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STYLE: some general spelling fixes

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This commit is contained in:
Mark Olesen
2020-05-04 09:15:21 +02:00
parent 2a24bab057
commit 8cfb483054
234 changed files with 332 additions and 340 deletions
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4
applications/solvers/combustion/PDRFoam/PDRFoam.C
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@ -35,7 +35,7 @@ Description
Combusting RANS code using the b-Xi two-equation model.
Xi may be obtained by either the solution of the Xi transport
equation or from an algebraic exression. Both approaches are
equation or from an algebraic expression. Both approaches are
based on Gulder's flame speed correlation which has been shown
to be appropriate by comparison with the results from the
spectral model.
@ -66,7 +66,7 @@ Description
CR | Drag tensor (1/m)
CT | Turbulence generation parameter (1/m)
Nv | Number of obstacles in cell per unit volume (m^-2)
nsv | Tensor whose diagonal indicates the number to substract from
nsv | Tensor whose diagonal indicates the number to subtract from
| Nv to get the number of obstacles crossing the flow in each
| direction.
\endplaintable

2
applications/solvers/combustion/PDRFoam/PDRFoamAutoRefine.C
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@ -32,7 +32,7 @@ Description
Combusting RANS code using the b-Xi two-equation model.
Xi may be obtained by either the solution of the Xi transport
equation or from an algebraic exression. Both approaches are
equation or from an algebraic expression. Both approaches are
based on Gulder's flame speed correlation which has been shown
to be appropriate by comparison with the results from the
spectral model.

2
applications/solvers/combustion/PDRFoam/setDeltaT.H
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@ -28,7 +28,7 @@ Global
Description
Reset the timestep to maintain a constant maximum courant Number.
Reduction of time-step is imediate but increase is damped to avoid
Reduction of time-step is immediate but increase is damped to avoid
unstable oscillations.
\*---------------------------------------------------------------------------*/

2
applications/solvers/combustion/XiFoam/XiDyMFoam/XiDyMFoam.C
View File

@ -36,7 +36,7 @@ Description
Combusting RANS code using the b-Xi two-equation model.
Xi may be obtained by either the solution of the Xi transport
equation or from an algebraic exression. Both approaches are
equation or from an algebraic expression. Both approaches are
based on Gulder's flame speed correlation which has been shown
to be appropriate by comparison with the results from the
spectral model.

2
applications/solvers/combustion/XiFoam/XiEngineFoam/XiEngineFoam.C
View File

@ -31,7 +31,7 @@ Description
Combusting RANS code using the b-Xi two-equation model.
Xi may be obtained by either the solution of the Xi transport
equation or from an algebraic exression. Both approaches are
equation or from an algebraic expression. Both approaches are
based on Gulder's flame speed correlation which has been shown
to be appropriate by comparison with the results from the
spectral model.

2
applications/solvers/combustion/XiFoam/XiFoam.C
View File

@ -35,7 +35,7 @@ Description
Combusting RANS code using the b-Xi two-equation model.
Xi may be obtained by either the solution of the Xi transport
equation or from an algebraic exression. Both approaches are
equation or from an algebraic expression. Both approaches are
based on Gulder's flame speed correlation which has been shown
to be appropriate by comparison with the results from the
spectral model.

2
applications/solvers/multiphase/MPPICInterFoam/MPPICInterFoam.C
View File

@ -119,7 +119,7 @@ int main(int argc, char *argv[])
alphac = max(1.0 - kinematicCloud.theta(), alphacMin);
alphac.correctBoundaryConditions();
Info<< "Continous phase-1 volume fraction = "
Info<< "Continuous phase-1 volume fraction = "
<< alphac.weightedAverage(mesh.Vsc()).value()
<< " Min(alphac) = " << min(alphac).value()
<< " Max(alphac) = " << max(alphac).value()

2
applications/solvers/multiphase/cavitatingFoam/setDeltaT.H
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@ -28,7 +28,7 @@ Global
Description
Reset the timestep to maintain a constant maximum courant Number.
Reduction of time-step is imediate but increase is damped to avoid
Reduction of time-step is immediate but increase is damped to avoid
unstable oscillations.
\*---------------------------------------------------------------------------*/

2
applications/solvers/multiphase/compressibleMultiphaseInterFoam/multiphaseMixtureThermo/alphaContactAngle/alphaContactAngleFvPatchScalarField.H
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@ -28,7 +28,7 @@ Class
Description
Contact-angle boundary condition for multi-phase interface-capturing
simulations. Used in conjuction with multiphaseMixture.
simulations. Used in conjunction with multiphaseMixture.
SourceFiles
alphaContactAngleFvPatchScalarField.C

2
applications/solvers/multiphase/icoReactingMultiphaseInterFoam/massTransferModels/InterfaceCompositionModel/InterfaceCompositionModel.H
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@ -143,7 +143,7 @@ public:
const volScalarField& Tf
) const;
//- Reference mass fraction for specied based models
//- Reference mass fraction for species based models
virtual tmp<volScalarField> Yf
(
const word& speciesName,

2
applications/solvers/multiphase/icoReactingMultiphaseInterFoam/massTransferModels/Lee/Lee.H
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@ -27,7 +27,7 @@ Class
Foam::meltingEvaporationModels::Lee
Description
Mass tranfer Lee model. Simple model driven by field value difference as:
Mass transfer Lee model. Simple model driven by field value difference as:
\f[
\dot{m} = C \rho \alpha (T - T_{activate})/T_{activate}

2
applications/solvers/multiphase/icoReactingMultiphaseInterFoam/massTransferModels/interfaceCompositionModel/interfaceCompositionModel.H
View File

@ -27,7 +27,7 @@ Class
Foam::interfaceCompositionModel
Description
Generic base class for interface models. Mass transer models are
Generic base class for interface models. Mass transfer models are
interface models between two thermos.
Abstract class for mass transfer functions

6
applications/solvers/multiphase/icoReactingMultiphaseInterFoam/massTransferModels/kineticGasEvaporation/kineticGasEvaporation.H
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@ -40,7 +40,7 @@ Description
Flux | mass flux rate [kg/s/m2]
M | molecular weight
T_{activate} | saturation temperature
C | accomodation coefficient
C | accommodation coefficient
R | universal gas constant
p_{sat} | saturation pressure
p | vapor partial pressure
@ -70,7 +70,7 @@ Description
(T - T_{activate})
\f]
This assumes liquid and vapour are in equilibrium, then the accomodation
This assumes liquid and vapour are in equilibrium, then the accommodation
coefficient are equivalent for the interface. This relation is known as the
Hertz-Knudsen-Schrage.
@ -145,7 +145,7 @@ class kineticGasEvaporation
//- Activation temperature
const dimensionedScalar Tactivate_;
//- Molar weight of the vapour in the continous phase
//- Molar weight of the vapour in the continuous phase
dimensionedScalar Mv_;
//- Interface area

4
applications/solvers/multiphase/icoReactingMultiphaseInterFoam/phasesSystem/phaseSystem/phaseSystem.H
View File

@ -267,7 +267,7 @@ public:
// Energy related thermo functionaliy functions
//- Return access to the inernal energy field [J/Kg]
//- Return access to the internal energy field [J/Kg]
// \note this mixture thermo is prepared to work with T
virtual volScalarField& he()
{
@ -275,7 +275,7 @@ public:
return const_cast<volScalarField&>(volScalarField::null());
}
//- Return access to the inernal energy field [J/Kg]
//- Return access to the internal energy field [J/Kg]
// \note this mixture thermo is prepared to work with T
virtual const volScalarField& he() const
{

2
applications/solvers/multiphase/multiphaseEulerFoam/multiphaseSystem/alphaContactAngle/alphaContactAngleFvPatchScalarField.H
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@ -28,7 +28,7 @@ Class
Description
Contact-angle boundary condition for multi-phase interface-capturing
simulations. Used in conjuction with multiphaseSystem.
simulations. Used in conjunction with multiphaseSystem.
SourceFiles
alphaContactAngleFvPatchScalarField.C

2
applications/solvers/multiphase/multiphaseEulerFoam/multiphaseSystem/multiphaseSystem.H
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@ -31,7 +31,7 @@ Description
Incompressible multi-phase mixture with built in solution for the
phase fractions with interface compression for interface-capturing.
Derived from transportModel so that it can be unsed in conjunction with
Derived from transportModel so that it can be unused in conjunction with
the incompressible turbulence models.
Surface tension and contact-angle is handled for the interface

2
applications/solvers/multiphase/multiphaseInterFoam/multiphaseMixture/alphaContactAngle/alphaContactAngleFvPatchScalarField.H
View File

@ -28,7 +28,7 @@ Class
Description
Contact-angle boundary condition for multi-phase interface-capturing
simulations. Used in conjuction with multiphaseMixture.
simulations. Used in conjunction with multiphaseMixture.
SourceFiles
alphaContactAngleFvPatchScalarField.C

2
applications/solvers/multiphase/multiphaseInterFoam/multiphaseMixture/multiphaseMixture.H
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@ -30,7 +30,7 @@ Description
Incompressible multi-phase mixture with built in solution for the
phase fractions with interface compression for interface-capturing.
Derived from transportModel so that it can be unsed in conjunction with
Derived from transportModel so that it can be unused in conjunction with
the incompressible turbulence models.
Surface tension and contact-angle is handled for the interface