Consistency update: nonNewtonianIcoFoam

This commit is contained in:
Vuko Vukcevic 2017-01-05 08:53:42 +01:00
parent 27a23484fa
commit b267ad83de

View file

@ -27,6 +27,7 @@ Application
Description Description
Transient solver for incompressible, laminar flow of non-Newtonian fluids. Transient solver for incompressible, laminar flow of non-Newtonian fluids.
Consistent formulation without time-step and relaxation dependence by Jasak Consistent formulation without time-step and relaxation dependence by Jasak
and Tukovic.
Author Author
Hrvoje Jasak, Wikki Ltd. All rights reserved Hrvoje Jasak, Wikki Ltd. All rights reserved
@ -63,6 +64,9 @@ int main(int argc, char *argv[])
fluid.correct(); fluid.correct();
// Time-derivative matrix
fvVectorMatrix ddtUEqn(fvm::ddt(U));
// Convection-diffusion matrix // Convection-diffusion matrix
fvVectorMatrix HUEqn fvVectorMatrix HUEqn
( (
@ -70,24 +74,23 @@ int main(int argc, char *argv[])
- fvm::laplacian(fluid.nu(), U) - fvm::laplacian(fluid.nu(), U)
); );
// Time derivative matrix
fvVectorMatrix ddtUEqn(fvm::ddt(U));
if (piso.momentumPredictor()) if (piso.momentumPredictor())
{ {
solve(ddtUEqn + HUEqn == -fvc::grad(p)); solve(ddtUEqn + HUEqn == -fvc::grad(p));
} }
// Prepare clean Ap without time derivative contribution // Prepare clean 1/a_p without time derivative contribution
// HJ, 26/Oct/2015 volScalarField rAU = 1.0/HUEqn.A();
volScalarField aU = HUEqn.A();
// --- PISO loop // --- PISO loop
while (piso.correct()) while (piso.correct())
{ {
U = HUEqn.H()/aU; // Calculate U from convection-diffusion matrix
phi = (fvc::interpolate(U) & mesh.Sf()); U = rAU*HUEqn.H();
// Consistently calculate flux
piso.calcTransientConsistentFlux(phi, U, rAU, ddtUEqn);
adjustPhi(phi, U, p); adjustPhi(phi, U, p);
@ -95,7 +98,14 @@ int main(int argc, char *argv[])
{ {
fvScalarMatrix pEqn fvScalarMatrix pEqn
( (
fvm::laplacian(1/aU, p) == fvc::div(phi) fvm::laplacian
(
fvc::interpolate(rAU)/piso.aCoeff(),
p,
"laplacian(rAU," + p.name() + ')'
)
==
fvc::div(phi)
); );
pEqn.setReference(pRefCell, pRefValue); pEqn.setReference(pRefCell, pRefValue);
@ -112,13 +122,8 @@ int main(int argc, char *argv[])
# include "continuityErrs.H" # include "continuityErrs.H"
// Note: cannot call H(U) here because the velocity is not complete // Consistently reconstruct velocity after pressure equation
// HJ, 22/Jan/2016 piso.reconstructTransientVelocity(U, phi, ddtUEqn, rAU, p);
U = 1.0/(aU + ddtUEqn.A())*
(
U*aU - fvc::grad(p) + ddtUEqn.H()
);
U.correctBoundaryConditions();
} }
runTime.write(); runTime.write();