterations 1
GAMG: Solving for p, Initial residual = 1, Final residual = 0.0285601, No Iterations 1
time step continuity errors : sum local = 2736.75, global = -639.791, cumulative = -639.791
ExecutionTime = 4.78 s ClockTime = 5 s

Time = 2

smoothSolver: Solving for Ux, Initial residual = 0.0690268, Final residual = 0.000134747, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.0667625, Final residual = 0.000110036, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.100766, Final residual = 0.000232851, No Iterations 1
GAMG: Solving for p, Initial residual = 0.893178, Final residual = 0.0296773, No Iterations 2
time step continuity errors : sum local = 664.798, global = 147.554, cumulative = -492.237
ExecutionTime = 7.27 s ClockTime = 8 s

Time = 3

smoothSolver: Solving for Ux, Initial residual = 0.539464, Final residual = 0.000930136, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.559662, Final residual = 0.00101096, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.460855, Final residual = 0.000848781, No Iterations 1
GAMG: Solving for p, Initial residual = 0.562958, Final residual = 0.0145996, No Iterations 2
time step continuity errors : sum local = 816.835, global = -396.305, cumulative = -888.542
ExecutionTime = 9.68 s ClockTime = 10 s

Time = 4

smoothSolver: Solving for Ux, Initial residual = 0.181828, Final residual = 0.000369129, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.191699, Final residual = 0.000363309, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.163456, Final residual = 0.000388016, No Iterations 1
GAMG: Solving for p, Initial residual = 0.445896, Final residual = 0.0413308, No Iterations 1
time step continuity errors : sum local = 1300.99, global = -453.554, cumulative = -1342.1
ExecutionTime = 11.96 s ClockTime = 12 s

Time = 5

smoothSolver: Solving for Ux, Initial residual = 0.157346, Final residual = 0.000294152, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.178279, Final residual = 0.000372299, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.12979, Final residual = 0.000339263, No Iterations 1
GAMG: Solving for p, Initial residual = 0.333383, Final residual = 0.0327735, No Iterations 2
time step continuity errors : sum local = 865.563, global = -95.1892, cumulative = -1437.29
ExecutionTime = 14.3 s ClockTime = 15 s

Time = 6

smoothSolver: Solving for Ux, Initial residual = 0.118667, Final residual = 0.000266071, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.14578, Final residual = 0.000287402, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.164746, Final residual = 0.000527067, No Iterations 1
GAMG: Solving for p, Initial residual = 0.340376, Final residual = 0.0297977, No Iterations 1
time step continuity errors : sum local = 933.368, global = 248.937, cumulative = -1188.35
ExecutionTime = 16.52 s ClockTime = 17 s

Time = 7

smoothSolver: Solving for Ux, Initial residual = 0.0951829, Final residual = 0.000200016, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.138162, Final residual = 0.000303547, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.138874, Final residual = 0.00046242, No Iterations 1
GAMG: Solving for p, Initial residual = 0.194145, Final residual = 0.014261, No Iterations 2
time step continuity errors : sum local = 493.546, global = 191.549, cumulative = -996.799
ExecutionTime = 18.97 s ClockTime = 19 s

Time = 8

smoothSolver: Solving for Ux, Initial residual = 0.108677, Final residual = 0.000179489, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.225636, Final residual = 0.000503802, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.11593, Final residual = 0.000352237, No Iterations 1
GAMG: Solving for p, Initial residual = 0.256212, Final residual = 0.0223614, No Iterations 1
time step continuity errors : sum local = 794.502, global = 202.588, cumulative = -794.211
ExecutionTime = 21.27 s ClockTime = 22 s

Time = 9

smoothSolver: Solving for Ux, Initial residual = 0.0982557, Final residual = 0.000304908, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.185531, Final residual = 0.000533666, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.0994782, Final residual = 0.00034999, No Iterations 1
GAMG: Solving for p, Initial residual = 0.293328, Final residual = 0.0275425, No Iterations 1
time step continuity errors : sum local = 1043.34, global = 151.985, cumulative = -642.226
ExecutionTime = 23.59 s ClockTime = 24 s

Time = 10

smoothSolver: Solving for Ux, Initial residual = 0.0937519, Final residual = 0.000187036, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.0959, Final residual = 0.000166799, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.0952078, Final residual = 0.000233081, No Iterations 1
GAMG: Solving for p, Initial residual = 0.368527, Final residual = 0.0356445, No Iterations 1
time step continuity errors : sum local = 1467.9, global = 92.6168, cumulative = -549.61
ExecutionTime = 27.46 s ClockTime = 28 s

Time = 11

smoothSolver: Solving for Ux, Initial residual = 0.164868, Final residual = 0.000163476, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.222946, Final residual = 0.000334008, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.12722, Final residual = 0.000234201, No Iterations 1
GAMG: Solving for p, Initial residual = 0.477769, Final residual = 0.0298537, No Iterations 1
time step continuity errors : sum local = 1505.12, global = 19.7979, cumulative = -529.812
ExecutionTime = 29.72 s ClockTime = 30 s

Time = 12

smoothSolver: Solving for Ux, Initial residual = 0.130392, Final residual = 0.000355599, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.321622, Final residual = 0.000903749, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.12949, Final residual = 0.00030575, No Iterations 1
GAMG: Solving for p, Initial residual = 0.703616, Final residual = 0.0332269, No Iterations 1
time step continuity errors : sum local = 2847.31, global = 90.554, cumulative = -439.258
ExecutionTime = 31.96 s ClockTime = 32 s

Time = 13

smoothSolver: Solving for Ux, Initial residual = 0.0826217, Final residual = 0.000238347, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.130508, Final residual = 0.000542229, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.18985, Final residual = 0.000381059, No Iterations 1
GAMG: Solving for p, Initial residual = 0.833578, Final residual = 0.0424293, No Iterations 1
time step continuity errors : sum local = 6137.85, global = 204.729, cumulative = -234.529
ExecutionTime = 34.2 s ClockTime = 35 s

Time = 14

smoothSolver: Solving for Ux, Initial residual = 0.130854, Final residual = 0.000467332, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.104228, Final residual = 0.000302874, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.119158, Final residual = 0.000711339, No Iterations 1
GAMG: Solving for p, Initial residual = 0.883089, Final residual = 0.0555208, No Iterations 1
time step continuity errors : sum local = 14200.1, global = 11.3717, cumulative = -223.157
ExecutionTime = 36.42 s ClockTime = 37 s

Time = 15

smoothSolver: Solving for Ux, Initial residual = 0.103926, Final residual = 0.000248405, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.233039, Final residual = 0.000832855, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.115342, Final residual = 0.000299915, No Iterations 1
GAMG: Solving for p, Initial residual = 0.893818, Final residual = 0.0572619, No Iterations 1
time step continuity errors : sum local = 18571, global = 876.462, cumulative = 653.305
ExecutionTime = 38.64 s ClockTime = 39 s

Time = 16

smoothSolver: Solving for Ux, Initial residual = 0.186822, Final residual = 0.0013917, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.206877, Final residual = 0.000716568, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.129085, Final residual = 2.18237e-05, No Iterations 2
GAMG: Solving for p, Initial residual = 0.929582, Final residual = 0.0374351, No Iterations 2
time step continuity errors : sum local = 37929.5, global = -19801.9, cumulative = -19148.6
ExecutionTime = 41.11 s ClockTime = 42 s

Time = 17

smoothSolver: Solving for Ux, Initial residual = 0.0989814, Final residual = 0.000175765, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.136444, Final residual = 0.00032175, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.0903033, Final residual = 0.000223593, No Iterations 1
GAMG: Solving for p, Initial residual = 0.893951, Final residual = 0.0713946, No Iterations 1
time step continuity errors : sum local = 89091.8, global = -5091.64, cumulative = -24240.2
ExecutionTime = 43.34 s ClockTime = 44 s

Time = 18

smoothSolver: Solving for Ux, Initial residual = 0.16088, Final residual = 0.000557163, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.232857, Final residual = 0.000855333, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.0866188, Final residual = 0.000243466, No Iterations 1
GAMG: Solving for p, Initial residual = 0.802139, Final residual = 0.0397683, No Iterations 1
time step continuity errors : sum local = 150507, global = -9986.03, cumulative = -34226.2
ExecutionTime = 45.56 s ClockTime = 46 s

Time = 19

smoothSolver: Solving for Ux, Initial residual = 0.0714521, Final residual = 0.000127453, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.0880485, Final residual = 0.000378587, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.0896318, Final residual = 0.00025341, No Iterations 1
GAMG: Solving for p, Initial residual = 0.936714, Final residual = 0.069373, No Iterations 1
time step continuity errors : sum local = 580022, global = -21106.1, cumulative = -55332.3
ExecutionTime = 47.79 s ClockTime = 48 s

Time = 20

smoothSolver: Solving for Ux, Initial residual = 0.104275, Final residual = 5.37614e-06, No Iterations 2
smoothSolver: Solving for Uy, Initial residual = 0.108497, Final residual = 8.93021e-05, No Iterations 2
smoothSolver: Solving for Uz, Initial residual = 0.0775309, Final residual = 0.000112957, No Iterations 2
GAMG: Solving for p, Initial residual = 0.991097, Final residual = 0.0726207, No Iterations 1
time step continuity errors : sum local = 1.70661e+08, global = 369551, cumulative = 314219
ExecutionTime = 51.79 s ClockTime = 52 s

Time = 21

smoothSolver: Solving for Ux, Initial residual = 0.130851, Final residual = 1.23498e-05, No Iterations 2
smoothSolver: Solving for Uy, Initial residual = 0.133453, Final residual = 1.14443e-05, No Iterations 2
smoothSolver: Solving for Uz, Initial residual = 0.123063, Final residual = 8.81908e-06, No Iterations 2
GAMG: Solving for p, Initial residual = 0.980152, Final residual = 0.0740928, No Iterations 5
time step continuity errors : sum local = 5.06379e+09, global = -1.63071e+08, cumulative = -1.62757e+08
ExecutionTime = 54.92 s ClockTime = 55 s

Time = 22

smoothSolver: Solving for Ux, Initial residual = 0.304109, Final residual = 0.000529039, No Iterations 1
smoothSolver: Solving for Uy, Initial residual = 0.0874946, Final residual = 0.000185472, No Iterations 1
smoothSolver: Solving for Uz, Initial residual = 0.114907, Final residual = 6.19314e-05, No Iterations 1
GAMG: Solving for p, Initial residual = 0.948518, Final residual = 0.0931426, No Iterations 1
time step continuity errors : sum local = 1.11399e+10, global = -1.46106e+08, cumulative = -3.08863e+08
ExecutionTime = 57.19 s ClockTime = 58 s

Time = 23

smoothSolver: Solving for Ux, Initial residual = 0.118614, Final residual = 0.0010459, No Iterations 2
smoothSolver: Solving for Uy, Initial residual = 0.129134, Final residual = 6.72522e-05, No Iterations 3
smoothSolver: Solving for Uz, Initial residual = 0.101372, Final residual = 2.39837e-05, No Iterations 3
GAMG: Solving for p, Initial residual = 0.423058, Final residual = 0.0259104, No Iterations 1
time step continuity errors : sum local = 2.47431e+14, global = -5.41145e+12, cumulative = -5.41176e+12
ExecutionTime = 59.73 s ClockTime = 60 s

Time = 24

smoothSolver: Solving for Ux, Initial residual = 0.120392, Final residual = 0.000117413, No Iterations 3
smoothSolver: Solving for Uy, Initial residual = 0.131364, Final residual = 1.21663e-05, No Iterations 3
smoothSolver: Solving for Uz, Initial residual = 0.127022, Final residual = 1.99985e-05, No Iterations 3
GAMG: Solving for p, Initial residual = 0.924117, Final residual = 0.0600726, No Iterations 1
time step continuity errors : sum local = 5.14431e+19, global = 2.03359e+17, cumulative = 2.03353e+17
ExecutionTime = 62.41 s ClockTime = 63 s

I stopped at this stage Because I know this will diverge.

Would you like to look at my BC. May be something wrong in that may be ?

Physics is Inlet at 1.8 bar and outlet at 1.5 bar. Flow in a micro channel with Hydrogen as fluid.

My p file

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

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

internalField uniform 1112347.05;

boundaryField
{
WALL
{
type zeroGradient;
}


INLET
{
type fixedValue;
value uniform 2002224.694;
}

OUTLET
{
type fixedValue;
value uniform 1668520.57;
}
}

My U file

\*---------------------------------------------------------------------------*/
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 pressureInletVelocity;
value uniform (0 0 0);
}



WALL
{
type noSlip;
}


OUTLET
{
type inletOutlet;
inletValue uniform (0.0001 0 0);
value uniform (0.0001 0 0);
}

}

Regards,
Manoj
Manojmech is offline   Reply With Quote

Reply

Tags
incompressible, pressure, reference density, simplefoam, solver


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 steadyState solvers using pressure BC Victor OpenFOAM 1 December 14, 2009 05:40
Setting pressure and velocity in inlet Asghari FLUENT 5 September 22, 2006 13:23
Slow convergence in steadystate incompressible simpleFoam suggestions brooksmoses OpenFOAM Running, Solving & CFD 0 March 3, 2006 04:57
pressure inlet in incompressible flow dirk FLUENT 2 June 22, 2005 13:27
incompressible flow - prescribing pressure drop - how best to do it? M. Gerritsen Main CFD Forum 4 January 10, 1999 09:53


All times are GMT -4. The time now is 05:31.