//- Return the set of times selected based on the argList options
    //  including support for \b -newTimes in which times are selected
    //  if the file <fName> does not exist in the time directory.
    //  Also set the runTime to the first instance or the
    //  \c constant/ directory if no instances are specified or available
    static instantList select
    (
        Time& runTime,
        const argList& args,
        const word& fName
    );

This is experimental functionality and currently on test in the yPlus
post-processing utility.

With the SIMPLE "consistent" option and optimized relaxation factors
this tutorial now converges in 210 iterations, previously with SIMPLE it
took 950.  Despite the increase in cost per time-step due to the
increase in relaxation factors and number of solver iterations the
speed-up is 3.5x.

Resolves feature request http://www.openfoam.org/mantisbt/view.php?id=1759

to support laminar simulations in the new framework.

Unfortunately this allows LES models to be instantiated although they
are not compatible with steady-state simulations.

Resolves feature-request http://www.openfoam.org/mantisbt/view.php?id=1754

Select LTS via the ddtScheme:

ddtSchemes
{
    default         localEuler rDeltaT;
}

The LTS algorithm is controlled with the standard settings in
controlDict, e.g.:

maxCo           0.5;
maxDeltaT       2e-8;

with the addition of the optional rDeltaT smoothing coefficient:

rDeltaTSmoothingCoeff 0.02;

which defaults to 0.02.

For cases with reasonably uniform meshes like the forwardStep tutorial
LTS does not provide much benefit but for cases with large variation in
cell-size like the biconic25-55Run35 tutorial LTS provides significant
speed-up to convergence particularly if started from uniform conditions.

Reverted changes proposed in
http://openfoam.org/mantisbt/view.php?id=1548 as it adversely affects
fixed-value BCs and is formulated to fix an issue with an unphysical
case.  Further analysis of the handling of fixed pressure outlet
conditions as the Mach number approaches 1 is required.

Use the trace as the limiter function for both symmTensor and tensor to
bound the normal stresses rather than the shear stresses.

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1751

Now consistent with the way the Courant number is calculated for other solvers

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1748

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1746

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1749

on the lambda of the film

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1745

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1636

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1157

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1741

pairPatchAgglomeration: Do not use the result agglomeratePatch if the return indicates it is not valid
Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1157

Applying patches provided by Timo Niemi
Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1636

Multi-species, mass-transfer and reaction support and multi-phase
structure provided by William Bainbridge.

Integration of the latest p-U and face-p_U algorithms with William's
multi-phase structure is not quite complete due to design
incompatibilities which needs further development.  However the
integration of the functionality is complete.

The results of the tutorials are not exactly the same for the
twoPhaseEulerFoam and reactingTwoPhaseEulerFoam solvers but are very
similar.  Further analysis in needed to ensure these differences are
physical or to resolve them; in the meantime the twoPhaseEulerFoam
solver will be maintained.

if it depends on the availability of the physical properties of both
phases as the construction of the phase-system may not be complete.

Resolves additional bug-report http://www.openfoam.org/mantisbt/view.php?id=1544

Resolves additional request in http://www.openfoam.org/mantisbt/view.php?id=1544

twoPhaseEulerFoam/interfacialModels/heatTransferModels/sphericalHeatTransfer: new heat-transfer model

Model which applies an analytical solution for heat transfer from the
surface of a sphere to the fluid within the sphere.

Provided by William Bainbridge

This is necessary to guarantee consistency between the residualAlpha
used for drag and buoyancy in a multi-phase system

to allow combustionModel to be used with more general forms of multi-phase

by naming fields including the phase name is needed

i.e. without the group suffix.

Patch provided by William Bainbridge

Applied as a correction pre-factor to the viscosity obtained from a
run-time selectable base-model.