Get binary mixture string value

Number of times the caloric superancillaries were (re)built. Used by tests to verify the multi-instance / multi-ref-state code path does not cause thr

Get the volume translation parameter

Checking function to see if we should stop the tracing of the critical contour

Get a constant for one of the fluids forming this mixture * @param i Index (0-based) of the fluid * @param param parameter you want to obt

Return a comma-separated list of fluid names

Return a comma-separated list of incompressible pure fluid names

Return a comma-separated list of solution names

Get the kij factor for the ij pair

Accessor for liquid-phase composition and density

Helper: Get IEEE 754 double precision NaN value for returning in case of errors in array outputs

Chebyshev-Lobatto nodes \f$\cos(\pi j/N), j = 0,..., N \f$ mapped to the range [xmin, xmax]

Get the minimum pressure in Pa

Read access to the global prefactor on alpha0 (and its derivatives). Used by the caloric-superancillary shift trick (#2773) so the offset translation

Determine which input pairs are supported

Accessor for vapor-phase composition and density

If a git repo, use git to update the gitrevision. If not a git repo, read the gitrevision from the gitrevision.txt file. Otherwise, fail.

Return true if the string has "BACKEND::*" format where * signifies a wildcard

Compute enthalpy at bubble line ! This function returns the enthalpy at bubble line from the state specified by the properties input Must be re

Leg 3: ideal-gas departure. Scale residual Helmholtz by lambda; anchor at lambda=0 (ideal gas, no dome) and continue lambda:0->1. Self-contained.

Leg 2: supercritical isentrope. Anchor on the dome-free T=Tmax isotherm at the density whose entropy equals s_t, then march (holding s == s_t).

Leg 4: melting-line anchor for the cold compressed-liquid corner (incl. sub-triple T).

Leg 1: saturation anchor. Anchor at the saturated state whose entropy equals the target's (found by the superancillary's native S-inversion), then ma

Cheap superancillary two-phase detector (no EOS): scan the Qh==Qs residual on the caloric superancillary for a sign change with quality strictly insid

Compute enthalpy at dew line ! This function returns the enthalpy at dew line from the state specified by the properties input Must be re-imple

* \brief Calculate an ideal curve for a pure fluid * * @param type The type of ideal curve you would like to calculate - "Ideal", "Boyle", "

Compatiblity with zlib API. See called functions for documentation */

Bind the superancillary classes (Chebyshev rootfinding building blocks + the SuperAncillary saturation evaluator). 1:1 mirror of the legacy Cython su

Inject values for acentric factor for i-th EOS

Inject values for pressure, enthalpy, entropy for critical point

Splice a check_points array (and a source_eos_hash stamp) into the SUPERANCILLARY block as a text edit, so the rest of the file (formatting, n

Inject values for pressure, enthalpy, entropy for reducing point

This will give the coordinates and rotation required to align a label with a line on a plot in axis units.

Mass fraction conversion function If the fluid type is mass-based, it does not do anything. Otherwise, * it converts the mass fraction to the requir

Mole fraction conversion function If the fluid type is mole-based, it does not do anything. Otherwise, * it converts the mole fraction to the requir

Volume fraction conversion function If the fluid type is volume-based, it does not do anything. Otherwise, * it converts the volume fraction to the

Determine the maximum heat transfer rate based on the internal pinching analysis