Files
CoolProp/wrappers/Python/CoolProp/cAbstractState.pxd
Ian Bell a53f3cd7cb Fix isobaric_expansion_coefficient; closes #714
Also implement missing python implementation
2015-07-07 21:56:16 -06:00

144 lines
7.3 KiB
Cython

from libcpp cimport bool
from libcpp.string cimport string
from libcpp.vector cimport vector
cimport constants_header
cdef extern from "PhaseEnvelope.h" namespace "CoolProp":
cdef cppclass PhaseEnvelopeData:
bool TypeI
size_t iTsat_max, ipsat_max, icrit
vector[double] T, p, lnT, lnp, rhomolar_liq, rhomolar_vap, lnrhomolar_liq, lnrhomolar_vap, hmolar_liq, hmolar_vap, smolar_liq, smolar_vap, Q
cdef extern from "AbstractState.h" namespace "CoolProp":
cdef cppclass GuessesStructure:
long double T, p, rhomolar, hmolar, smolar
long double rhomolar_liq, rhomolar_vap
double _rhomolar_liq, _rhomolar_vap
vector[long double] x, y
cdef cppclass AbstractState:
## Nullary Constructor
AbstractState() except +ValueError
## Constructor with fluid name
AbstractState(string FluidName) except +ValueError
void set_mole_fractions(vector[double]) except+ValueError
void set_mass_fractions(vector[double]) except+ValueError
void set_volu_fractions(vector[double]) except+ValueError
vector[long double] mole_fractions_liquid() except +ValueError
vector[long double] mole_fractions_vapor() except +ValueError
constants_header.phases phase() except +ValueError
void specify_phase(constants_header.phases phase) except +ValueError
void unspecify_phase() except +ValueError
string name() except +ValueError
bool clear()
## Limits
double Tmin()
double Tmax()
double pmax()
double Ttriple()
void ideal_curve(const string &, vector[double] &T, vector[double] &p) except +ValueError
## Property updater
## Uses the indices in CoolProp for the input parameters
void update(constants_header.input_pairs iInput1, double Value1, double Value2) except +ValueError
## Uses the indices in CoolProp for the input parameters
void update_with_guesses(constants_header.input_pairs iInput1, double Value1, double Value2, GuessesStructure) except +ValueError
## Bulk properties accessors - temperature, pressure and density are directly calculated every time
## All other parameters are calculated on an as-needed basis
## If single-phase, just plug into the EOS, otherwise need to do two-phase analysis
double T() except +ValueError
double rhomolar() except +ValueError
double rhomass() except +ValueError
double p() except +ValueError
double Q() except +ValueError
double hmolar() except +ValueError
double hmass() except +ValueError
double smolar() except +ValueError
double smass() except +ValueError
double umolar() except +ValueError
double umass() except +ValueError
double cpmolar() except +ValueError
double cpmass() except +ValueError
double cp0molar() except +ValueError
double cp0mass() except +ValueError
double cvmolar() except +ValueError
double cvmass() except +ValueError
double speed_sound() except +ValueError
double tau() except +ValueError
double delta() except +ValueError
double viscosity() except+ValueError
double conductivity() except+ValueError
double surface_tension() except+ValueError
double Prandtl() except +ValueError
double Bvirial() except +ValueError
double Cvirial() except +ValueError
double PIP() except +ValueError
double isothermal_compressibility() except +ValueError
double isobaric_expansion_coefficient() except +ValueError
double fugacity(size_t) except +ValueError
double fugacity_coefficient(size_t) except +ValueError
double keyed_output(constants_header.parameters) except+ValueError
double trivial_keyed_output(constants_header.parameters) except+ValueError
double saturated_liquid_keyed_output(constants_header.parameters) except+ValueError
double saturated_vapor_keyed_output(constants_header.parameters) except+ValueError
double molar_mass() except+ValueError
double acentric_factor() except+ValueError
double gas_constant() except+ValueError
long double first_partial_deriv(constants_header.parameters, constants_header.parameters, constants_header.parameters) except+ValueError
long double second_partial_deriv(constants_header.parameters, constants_header.parameters, constants_header.parameters, constants_header.parameters, constants_header.parameters) except+ValueError
long double first_saturation_deriv(constants_header.parameters, constants_header.parameters) except+ValueError
long double second_saturation_deriv(constants_header.parameters, constants_header.parameters, constants_header.parameters) except+ValueError
double first_two_phase_deriv(constants_header.parameters Of, constants_header.parameters Wrt, constants_header.parameters Constant) except+ValueError
double second_two_phase_deriv(constants_header.parameters Of, constants_header.parameters Wrt1, constants_header.parameters Constant1, constants_header.parameters Wrt2, constants_header.parameters Constant2) except+ValueError
double first_two_phase_deriv_splined(constants_header.parameters Of, constants_header.parameters Wrt, constants_header.parameters Constant, double x_end) except+ValueError
void true_critical_point(double &T, double &rho) except +ValueError
double melting_line(int,int,double) except+ValueError
bool has_melting_line() except+ValueError
double saturation_ancillary(constants_header.parameters, int, constants_header.parameters, double) except +ValueError
double build_phase_envelope() except+ValueError
void build_phase_envelope(string) except+ValueError
PhaseEnvelopeData get_phase_envelope_data() except+ValueError
long double alpha0() except+ValueError
long double dalpha0_dDelta() except+ValueError
long double dalpha0_dTau() except+ValueError
long double d2alpha0_dDelta2() except+ValueError
long double d2alpha0_dDelta_dTau() except+ValueError
long double d2alpha0_dTau2() except+ValueError
long double d3alpha0_dTau3() except+ValueError
long double d3alpha0_dDelta_dTau2() except+ValueError
long double d3alpha0_dDelta2_dTau() except+ValueError
long double d3alpha0_dDelta3() except+ValueError
long double alphar() except+ValueError
long double dalphar_dDelta() except+ValueError
long double dalphar_dTau() except+ValueError
long double d2alphar_dDelta2() except+ValueError
long double d2alphar_dDelta_dTau() except+ValueError
long double d2alphar_dTau2() except+ValueError
long double d3alphar_dDelta3() except+ValueError
long double d3alphar_dDelta2_dTau() except+ValueError
long double d3alphar_dDelta_dTau2() except+ValueError
long double d3alphar_dTau3() except+ValueError
# The static factory method for the AbstractState
cdef extern from "AbstractState.h" namespace "CoolProp::AbstractState":
AbstractState* factory(const string &backend, const string &fluid_string) except+ValueError