Convert to the units used in the plot

Convert to the units used in the plot

Base function to produce polynomials of order len(coefficients) with the coefficients

A helper function to ensure that configuration is not accessed before it is initialized (was formerly static)

Returns the base, non-dimensional, Helmholtz energy term (no derivatives) [-] @param tau Reciprocal reduced temperature where \f$\tau=T_c / T\f$

fast_evaluate: vectorized cache-bypassing batch path. Mirrors update()'s routing per point but writes directly to out_buffer without touching any per

Get the array with coefficients.

Get the mole fractions of the equilibrium liquid phase

Get the mole fractions of the equilibrium vapor phase

Return the name - backend dependent

Check input for state object or fluid string Parameters ---------- fluid_ref : str, CoolProp.AbstractState fractions : str, s

In the secant function, a 1-D Newton-Raphson solver is implemented. An initial guess for the solution is provided. @param f A pointer to an instance

Return thermal conductivity in [W/m-K]

This is just a shorthand function for getting a parameter from ``CoolProp.get_global_param_string``

Read-only accessor for value of R_u (universal gas constant)

Build a SaturationAncillaryFunction from its JSON description. Parses into a plain-typed SaturationAncillaryFunction::Values bundle and constructs fro

Density as a function of temperature, pressure and composition.

Density via CoolProp

Return the vector of critical points, including points that are unstable or correspond to negative pressure

Clear all the cached values

If you only want a single entry from your bibliography and not the whole thing, this function is for you. It uses Pybtex, but removes

Get the reducing density to be used

Solve the objective function using Brent's method and the maximum heat transfer rate calculated from the pinching analysis

Sample `f(p)` at `n_knots` log-uniform points in [p_min, p_max] and build a CubicSplineCurve through the resulting (p, f(p)) knots. This is the common

Returns true if the cell coefficients seem to have been calculated properly

Helper: check that a complex scalar input is Real and return proper Mathcad error

Resolve the backend factory string (e.g. ``SVDSBTL&IF97::Water``) to an AbstractState we keep alive for the whole sweep, paying the surface-lo

A pseudo logger that prints to stdout without line breaks

\brief Change the equation of state for a given component to a specified EOS @param i Index of the component to change (if a pure fluid, i=0) @param E

Get the minimum temperature in K

\brief Return best estimate for the stability of the point */