dd8341f659
- controlled by the the 'printExecutionFormat' InfoSwitch in
etc/controlDict
// Style for "ExecutionTime = " output
// - 0 = seconds (with trailing 's')
// - 1 = day-hh:mm:ss
ExecutionTime = 112135.2 s ClockTime = 113017 s
ExecutionTime = 1-07:08:55.20 ClockTime = 1-07:23:37
- Callable via the new Time::printExecutionTime() method,
which also helps to reduce clutter in the applications.
Eg,
runTime.printExecutionTime(Info);
vs
Info<< "ExecutionTime = " << runTime.elapsedCpuTime() << " s"
<< " ClockTime = " << runTime.elapsedClockTime() << " s"
<< nl << endl;
--
ENH: return elapsedClockTime() and clockTimeIncrement as double
- previously returned as time_t, which is less portable.
135 lines
3.8 KiB
C
135 lines
3.8 KiB
C
/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration |
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\\ / A nd | Copyright (C) 2011-2016 OpenFOAM Foundation
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\\/ M anipulation |
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-------------------------------------------------------------------------------
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License
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This file is part of OpenFOAM.
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OpenFOAM is free software: you can redistribute it and/or modify it
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under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
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ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
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FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
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for more details.
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You should have received a copy of the GNU General Public License
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along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
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Application
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interPhaseChangeFoam
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Group
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grpMultiphaseSolvers
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Description
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Solver for 2 incompressible, isothermal immiscible fluids with phase-change
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(e.g. cavitation). Uses a VOF (volume of fluid) phase-fraction based
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interface capturing approach.
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The momentum and other fluid properties are of the "mixture" and a
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single momentum equation is solved.
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The set of phase-change models provided are designed to simulate cavitation
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but other mechanisms of phase-change are supported within this solver
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framework.
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Turbulence modelling is generic, i.e. laminar, RAS or LES may be selected.
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\*---------------------------------------------------------------------------*/
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#include "fvCFD.H"
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#include "CMULES.H"
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#include "subCycle.H"
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#include "interfaceProperties.H"
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#include "phaseChangeTwoPhaseMixture.H"
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#include "turbulentTransportModel.H"
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#include "pimpleControl.H"
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#include "fvOptions.H"
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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int main(int argc, char *argv[])
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{
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#include "postProcess.H"
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#include "setRootCase.H"
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#include "createTime.H"
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#include "createMesh.H"
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#include "createControl.H"
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#include "createFields.H"
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#include "createFvOptions.H"
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#include "createTimeControls.H"
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#include "CourantNo.H"
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#include "setInitialDeltaT.H"
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turbulence->validate();
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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Info<< "\nStarting time loop\n" << endl;
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while (runTime.run())
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{
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#include "readTimeControls.H"
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#include "CourantNo.H"
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#include "setDeltaT.H"
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runTime++;
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Info<< "Time = " << runTime.timeName() << nl << endl;
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// --- Pressure-velocity PIMPLE corrector loop
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while (pimple.loop())
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{
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#include "alphaControls.H"
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surfaceScalarField rhoPhi
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(
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IOobject
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(
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"rhoPhi",
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runTime.timeName(),
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mesh
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),
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mesh,
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dimensionedScalar(dimMass/dimTime, Zero)
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);
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mixture->correct();
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#include "alphaEqnSubCycle.H"
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interface.correct();
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#include "UEqn.H"
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// --- Pressure corrector loop
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while (pimple.correct())
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{
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#include "pEqn.H"
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}
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if (pimple.turbCorr())
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{
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turbulence->correct();
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}
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}
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runTime.write();
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runTime.printExecutionTime(Info);
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}
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Info<< "End\n" << endl;
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return 0;
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}
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// ************************************************************************* //
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