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Standardise on British spelling: -ize -> -ise
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OpenFOAM is predominantly written in Britain with British spelling conventions
so -ise is preferred to -ize.
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Henry Weller committed Jun 1, 2021
1 parent 55f7516 commit ee777e4
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adjointOutletPressure/adjointOutletPressureFvPatchScalarField.C
adjointOutletVelocity/adjointOutletVelocityFvPatchVectorField.C
adjointShapeOptimizationFoam.C
adjointShapeOptimisationFoam.C

EXE = $(FOAM_APPBIN)/adjointShapeOptimizationFoam
EXE = $(FOAM_APPBIN)/adjointShapeOptimisationFoam
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2018 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2019 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2019 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
Application
adjointShapeOptimizationFoam
adjointShapeOptimisationFoam
Description
Steady-state solver for incompressible, turbulent flow of non-Newtonian
Expand All @@ -31,7 +31,7 @@ Description
References:
\verbatim
"Implementation of a continuous adjoint for topology optimization of
"Implementation of a continuous adjoint for topology optimisation of
ducted flows"
C. Othmer,
E. de Villiers,
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2018 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2019 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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Expand Up @@ -250,7 +250,7 @@ void Foam::functionObjects::sizeDistribution::writeDistribution()

}

if (normalize_)
if (normalise_)
{
if(sum(result) != 0)
{
Expand Down Expand Up @@ -460,7 +460,7 @@ bool Foam::functionObjects::sizeDistribution::read(const dictionary& dict)
{
fvMeshFunctionObject::read(dict);

normalize_ = dict.lookupOrDefault<Switch>("normalize", false);
normalise_ = dict.lookupOrDefault<Switch>("normalise", false);
densityFunction_ = dict.lookupOrDefault<Switch>("densityFunction", false);
geometric_ = dict.lookupOrDefault<Switch>("geometric", false);
maxOrder_ = dict.lookupOrDefault("maxOrder", 3);
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2017-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2017-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
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populationBalance | corresponding populationBalance | yes |
functionType | number/volume/moments/stdDev | yes |
coordinateType | used for density/moment calculation | yes |
normalize | normalize concentrations | no | no
normalise | normalise concentrations | no | no
densityFunction | compute densityFunction | no | no
logBased | use log of coordinate for density | no | no
maxOrder | maxim order of moment output | no | 3
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//- List of volume-averaged diameters
scalarField d_;

//- Normalize number/volume concentrations
Switch normalize_;
//- Normalise number/volume concentrations
Switch normalise_;

//- Determines whether density function is calculated
Switch densityFunction_;
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand All @@ -29,7 +29,7 @@ Description
Reference:
\verbatim
Enwald, H., Peirano, E., & Almstedt, A. E. (1996).
Eulerian two-phase flow theory applied to fluidization.
Eulerian two-phase flow theory applied to fluidisation.
International Journal of Multiphase Flow, 22, 21-66.
\endverbatim
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand All @@ -29,7 +29,7 @@ Description
Reference:
\verbatim
Enwald, H., Peirano, E., & Almstedt, A. E. (1996).
Eulerian two-phase flow theory applied to fluidization.
Eulerian two-phase flow theory applied to fluidisation.
International Journal of Multiphase Flow, 22, 21-66.
Eq. 106, p. 43.
\endverbatim
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand Down Expand Up @@ -30,7 +30,7 @@ Description
Reference:
\verbatim
Gidaspow, D. (1994).
Multiphase flow and fluidization: continuum and kinetic theory
Multiphase flow and fluidisation: continuum and kinetic theory
descriptions.
Academic press, New York.
\endverbatim
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand Down Expand Up @@ -30,13 +30,13 @@ Description
References:
\verbatim
Enwald, H., Peirano, E., & Almstedt, A. E. (1996).
Eulerian two-phase flow theory applied to fluidization.
Eulerian two-phase flow theory applied to fluidisation.
International Journal of Multiphase Flow, 22, 21-66.
This is identical to the Wen and Yu, Rowe model Table 3.6 p.56 in
van Wachem, B. G. M. (2000).
Derivation, implementation, and validation of computer simulation models
for gas-solid fluidized beds.
for gas-solid fluidised beds.
PhD Thesis, TU Delft.
\endverbatim
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2011-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand Down Expand Up @@ -30,7 +30,7 @@ Description
Reference:
\verbatim
Enwald, H., Peirano, E., & Almstedt, A. E. (1996).
Eulerian two-phase flow theory applied to fluidization.
Eulerian two-phase flow theory applied to fluidisation.
International Journal of Multiphase Flow, 22, 21-66.
Eq. 86-87, p. 40.
\endverbatim
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2019-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2019-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand All @@ -25,7 +25,7 @@ Class
Foam::heatTransferModels::Gunn
Description
Gunn (1978) correlation for fixed and fluidized beds with Re < 10^5
Gunn (1978) correlation for fixed and fluidised beds with Re < 10^5
and continuous phase fraction between 0.35 and 1.
Reference:
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2014-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2014-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand Down Expand Up @@ -31,7 +31,7 @@ Description
\verbatim
Reuge, N., Cadoret, L., Coufort-Saudejaud, C., Pannala, S., Syamlal, M.,
& Caussat, B. (2008).
Multifluid Eulerian modeling of dense gas–solids fluidized bed
Multifluid Eulerian modeling of dense gas–solids fluidised bed
hydrodynamics: influence of the dissipation parameters.
Chemical Engineering Science, 63(22), 5540-5551.
\endverbatim
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2014-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2014-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand Down Expand Up @@ -31,7 +31,7 @@ Description
\verbatim
Reuge, N., Cadoret, L., Coufort-Saudejaud, C., Pannala, S., Syamlal, M.,
& Caussat, B. (2008).
Multifluid Eulerian modeling of dense gas–solids fluidized bed
Multifluid Eulerian modeling of dense gas–solids fluidised bed
hydrodynamics: influence of the dissipation parameters.
Chemical Engineering Science, 63(22), 5540-5551.
\endverbatim
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Expand Up @@ -31,7 +31,7 @@ Description
\verbatim
van Wachem, B. G. M. (2000).
Derivation, implementation, and validation of computer simulation models
for gas-solid fluidized beds.
for gas-solid fluidised beds.
PhD Thesis, TU Delft.
\endverbatim
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2019-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2019-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand All @@ -26,7 +26,7 @@ Class
Description
Base class for modeling shape, i.e. a physical diameter of a sizeGroup.
This diameter may then be utilized for calculation of breakup, coalescence
This diameter may then be utilised for calculation of breakup, coalescence
or drift rates, depending on the model implementation.
SourceFiles
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Expand Up @@ -68,7 +68,7 @@ class phaseModel
label index_;

//- Return the residual phase-fraction for given phase
// Used to stabilize the phase momentum as the phase-fraction -> 0
// Used to stabilise the phase momentum as the phase-fraction -> 0
dimensionedScalar residualAlpha_;

//- Optional maximum phase-fraction (e.g. packing limit)
Expand Down Expand Up @@ -185,7 +185,7 @@ public:
const phaseSystem& fluid() const;

//- Return the residual phase-fraction for given phase
// Used to stabilize the phase momentum as the phase-fraction -> 0
// Used to stabilise the phase momentum as the phase-fraction -> 0
const dimensionedScalar& residualAlpha() const;

//- Return the maximum phase-fraction (e.g. packing limit)
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2019-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2019-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand Down Expand Up @@ -98,7 +98,7 @@ Description
\rho_c | Density of continuous phase [kg/m^3]
\eta | Kolmogorov length scale [m]
\Gamma(a,z) | Upper incomplete gamma function
Q(a,z) | Regularized upper incomplete gamma function
Q(a,z) | Regularised upper incomplete gamma function
\Gamma(a) | Gamma function
\endvartable
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2019-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2019-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand All @@ -25,7 +25,7 @@ Class
Foam::diameterModels::coalescenceModels::BrownianCollisions
Description
Model describing coagulation due to Brownian motion. Utilizes collisional
Model describing coagulation due to Brownian motion. Utilises collisional
diameters and the Cunningham slip correction. The slip correction
coefficient is implemented in the following form:
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========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2019-2020 OpenFOAM Foundation
\\ / A nd | Copyright (C) 2019-2021 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
License
Expand All @@ -26,7 +26,7 @@ Class
Description
Interpolation formula of Dahneke (1983) as presented by Otto et al. (1999).
Utilizes collisional diameters.
Utilises collisional diameters.
References:
\verbatim
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