CoolProp.CoolProp module

class CoolProp.CoolProp.AbstractState(self, arg0: str, arg1: str, /)

Bases: object

Bvirial

Cvirial

PIP

Prandtl

Q

Qmass

T

T_critical

T_reducing

Tmax

Tmin

Ttriple

acentric_factor

all_critical_points

alpha0

alphar

apply_simple_mixing_rule

available_in_high_level

backend_name

build_options_json

build_phase_envelope

build_spinodal

change_EOS

chemical_potential

clear

compressibility_factor

conductivity

conductivity_contributions

conformal_state

cp0mass

cp0molar

cpmass

cpmolar

criticality_contour_values

cvmass

cvmolar

d2alpha0_dDelta2

d2alpha0_dDelta_dTau

d2alpha0_dTau2

d2alphar_dDelta2

d2alphar_dDelta_dTau

d2alphar_dTau2

d3alpha0_dDelta2_dTau

d3alpha0_dDelta3

d3alpha0_dDelta_dTau2

d3alpha0_dTau3

d3alphar_dDelta2_dTau

d3alphar_dDelta3

d3alphar_dDelta_dTau2

d3alphar_dTau3

d4alphar_dDelta2_dTau2

d4alphar_dDelta3_dTau

d4alphar_dDelta4

d4alphar_dDelta_dTau3

d4alphar_dTau4

dBvirial_dT

dCvirial_dT

dalpha0_dDelta

dalpha0_dTau

dalphar_dDelta

dalphar_dTau

delta

dipole_moment

fast_evaluate

first_partial_deriv

first_saturation_deriv

first_two_phase_deriv

first_two_phase_deriv_splined

fluid_names

fluid_param_string

fugacity

fugacity_coefficient

fundamental_derivative_of_gas_dynamics

gas_constant

get_binary_interaction_double

get_binary_interaction_string

get_fluid_constant

get_fluid_parameter_double

get_mass_fractions

get_mole_fractions

get_phase_envelope_data

get_reducing_state

get_spinodal_data

get_state

gibbsmass

gibbsmass_excess

gibbsmolar

gibbsmolar_excess

gibbsmolar_residual

has_melting_line

helmholtzmass

helmholtzmass_excess

helmholtzmolar

helmholtzmolar_excess

hmass

hmass_excess

hmass_idealgas

hmolar

hmolar_excess

hmolar_idealgas

hmolar_residual

ideal_curve

isobaric_expansion_coefficient

isothermal_compressibility

keyed_output

melting_line

molar_mass

mole_fractions_liquid

mole_fractions_liquid_double

mole_fractions_vapor

mole_fractions_vapor_double

name

neff

p

p_critical

p_triple

phase

pmax

rhomass

rhomass_critical

rhomass_reducing

rhomolar

rhomolar_critical

rhomolar_reducing

saturated_liquid_keyed_output

saturated_vapor_keyed_output

saturation_ancillary

second_partial_deriv

second_saturation_deriv

second_two_phase_deriv

set_T

set_binary_interaction_double

set_binary_interaction_string

set_cubic_alpha_C

set_fluid_parameter_double

set_mass_fractions

set_mole_fractions

set_volu_fractions

smass

smass_excess

smass_idealgas

smolar

smolar_excess

smolar_idealgas

smolar_residual

specify_phase

speed_sound

surface_tension

tangent_plane_distance

tau

trivial_keyed_output

true_critical_point

umass

umass_excess

umass_idealgas

umolar

umolar_excess

umolar_idealgas

unspecify_phase

update

update_QT_pure_superanc

update_with_guesses

using_mass_fractions

using_mole_fractions

using_volu_fractions

viscosity

viscosity_contributions

volumemass_excess

volumemolar_excess

class CoolProp.CoolProp.ChebyshevApproximation1D(self, expansions: collections.abc.Sequence[CoolProp.CoolProp.ChebyshevExpansion])

Bases: object

count_x_for_y_many

eval_many

get_x_for_y

is_monotonic

monotonic_intervals

xmax

xmin

class CoolProp.CoolProp.ChebyshevExpansion(self, xmin: float, xmax: float, coef: collections.abc.Sequence[float])

Bases: object

coeff

eval_many

solve_for_x

solve_for_x_many

xmax

xmin

class CoolProp.CoolProp.CriticalState(self)

Bases: SimpleState

property stable

(self) -> bool

class CoolProp.CoolProp.GuessesStructure(self)

Bases: object

property T

(self) -> float

clear

property hmolar

(self) -> float

property p

(self) -> float

property rhomolar

(self) -> float

property rhomolar_liq

(self) -> float

property rhomolar_vap

(self) -> float

property smolar

(self) -> float

property x

(self) -> list[float]

property y

(self) -> list[float]

class CoolProp.CoolProp.IntervalMatch

Bases: object

property expansioninfo

(self) -> list[CoolProp.CoolProp.MonotonicExpansionMatch]

property xmax

(self) -> float

property xmin

(self) -> float

property ymax

(self) -> float

property ymin

(self) -> float

class CoolProp.CoolProp.MonotonicExpansionMatch

Bases: object

property idx

(self) -> int

property xmax

(self) -> float

property xmin

(self) -> float

property ymax

(self) -> float

property ymin

(self) -> float

class CoolProp.CoolProp.PhaseEnvelopeData(self)

Bases: object

property K

(self) -> list[list[float]]

property Q

(self) -> list[float]

property T

(self) -> list[float]

property conductivity_liq

(self) -> list[float]

property conductivity_vap

(self) -> list[float]

property cpmolar_liq

(self) -> list[float]

property cpmolar_vap

(self) -> list[float]

property cvmolar_liq

(self) -> list[float]

property cvmolar_vap

(self) -> list[float]

property hmolar_liq

(self) -> list[float]

property hmolar_vap

(self) -> list[float]

property lnK

(self) -> list[list[float]]

property lnT

(self) -> list[float]

property lnp

(self) -> list[float]

property lnrhomolar_liq

(self) -> list[float]

property lnrhomolar_vap

(self) -> list[float]

property p

(self) -> list[float]

property rhomolar_liq

(self) -> list[float]

property rhomolar_vap

(self) -> list[float]

property smolar_liq

(self) -> list[float]

property smolar_vap

(self) -> list[float]

property speed_sound_vap

(self) -> list[float]

property viscosity_liq

(self) -> list[float]

property viscosity_vap

(self) -> list[float]

property x

(self) -> list[list[float]]

property y

(self) -> list[list[float]]

CoolProp.CoolProp.PyCriticalState

alias of CriticalState

CoolProp.CoolProp.PyGuessesStructure

alias of GuessesStructure

CoolProp.CoolProp.PyPhaseEnvelopeData

alias of PhaseEnvelopeData

CoolProp.CoolProp.PySpinodalData

alias of SpinodalData

class CoolProp.CoolProp.SimpleState(self)

Bases: object

property T

(self) -> float

property p

(self) -> float

property rhomolar

(self) -> float

class CoolProp.CoolProp.SpinodalData(self)

Bases: object

property M1

(self) -> list[float]

property delta

(self) -> list[float]

property tau

(self) -> list[float]

class CoolProp.CoolProp.SuperAncillary(self, json_as_string: str)

Bases: object

eval_sat

eval_sat_many

class CoolProp.CoolProp.configuration_keys(value, names=<not given>, *values, module=None, qualname=None, type=None, start=1, boundary=None)

Bases: IntEnum

ALLOW_SVDSBTL_IN_PROPSSI = 33

ALTERNATIVE_REFPROP_HMX_BNC_PATH = 7

ALTERNATIVE_REFPROP_LIBRARY_PATH = 8

ALTERNATIVE_REFPROP_PATH = 6

ALTERNATIVE_SVDTABLES_DIRECTORY = 5

ALTERNATIVE_TABLES_DIRECTORY = 4

ASSUME_CRITICAL_POINT_STABLE = 26

CRITICAL_SPLINES_ENABLED = 2

CRITICAL_WITHIN_1UK = 1

DONT_CHECK_PROPERTY_LIMITS = 16

ENABLE_MELTING_CALORIC_HS = 30

ENABLE_SUPERANCILLARIES = 29

FLOAT_PUNCTUATION = 28

HENRYS_LAW_TO_GENERATE_VLE_GUESSES = 17

HSU_D_TWOPHASE_EOS_POLISH = 31

LIST_STRING_DELIMITER = 32

MAXIMUM_TABLE_DIRECTORY_SIZE_IN_GB = 15

MIXTURE_STABILITY_ALGORITHM = 36

NORMALIZE_GAS_CONSTANTS = 0

OVERWRITE_BINARY_INTERACTION = 24

OVERWRITE_DEPARTURE_FUNCTION = 23

OVERWRITE_FLUIDS = 22

PHASE_ENVELOPE_STARTING_PRESSURE_PA = 18

REFPROP_DONT_ESTIMATE_INTERACTION_PARAMETERS = 9

REFPROP_ERROR_THRESHOLD = 12

REFPROP_IGNORE_ERROR_ESTIMATED_INTERACTION_PARAMETERS = 10

REFPROP_RESOLVE_COOLPROP_ALIASES = 14

REFPROP_USE_GERG = 11

REFPROP_USE_PENGROBINSON = 13

R_U_CODATA = 19

SAVE_RAW_TABLES = 3

SPINODAL_MINIMUM_DELTA = 21

SVDSBTL_SAMPLING_THREADS = 34

TABULAR_NX = 35

TABULAR_NY = 37

USE_GUESSES_IN_PROPSSI = 25

VTPR_ALWAYS_RELOAD_LIBRARY = 27

VTPR_UNIFAC_PATH = 20

class CoolProp.CoolProp.fast_evaluate_status(value, names=<not given>, *values, module=None, qualname=None, type=None, start=1, boundary=None)

Bases: IntEnum

fast_evaluate_internal_error = 5

fast_evaluate_ok = 0

fast_evaluate_out_of_range = 1

fast_evaluate_two_phase_disallowed = 2

fast_evaluate_unsupported_input = 3

fast_evaluate_unsupported_output = 4

class CoolProp.CoolProp.fluid_types(value, names=<not given>, *values, module=None, qualname=None, type=None, start=1, boundary=None)

Bases: IntEnum

FLUID_TYPE_INCOMPRESSIBLE_LIQUID = 3

FLUID_TYPE_INCOMPRESSIBLE_SOLUTION = 4

FLUID_TYPE_PSEUDOPURE = 1

FLUID_TYPE_PURE = 0

FLUID_TYPE_REFPROP = 2

FLUID_TYPE_UNDEFINED = 5

class CoolProp.CoolProp.input_pairs(value, names=<not given>, *values, module=None, qualname=None, type=None, start=1, boundary=None)

Bases: IntEnum

DmassHmass_INPUTS = 38

DmassP_INPUTS = 26

DmassQ_INPUTS = 15

DmassQmass_INPUTS = 16

DmassSmass_INPUTS = 40

DmassT_INPUTS = 18

DmassUmass_INPUTS = 42

DmolarHmolar_INPUTS = 39

DmolarP_INPUTS = 27

DmolarQ_INPUTS = 13

DmolarQmass_INPUTS = 14

DmolarSmolar_INPUTS = 41

DmolarT_INPUTS = 19

DmolarUmolar_INPUTS = 43

HmassP_INPUTS = 28

HmassQ_INPUTS = 11

HmassQmass_INPUTS = 12

HmassSmass_INPUTS = 34

HmassT_INPUTS = 21

HmolarP_INPUTS = 29

HmolarQ_INPUTS = 9

HmolarQmass_INPUTS = 10

HmolarSmolar_INPUTS = 35

HmolarT_INPUTS = 20

INPUT_PAIR_INVALID = 0

PQ_INPUTS = 3

PQmass_INPUTS = 4

PSmass_INPUTS = 30

PSmolar_INPUTS = 31

PT_INPUTS = 17

PUmass_INPUTS = 32

PUmolar_INPUTS = 33

QSmass_INPUTS = 7

QSmolar_INPUTS = 5

QT_INPUTS = 1

QmassSmass_INPUTS = 8

QmassSmolar_INPUTS = 6

QmassT_INPUTS = 2

SmassT_INPUTS = 23

SmassUmass_INPUTS = 36

SmolarT_INPUTS = 22

SmolarUmolar_INPUTS = 37

TUmass_INPUTS = 25

TUmolar_INPUTS = 24

class CoolProp.CoolProp.parameters(value, names=<not given>, *values, module=None, qualname=None, type=None, start=1, boundary=None)

Bases: IntEnum

INVALID_PARAMETER = 0

iBvirial = 69

iCp0mass = 44

iCp0molar = 29

iCpmass = 43

iCpmolar = 28

iCvirial = 70

iCvmass = 45

iCvmolar = 30

iDelta = 24

iDmass = 40

iDmolar = 25

iFH = 81

iGWP100 = 79

iGWP20 = 78

iGWP500 = 80

iGmass = 47

iGmolar = 32

iGmolar_residual = 36

iHH = 82

iHelmholtzmass = 48

iHelmholtzmolar = 33

iHmass = 41

iHmass_idealgas = 49

iHmolar = 26

iHmolar_idealgas = 37

iHmolar_residual = 34

iODP = 84

iP = 20

iPH = 83

iPIP = 74

iP_critical = 10

iP_max = 16

iP_min = 17

iP_reducing = 11

iP_triple = 13

iPhase = 85

iPrandtl = 55

iQ = 21

iQmass = 22

iSmass = 42

iSmass_idealgas = 50

iSmolar = 27

iSmolar_idealgas = 38

iSmolar_residual = 35

iT = 19

iT_critical = 7

iT_freeze = 77

iT_max = 15

iT_min = 14

iT_reducing = 6

iT_triple = 12

iTau = 23

iUmass = 46

iUmass_idealgas = 51

iUmolar = 31

iUmolar_idealgas = 39

iZ = 73

iacentric_factor = 3

ialpha0 = 64

ialphar = 61

iconductivity = 53

id2alpha0_ddelta2_consttau = 67

id3alpha0_ddelta3_consttau = 68

idBvirial_dT = 71

idCvirial_dT = 72

idalpha0_ddelta_consttau = 66

idalpha0_dtau_constdelta = 65

idalphar_ddelta_consttau = 63

idalphar_dtau_constdelta = 62

idipole_moment = 18

ifraction_max = 76

ifraction_min = 75

ifundamental_derivative_of_gas_dynamics = 60

igas_constant = 1

iisentropic_expansion_coefficient = 59

iisobaric_expansion_coefficient = 58

iisothermal_compressibility = 57

imolar_mass = 2

irhomass_critical = 9

irhomass_reducing = 8

irhomolar_critical = 5

irhomolar_reducing = 4

ispeed_sound = 56

isurface_tension = 54

iundefined_parameter = 86

iviscosity = 52

class CoolProp.CoolProp.phases(value, names=<not given>, *values, module=None, qualname=None, type=None, start=1, boundary=None)

Bases: IntEnum

iphase_critical_point = 4

iphase_gas = 5

iphase_liquid = 0

iphase_not_imposed = 8

iphase_supercritical = 1

iphase_supercritical_gas = 2

iphase_supercritical_liquid = 3

iphase_twophase = 6

iphase_unknown = 7