Compute temperature ! This function returns the temperature from the state specified by the properties input Must be re-implemented in the spec

Return the molar density in mol/m³

Calculate fluid properties for a given state from SI inputs.

Set the mole fractions of the components in the mixtures (not the groups)

Return the molar enthalpy in J/mol

Return the mass density in kg/m³

Return the vapor quality (mol/mol); Q = 0 for saturated liquid

@brief Convenience method to get the number of points in the isoline. ``size() = x.size() = y.size()``. */

Return the mass enthalpy in J/kg

Return the molar entropy in J/mol/K

\brief The first partial derivative in homogeneous phases * * \f[ \left(\frac{\partial A}{\partial B}\right)_C = \frac{\left(\frac{\partial

Compute phase flag ! This function returns the phase flag from the state specified by the properties input Must be re-implemented in the specif

Specify the phase for all further calculations with this state class

This implementation uses the Dymola log and error window to report errors

Update the internal cached derivatives in each departure function

This is a stub overload to help with all the strcmp calls below and avoid needing to rewrite all of them

Return the mass entropy in J/kg/K

Take all the vectors that are in the class and pack them into the vectors map for easy unpacking using msgpack

Some functions related to testing and comparison of values

Unspecify the phase and go back to calculating it based on the inputs

Returns the amount of milliseconds elapsed since the UNIX epoch. Works on both * windows and linux. * Taken from http://stackoverflow.com/questions/

Return the molar internal energy in J/mol

This function implements a 1-D bounded solver using the algorithm from Brent, R. P., Algorithms for Minimization Without Derivatives. Englewood Cliffs