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

Question about rhoSimpleFoam "if (transonic)"

Register Blogs Community New Posts Updated Threads Search

 
 
LinkBack Thread Tools Search this Thread Display Modes
Prev Previous Post   Next Post Next
Old   April 12, 2010, 14:36
Default Question about rhoSimpleFoam "if (transonic)"
  #1
New Member
 
yu
Join Date: Nov 2009
Posts: 26
Rep Power: 16
universez is on a distinguished road
Hi,
I try to study rhoSimpleFoam. In the pEqn.H of rhoSimpleFoam, there is a line "if (transonic)" see below for the file. I understand the function of the that is using incompressible SIMPLE method for low mach number cases and adding convertive term for compressible flow. (by the way, the compressible part in the rhoSimpleFoam of OpenFoam-dev1.5 is different).

I did output the the value transonic by adding
"Info<<"transonic = "<<transonic<<endl;"
in the rhoSimpleFoam.

the output of the is always "0" (see below)

My question are :

1, how to control transonic? it is specified at somewhere or it is defined by mach number?

2, if transonic = 0, it is always solving an incompressible problem but not a compressible problem.

Thank
yu

==============================================

Time = 172
smoothSolver: Solving for Ux, Initial residual = 0.130169, Final residual = 6.88999e-05, No Iterations 2
smoothSolver: Solving for Uy, Initial residual = 0.120254, Final residual = 9.18545e-05, No Iterations 2
DILUPBiCG: Solving for h, Initial residual = 0.0154733, Final residual = 4.72774e-05, No Iterations 1
transonic = 0
GAMG: Solving for p, Initial residual = 0.277657, Final residual = 0.00683687, No Iterations 6
time step continuity errors : sum local = 5.41896, global = 0.830172, cumulative = 3.09577
rho max/min : 1.79102 1.26744
ExecutionTime = 53.24 s ClockTime = 68 s

===============================================





===========================================
below is the modified pEqu file in the folder of rhoSimpleFoam
================================================
rho = thermo.rho();
rho = max(rho, rhoMin);
rho = min(rho, rhoMax);
rho.relax();
volScalarField rUA = 1.0/UEqn().A();
U = rUA*UEqn().H();
UEqn.clear();
bool closedVolume = false;
Info<<"transonic = "<<transonic<<endl; // output transonic
if (transonic)
{
surfaceScalarField phid
(
"phid",
fvc::interpolate(psi)*(fvc::interpolate(U) & mesh.Sf())
);
for (int nonOrth=0; nonOrth<=nNonOrthCorr; nonOrth++)
{
fvScalarMatrix pEqn
(
fvm::div(phid, p)
- fvm::laplacian(rho*rUA, p)
);
// Relax the pressure equation to ensure diagonal-dominance
pEqn.relax(mesh.relaxationFactor("pEqn"));
pEqn.setReference(pRefCell, pRefValue);
// retain the residual from the first iteration
if (nonOrth == 0)
{
eqnResidual = pEqn.solve().initialResidual();
maxResidual = max(eqnResidual, maxResidual);
}
else
{
pEqn.solve();
}
if (nonOrth == nNonOrthCorr)
{
phi == pEqn.flux();
}
}
}
else
{
phi = fvc::interpolate(rho)*(fvc::interpolate(U) & mesh.Sf());
closedVolume = adjustPhi(phi, U, p);
for (int nonOrth=0; nonOrth<=nNonOrthCorr; nonOrth++)
{
fvScalarMatrix pEqn
(
fvm::laplacian(rho*rUA, p) == fvc::div(phi)
);
pEqn.setReference(pRefCell, pRefValue);
// Retain the residual from the first iteration
if (nonOrth == 0)
{
eqnResidual = pEqn.solve().initialResidual();
maxResidual = max(eqnResidual, maxResidual);
}
else
{
pEqn.solve();
}
if (nonOrth == nNonOrthCorr)
{
phi -= pEqn.flux();
}
}
}

#include "incompressible/continuityErrs.H"
// Explicitly relax pressure for momentum corrector
p.relax();
U -= rUA*fvc::grad(p);
U.correctBoundaryConditions();
// For closed-volume cases adjust the pressure and density levels
// to obey overall mass continuity
if (closedVolume)
{
p += (initialMass - fvc::domainIntegrate(psi*p))
/fvc::domainIntegrate(psi);
}
rho = thermo.rho();
rho = max(rho, rhoMin);
rho = min(rho, rhoMax);
rho.relax();
Info<< "rho max/min : " << max(rho).value() << " " << min(rho).value() << endl;

Yu

Last edited by universez; April 12, 2010 at 20:27.
universez is offline   Reply With Quote

 


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
Unanswered question niklas OpenFOAM 2 July 31, 2013 16:03
Question about Table applicaiton. universez OpenFOAM Running, Solving & CFD 0 January 12, 2010 20:31
Momentum equation discretization in rhoSimpleFoam mighelone OpenFOAM Running, Solving & CFD 0 October 16, 2007 04:51
CHANNEL FLOW: a question and a request Carlos Main CFD Forum 4 August 23, 2002 05:55
question K.L.Huang Siemens 1 March 29, 2000 04:57


All times are GMT -4. The time now is 09:01.