Finds all issues that have been closed after the tag_data

Solve the Rachford-Rice residual sum_i z_i (K_i - 1) / (1 - beta + beta K_i) = 0 for beta on [0, 1] by bisection. The caller ensures the residual do

Image + downloads RST that the fluid page does NOT carry for REFPROP.

dlopen the REFPROP library (refcounted; returns existing handle if already loaded) and dlsym a named symbol, trying the canonical Fortran-mangling var

Update the .version file which is used by pyproject.toml

Return the mass density in kg/m^3

Run a command and handle errors.

\brief The second partial derivative along the saturation curve * * Implementing the algorithms and ideas of: * Matthis Thorade, Ali Sa

Evaluate the cubic on segment [a_i, a_{i+1}] at parameter t in [0,1] given knot values b_i, b_{i+1} and second derivatives M_i, M_{i+1} and segment wi

Split release keys into (keep_keys, delete_keys). Only non-final releases are candidates (``.dev``/pre-release, and ``.post`` defensively).

Set saturation properties from T ! This function sets the saturation properties for the given temperature T. The computed values are written to th

Set the three Twu constants in one shot for the component i of a mixture

Set the alpha function for the i-th component

Set the limits of the internal axis object based on the active units, takes [xmin, xmax, ymin, ymax]

Solve for independent variable given a bracketing interval [a,b] with the use of the TOMS 748 algorithm from boost which is an improvement over Br

Uses the Newton solver to find the roots of p(x_in,y_in)-z_in @param res Poly2DResidual object to calculate residuals and derivatives @param guess dou

T-parameterized cubic-spline sampler. Mirror of spline_through_log_p_samples, but linear-T spacing since the T span over a dome arc is at most factor

Return surface tension in [N/m]

Return the tangent plane distance for a given trial composition w @param T Temperature (K) @param p Pressure (Pa) @param w The trial composition @para

Simple PNG writer function by Alex Evans, 2011. Released into the public domain: https://gist.github.com/908299, more context at http://altdevblo

But actually it doesn't matter since it is only a pure fluid

Validate the EOS that was just constructed

Monotonically increasing counter bumped whenever this alpha function's parameters change; callers that cache term() values (e.g., AbstractCubic::_ensu

T in [K], e_k in [K], sigma in [nm] viscosity returned is in [Pa-s]

Single-Dimensional solvers, refere

COP for a cooling process Calculates the coefficient of performance for a cooling process, :math:`COP_c = \frac{q_{eva}}{w_{comp}}`.

COP for a heating process Calculates the coefficient of performance for a heating process, :math:`COP_h = \frac{q_{con}}{w_{comp}}`.

Move constructor given a vector of expansions

In the secant function, a 1-D Newton-Raphson solver is implemented. An initial guess for the solution is provided. Note that this is different than t

Helper: Determine which of the valid delimiters were passed in a String.