Ur can be generated using a functionObject or in the post-processor

to use the transport matrix construction in MovingPhaseModel

between incompressible and compressible phases

Now combinations of incompressible, compressible phases with or without
mass-transfer are supported efficiently.

This file contains definitions rather than declarations

This makes looping over the phases much simpler which maintaining
support for phase-name lookup.

Supporting any number of phases with heat and mass transfer, phase-change and reactions

The previous method using a HashTable required a separate ordered list
of names which is hard to work with and maintain.

to allow the turbulent energy transport properties to be updated for
every energy solution if required.

Added correctEnergyTransport() call to reactingTwoPhaseEulerFoam

and two-phase functionality separated from multiphase functionality

Resolved bug-report http://openfoam.org/mantisbt/view.php?id=1831

Includes many contributions from Juho Peltola

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1816

Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1794

Resolves bug-report http://openfoam.org/mantisbt/view.php?id=1805

to simplify construction of dimensionedScalar properties and avoid the
duplication of the name string in the constructor call.

so that the specification of the name and dimensions are optional in property dictionaries.

Update tutorials so that the name of the dimensionedScalar property is
no longer duplicated but optional dimensions are still provided and are
checked on read.

Also removed __GNUC__ conditional compilation statements which are no
longer needed.

The interfacial temperature is assumed equal to the saturation
temperature.  Only a single species is considered volatile and the other
species to not affect the mass-transfer.

Added calls to setFluxRequired for p, p_rgh etc. in all solvers which
avoids the need to add fluxRequired entries in fvSchemes dictionaries.

Currently this is implemented only for the Antoine equation, for the
other more complex models an iterative inversion from pressure to
temperature is required.