Python Wrapper¶
PyFluids (3-party wrapper)¶
It is a simple, full-featured, lightweight CoolProp wrapper for Python. PyFluids gets published on PyPI, so you can easily install it using:
pip install pyfluids
All CoolProp features are included: thermophysical properties of pure fluids, mixtures and humid air. Also you can easily convert the results to a JSON string or Python dict, add new properties or inputs for lookups, and more.
Benefits¶
Easy to use: all fluids and properties are at hand, no need to remember CoolProp keys.
Processes for fluids and humid air are included: there is no need to code it anymore.
User-friendly interface: writing code is faster.
Examples¶
To calculate the specific heat of saturated water vapor at 1 atm:
from pyfluids import Fluid, FluidsList
water_vapour = Fluid(FluidsList.Water).dew_point_at_pressure(101325)
print(water_vapour.specific_heat) # 2079.937085633241
To calculate the dynamic viscosity of propylene glycol aqueous solution with 60 % mass fraction at 100 kPa and -20 °C:
from pyfluids import Fluid, FluidsList, Input
propylene_glycol = Fluid(FluidsList.MPG, 60).with_state(
Input.pressure(100e3), Input.temperature(-20)
)
print(propylene_glycol.dynamic_viscosity) # 0.13907391053938878
To calculate the density of ethanol aqueous solution (with ethanol 40 % mass fraction) at 200 kPa and 4 °C:
from pyfluids import Mixture, FluidsList, Input
mixture = Mixture([FluidsList.Water, FluidsList.Ethanol], [60, 40]).with_state(
Input.pressure(200e3), Input.temperature(4)
)
print(mixture.density) # 883.3922771627963
To calculate the wet bulb temperature of humid air at 99 kPa, 30 °C and 50 % relative humidity:
from pyfluids import HumidAir, InputHumidAir
humid_air = HumidAir().with_state(
InputHumidAir.pressure(99e3),
InputHumidAir.temperature(30),
InputHumidAir.relative_humidity(50),
)
print(humid_air.wet_bulb_temperature) # 21.946578559079228
For any questions or more examples, see PyFluids on GitHub.
Automatic installation¶
Using the pip
installation program, you can install the official release from the pypi server using:
pip install CoolProp
There are also unofficial Conda packages available from the conda-forge
channel. To
install, use:
conda install conda-forge::coolprop
If you dare, you can also try the latest nightly release from Python or get it directly from the development server using:
pip install -vvv --pre --trusted-host www.coolprop.dreamhosters.com --find-links http://www.coolprop.dreamhosters.com/binaries/Python/ -U --no-cache --force-reinstall CoolProp
Manual installation¶
Compilation of the python wrapper requires a few common wrapper pre-requisites
On all platforms, if it is not already there, you need Cython to be installed:
sudo pip install Cython
Then, follow the commands:
# Check out the sources for CoolProp
git clone https://github.com/CoolProp/CoolProp --recursive
# Move into the folder you just created
cd CoolProp/wrappers/Python
# Start the installation
sudo python setup.py install
If you would like to install CoolProp just for a given version of Python (for
example if python
links to python3.4
and you also have a python2.7
executable), simply use this version of python to execute the setup.py
script:
sudo python2.7 setup.py install
If you have multiple versions of Visual Studio installed and need to specify the version to use and choice of 32-bit or 64-bit compilation, you can use:
# 64-bit using VS2008 on Pytnon 2.7
sudo python setup.py install --cmake-compiler vc9 --cmake-bitness 64
or, equivalently:
sudo python setup.py install cmake=vc9,64
Omitting the cmake options will use the default (latest) compiler on the machine.
Local installation¶
If you prefer not to be sudoer when compiling coolprop on Linux/MacOS, you can
also install it locally using the --user
switch:
# Check out the sources for CoolProp
git clone https://github.com/CoolProp/CoolProp --recursive
# Move into the folder you just created
cd CoolProp/wrappers/Python
# Start the installation
python setup.py install --user
For Pyzo users¶
Suppose the directory containing pyzo is on your Desktop in
~/Desktop/pyzo2014a/
. Then you can install CoolProp to be used within pyzo
by following the same lines as above:
# Check out the sources for CoolProp
git clone https://github.com/CoolProp/CoolProp --recursive
# Move into the folder you just created
cd CoolProp/wrappers/Python
# Start the installation (~/Desktop/pyzo2014a/ to be changed according to
# your effective installation)
sudo ~/Desktop/pyzo2014a/bin/python setup.py install
Usage¶
There is example code at the end of this page
Once installed, you can use CoolProp for various things:
Compute special values in SI units:
import CoolProp.CoolProp as CP fluid = 'Water' pressure_at_critical_point = CP.PropsSI(fluid,'pcrit') # Massic volume (in m^3/kg) is the inverse of density # (or volumic mass in kg/m^3). Let's compute the massic volume of liquid # at 1bar (1e5 Pa) of pressure vL = 1/CP.PropsSI('D','P',1e5,'Q',0,fluid) # Same for saturated vapor vG = 1/CP.PropsSI('D','P',1e5,'Q',1,fluid)
Get some nice graphs:
import CoolProp.Plots as CPP ph_plot = CPP.PropertyPlot('Water','Ph') ph_plot.savefig('enthalpy_pressure_graph_for_Water.png')
Solve thermodynamics exercices
Make your own more complex graphs if you feel the graphing interface is lacking something
Make even more complex graphs using 3D stuff
Example Code¶
from __future__ import print_function
from CoolProp import AbstractState
from CoolProp.CoolProp import PhaseSI, PropsSI, get_global_param_string
import CoolProp.CoolProp as CoolProp
from CoolProp.HumidAirProp import HAPropsSI
from math import sin
print("**************** INFORMATION ***************")
print("This example was auto-generated by the language-agnostic dev/scripts/example_generator.py script written by Ian Bell")
print("CoolProp version:", get_global_param_string("version"))
print("CoolProp gitrevision:", get_global_param_string("gitrevision"))
print("CoolProp Fluids:", get_global_param_string("FluidsList"))
# See http://www.coolprop.org/coolprop/HighLevelAPI.html#table-of-string-inputs-to-propssi-function for a list of inputs to high-level interface
print("*********** HIGH LEVEL INTERFACE *****************")
print("Critical temperature of water:", PropsSI("Water", "Tcrit"), "K")
print("Boiling temperature of water at 101325 Pa:", PropsSI("T", "P", 101325, "Q", 0, "Water"), "K")
print("Phase of water at 101325 Pa and 300 K:", PhaseSI("P", 101325, "T", 300, "Water"))
print("c_p of water at 101325 Pa and 300 K:", PropsSI("C", "P", 101325, "T", 300, "Water"), "J/kg/K")
print("c_p of water (using derivatives) at 101325 Pa and 300 K:", PropsSI("d(H)/d(T)|P", "P", 101325, "T", 300, "Water"), "J/kg/K")
print("*********** HUMID AIR PROPERTIES *****************")
print("Humidity ratio of 50% rel. hum. air at 300 K, 101325 Pa:", HAPropsSI("W", "T", 300, "P", 101325, "R", 0.5), "kg_w/kg_da")
print("Relative humidity from last calculation:", HAPropsSI("R", "T", 300, "P", 101325, "W", HAPropsSI("W", "T", 300, "P", 101325, "R", 0.5)), "(fractional)")
print("*********** INCOMPRESSIBLE FLUID AND BRINES *****************")
print("Density of 50% (mass) ethylene glycol/water at 300 K, 101325 Pa:", PropsSI("D", "T", 300, "P", 101325, "INCOMP::MEG-50%"), "kg/m^3")
print("Viscosity of Therminol D12 at 350 K, 101325 Pa:", PropsSI("V", "T", 350, "P", 101325, "INCOMP::TD12"), "Pa-s")
# If you don't have REFPROP installed, disable the following lines
print("*********** REFPROP *****************")
print("REFPROP version:", get_global_param_string("REFPROP_version"))
print("Critical temperature of water:", PropsSI("REFPROP::WATER", "Tcrit"), "K")
print("Boiling temperature of water at 101325 Pa:", PropsSI("T", "P", 101325, "Q", 0, "REFPROP::WATER"), "K")
print("c_p of water at 101325 Pa and 300 K:", PropsSI("C", "P", 101325, "T", 300, "REFPROP::WATER"), "J/kg/K")
print("*********** TABULAR BACKENDS *****************")
TAB = AbstractState("BICUBIC&HEOS", "R245fa")
TAB.update(CoolProp.PT_INPUTS, 101325, 300)
print("Mass density of refrigerant R245fa at 300 K, 101325 Pa:", TAB.rhomass(), "kg/m^3")
print("*********** SATURATION DERIVATIVES (LOW-LEVEL INTERFACE) ***************")
AS_SAT = AbstractState("HEOS", "R245fa")
AS_SAT.update(CoolProp.PQ_INPUTS, 101325, 0)
print("First saturation derivative:", AS_SAT.first_saturation_deriv(CoolProp.iP, CoolProp.iT), "Pa/K")
print("*********** LOW-LEVEL INTERFACE *****************")
AS = AbstractState("HEOS", "Water&Ethanol")
z = [0.5, 0.5]
AS.set_mole_fractions(z)
AS.update(CoolProp.PQ_INPUTS, 101325, 1)
print("Normal boiling point temperature of water and ethanol:", AS.T(), "K")
# If you don't have REFPROP installed, disable the following block
print("*********** LOW-LEVEL INTERFACE (REFPROP) *****************")
AS2 = AbstractState("REFPROP", "METHANEÐANE")
z2 = [0.2, 0.8]
AS2.set_mole_fractions(z2)
AS2.update(CoolProp.QT_INPUTS, 1, 120)
print("Vapor molar density:", AS2.keyed_output(CoolProp.iDmolar), "mol/m^3")
Example Code Output¶
**************** INFORMATION ***************
This example was auto-generated by the language-agnostic dev/scripts/example_generator.py script written by Ian Bell
CoolProp version: 6.6.1dev
CoolProp gitrevision: fb011601daf1c63dec6b394f3ae88850a1b09ffe
CoolProp Fluids: Xenon,Hydrogen,Ethylene,R365MFC,Air,1-Butene,IsoButene,D4,Methanol,R1243zf,MethylLinolenate,R124,ParaDeuterium,n-Propane,R40,Water,OrthoHydrogen,R143a,SulfurHexafluoride,R13I1,R23,HydrogenSulfide,D5,Ethane,n-Octane,SES36,cis-2-Butene,Isohexane,HFE143m,Neopentane,OrthoDeuterium,R227EA,R125,R116,n-Heptane,Ammonia,o-Xylene,R11,n-Nonane,Acetone,trans-2-Butene,R113,Cyclopentane,CarbonDioxide,R114,Propyne,Krypton,R410A,MethylPalmitate,p-Xylene,CycloHexane,DiethylEther,R507A,R123,R407C,CarbonylSulfide,R245fa,EthylBenzene,Oxygen,Fluorine,R32,IsoButane,MM,MDM,R1234ze(Z),CycloPropane,MethylLinoleate,Deuterium,Novec649,D6,R236FA,R1234ze(E),R41,HeavyWater,Ethanol,DimethylCarbonate,Neon,R1336MZZE,NitrousOxide,MD2M,MD4M,RC318,R218,n-Dodecane,n-Decane,Argon,EthyleneOxide,CarbonMonoxide,Toluene,n-Butane,ParaHydrogen,R1233zd(E),R115,R152A,R142b,Dichloroethane,Helium,R404A,R14,m-Xylene,Benzene,R13,SulfurDioxide,R236EA,MethylOleate,Methane,n-Pentane,DimethylEther,n-Undecane,R161,R141b,MD3M,R1234yf,R22,Nitrogen,HydrogenChloride,R21,MethylStearate,R134a,R245ca,Propylene,R12,Isopentane,n-Hexane
*********** HIGH LEVEL INTERFACE *****************
Critical temperature of water: 647.096 K
Boiling temperature of water at 101325 Pa: 373.1242958476844 K
Phase of water at 101325 Pa and 300 K: liquid
c_p of water at 101325 Pa and 300 K: 4180.6357765560715 J/kg/K
c_p of water (using derivatives) at 101325 Pa and 300 K: 4180.6357765560715 J/kg/K
*********** HUMID AIR PROPERTIES *****************
Humidity ratio of 50% rel. hum. air at 300 K, 101325 Pa: 0.011095529705199761 kg_w/kg_da
Relative humidity from last calculation: 0.5000000000000001 (fractional)
*********** INCOMPRESSIBLE FLUID AND BRINES *****************
Density of 50% (mass) ethylene glycol/water at 300 K, 101325 Pa: 1061.1793077204613 kg/m^3
Viscosity of Therminol D12 at 350 K, 101325 Pa: 0.0005228837990955358 Pa-s
*********** REFPROP *****************
REFPROP version: 10.0
Critical temperature of water: 647.096 K
Boiling temperature of water at 101325 Pa: 373.124295847701 K
c_p of water at 101325 Pa and 300 K: 4180.635776575593 J/kg/K
*********** TABULAR BACKENDS *****************
Mass density of refrigerant R245fa at 300 K, 101325 Pa: 5.648128257046375 kg/m^3
*********** SATURATION DERIVATIVES (LOW-LEVEL INTERFACE) ***************
First saturation derivative: 4058.5197550507155 Pa/K
*********** LOW-LEVEL INTERFACE *****************
Normal boiling point temperature of water and ethanol: 357.2729801712649 K
*********** LOW-LEVEL INTERFACE (REFPROP) *****************
Vapor molar density: 0.44146562665387795 mol/m^3
Code Warnings¶
Messages may be issued from the Python CoolProp wrapper via the Python warnings module. This module allows non-fatal warning messages to be issued to the calling program and stdout to warn of improper function usage or deprecation of features. These warnings will, by default, be issued each and every time a suspect call is made to CoolProp. While, the best solution is to correct the calling code according to the message received, sometimes this is difficult to do in a legacy or third party code and can result in many, many warning messages that obscure the output and hinder debugging.
Suppressing warning messages¶
The calling code can suppress or ignore these warning messages by overriding the default warnings filter and changing the behavior of the warnings module. As an example, the following script will result in a DeprecationWarning on each call to the deprecated function Props():
from CoolProp.CoolProp import Props
Rho = Props('D','T',298.15,'P',10000,'R744')
print("R744 Density at {} K and {} kPa = {} kg/m³".format(298.15, 10000, Rho))
H = Props('H','T',298.15,'Q',1,'R134a');
print("R134a Saturated Liquid Enthalpy at {} K = {} kJ/kg".format(298.15, H))
Example output:
TestProps.py:14: DeprecationWarning: Props() function is deprecated; Use the PropsSI() function
Rho = Props('D','T',298.15,'P',10000,'R744')
R744 Density at 298.15 K and 10000 kPa = 817.6273812375758 kg/m³
TestProps.py:16: DeprecationWarning: Props() function is deprecated; Use the PropsSI() function
H = Props('H','T',298.15,'Q',1,'R134a');
R134a Saturated Liquid Enthalpy at 298.15 K = 412.33395323186807 kJ/kg
Legacy applications can create a filter override to ignore all deprecation warnings by including the following code just after the last import from CoolProp, but before any calls to CoolProp:
import warnings
warnings.filterwarnings('ignore', category=DeprecationWarning)
To suppress, for example, only deprecation warning messages that contain the string “Props()”, the second parameter to filterwarnings() can be a pattern matching regular expression:
import warnings
warnings.filterwarnings('ignore', '.*Props()*.', category=DeprecationWarning)
This filter will suppress any DeprecationWarning messages that contain the string “Props()” but will allow all other warning messages to be displayed. The first parameter, ignore, can also be set to once, which will result in a given message to be issued only once and then ignored on further instances.
See Python >>> Module Warnings for more information on using filterwarnings()
Module Documentation¶
- CoolProp package
- Subpackages
- CoolProp.GUI package
- CoolProp.Plots package
- Submodules
- CoolProp.Plots.Common module
Base2DObject
BaseDimension
BasePlot
BasePlot.HI_FACTOR
BasePlot.ID_FACTOR
BasePlot.LINE_PROPS
BasePlot.LO_FACTOR
BasePlot.PROPERTIES
BasePlot.TP_LIMITS
BasePlot.UNIT_SYSTEMS
BasePlot.axis
BasePlot.figure
BasePlot.generate_ranges()
BasePlot.get_Tp_limits()
BasePlot.get_axis_limits()
BasePlot.get_x_y_dydx()
BasePlot.grid()
BasePlot.inline_label()
BasePlot.limits
BasePlot.props
BasePlot.savefig()
BasePlot.set_Tp_limits()
BasePlot.set_axis_limits()
BasePlot.show()
BasePlot.system
BasePlot.title()
BasePlot.xlabel()
BasePlot.ylabel()
BaseQuantity
EURunits
IsoLine
KSIunits
PropertyDict
SIunits
get_critical_point()
interpolate_values_1d()
is_string()
process_fluid_state()
- CoolProp.Plots.ConsistencyPlots module
ConsistencyAxis
ConsistencyFigure
ConsistencyFigure.add_to_pdf()
ConsistencyFigure.calc_Tmax_curve()
ConsistencyFigure.calc_melting_curve()
ConsistencyFigure.calc_saturation_curves()
ConsistencyFigure.plot_Tmax_curve()
ConsistencyFigure.plot_melting_curve()
ConsistencyFigure.plot_saturation_curves()
ConsistencyFigure.savefig()
ConsistencyFigure.tight_layout()
myprint()
split_pair()
split_pair_xy()
- CoolProp.Plots.ConsistencyPlots_pcsaft module
ConsistencyAxis
ConsistencyFigure
ConsistencyFigure.add_to_pdf()
ConsistencyFigure.calc_Tmax_curve()
ConsistencyFigure.calc_melting_curve()
ConsistencyFigure.calc_saturation_curves()
ConsistencyFigure.plot_Tmax_curve()
ConsistencyFigure.plot_melting_curve()
ConsistencyFigure.plot_saturation_curves()
ConsistencyFigure.savefig()
ConsistencyFigure.tight_layout()
myprint()
split_pair()
split_pair_xy()
- CoolProp.Plots.Plots module
- CoolProp.Plots.PsychChart module
- CoolProp.Plots.PsychScript module
- CoolProp.Plots.SimpleCycles module
- CoolProp.Plots.SimpleCyclesCompression module
- CoolProp.Plots.SimpleCyclesExpansion module
- CoolProp.Plots.Tests module
- CoolProp.Plots.psy module
- CoolProp.Plots.Common module
- Module contents
- Submodules
- CoolProp.tests package
- Submodules
- CoolProp.AbstractState module
Bvirial()
Cvirial()
PIP()
Prandtl()
Q()
T()
T_critical()
T_reducing()
Tmax()
Tmin()
Ttriple()
acentric_factor()
all_critical_points()
alpha0()
alphar()
apply_simple_mixing_rule()
backend_name()
build_phase_envelope()
build_spinodal()
change_EOS()
chemical_potential()
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()
dalpha0_dDelta()
dalpha0_dTau()
dalphar_dDelta()
dalphar_dTau()
delta()
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_string()
get_fluid_constant()
get_fluid_parameter_double()
get_mass_fractions()
get_mole_fractions()
get_phase_envelope_data()
get_spinodal_data()
gibbsmass()
gibbsmass_excess()
gibbsmolar()
gibbsmolar_excess()
gibbsmolar_residual()
has_melting_line()
helmholtzmass()
helmholtzmass_excess()
helmholtzmolar()
helmholtzmolar_excess()
hmass()
hmass_excess()
hmolar()
hmolar_excess()
hmolar_residual()
ideal_curve()
isobaric_expansion_coefficient()
isothermal_compressibility()
keyed_output()
melting_line()
molar_mass()
mole_fractions_liquid()
mole_fractions_vapor()
name()
neff()
p()
p_critical()
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_fluid_parameter_double()
set_mass_fractions()
set_mole_fractions()
set_volu_fractions()
smass()
smass_excess()
smolar()
smolar_excess()
smolar_residual()
specify_phase()
speed_sound()
surface_tension()
tangent_plane_distance()
tau()
trivial_keyed_output()
true_critical_point()
umass()
umass_excess()
umolar()
umolar_excess()
unspecify_phase()
update()
update_with_guesses()
viscosity()
viscosity_contributions()
volumemass_excess()
volumemolar_excess()
- CoolProp.BibtexParser module
- CoolProp.CoolProp module
AbstractState
AbstractState.Bvirial()
AbstractState.Cvirial()
AbstractState.PIP()
AbstractState.Prandtl()
AbstractState.Q()
AbstractState.T()
AbstractState.T_critical()
AbstractState.T_reducing()
AbstractState.Tmax()
AbstractState.Tmin()
AbstractState.Ttriple()
AbstractState.acentric_factor()
AbstractState.all_critical_points()
AbstractState.alpha0()
AbstractState.alphar()
AbstractState.apply_simple_mixing_rule()
AbstractState.backend_name()
AbstractState.build_phase_envelope()
AbstractState.build_spinodal()
AbstractState.change_EOS()
AbstractState.chemical_potential()
AbstractState.compressibility_factor()
AbstractState.conductivity()
AbstractState.conductivity_contributions()
AbstractState.conformal_state()
AbstractState.cp0mass()
AbstractState.cp0molar()
AbstractState.cpmass()
AbstractState.cpmolar()
AbstractState.criticality_contour_values()
AbstractState.cvmass()
AbstractState.cvmolar()
AbstractState.d2alpha0_dDelta2()
AbstractState.d2alpha0_dDelta_dTau()
AbstractState.d2alpha0_dTau2()
AbstractState.d2alphar_dDelta2()
AbstractState.d2alphar_dDelta_dTau()
AbstractState.d2alphar_dTau2()
AbstractState.d3alpha0_dDelta2_dTau()
AbstractState.d3alpha0_dDelta3()
AbstractState.d3alpha0_dDelta_dTau2()
AbstractState.d3alpha0_dTau3()
AbstractState.d3alphar_dDelta2_dTau()
AbstractState.d3alphar_dDelta3()
AbstractState.d3alphar_dDelta_dTau2()
AbstractState.d3alphar_dTau3()
AbstractState.d4alphar_dDelta2_dTau2()
AbstractState.d4alphar_dDelta3_dTau()
AbstractState.d4alphar_dDelta4()
AbstractState.d4alphar_dDelta_dTau3()
AbstractState.d4alphar_dTau4()
AbstractState.dalpha0_dDelta()
AbstractState.dalpha0_dTau()
AbstractState.dalphar_dDelta()
AbstractState.dalphar_dTau()
AbstractState.delta()
AbstractState.first_partial_deriv()
AbstractState.first_saturation_deriv()
AbstractState.first_two_phase_deriv()
AbstractState.first_two_phase_deriv_splined()
AbstractState.fluid_names()
AbstractState.fluid_param_string()
AbstractState.fugacity()
AbstractState.fugacity_coefficient()
AbstractState.fundamental_derivative_of_gas_dynamics()
AbstractState.gas_constant()
AbstractState.get_binary_interaction_double
AbstractState.get_binary_interaction_string()
AbstractState.get_fluid_constant()
AbstractState.get_fluid_parameter_double()
AbstractState.get_mass_fractions()
AbstractState.get_mole_fractions()
AbstractState.get_phase_envelope_data()
AbstractState.get_spinodal_data()
AbstractState.gibbsmass()
AbstractState.gibbsmass_excess()
AbstractState.gibbsmolar()
AbstractState.gibbsmolar_excess()
AbstractState.gibbsmolar_residual()
AbstractState.has_melting_line()
AbstractState.helmholtzmass()
AbstractState.helmholtzmass_excess()
AbstractState.helmholtzmolar()
AbstractState.helmholtzmolar_excess()
AbstractState.hmass()
AbstractState.hmass_excess()
AbstractState.hmolar()
AbstractState.hmolar_excess()
AbstractState.hmolar_residual()
AbstractState.ideal_curve()
AbstractState.isobaric_expansion_coefficient()
AbstractState.isothermal_compressibility()
AbstractState.keyed_output()
AbstractState.melting_line()
AbstractState.molar_mass()
AbstractState.mole_fractions_liquid()
AbstractState.mole_fractions_vapor()
AbstractState.name()
AbstractState.neff()
AbstractState.p()
AbstractState.p_critical()
AbstractState.phase()
AbstractState.pmax()
AbstractState.rhomass()
AbstractState.rhomass_critical()
AbstractState.rhomass_reducing()
AbstractState.rhomolar()
AbstractState.rhomolar_critical()
AbstractState.rhomolar_reducing()
AbstractState.saturated_liquid_keyed_output()
AbstractState.saturated_vapor_keyed_output()
AbstractState.saturation_ancillary()
AbstractState.second_partial_deriv()
AbstractState.second_saturation_deriv()
AbstractState.second_two_phase_deriv()
AbstractState.set_binary_interaction_double
AbstractState.set_binary_interaction_string
AbstractState.set_fluid_parameter_double()
AbstractState.set_mass_fractions()
AbstractState.set_mole_fractions()
AbstractState.set_volu_fractions()
AbstractState.smass()
AbstractState.smass_excess()
AbstractState.smolar()
AbstractState.smolar_excess()
AbstractState.smolar_residual()
AbstractState.specify_phase()
AbstractState.speed_sound()
AbstractState.surface_tension()
AbstractState.tangent_plane_distance()
AbstractState.tau()
AbstractState.trivial_keyed_output()
AbstractState.true_critical_point()
AbstractState.umass()
AbstractState.umass_excess()
AbstractState.umolar()
AbstractState.umolar_excess()
AbstractState.unspecify_phase()
AbstractState.update()
AbstractState.update_with_guesses()
AbstractState.viscosity()
AbstractState.viscosity_contributions()
AbstractState.volumemass_excess()
AbstractState.volumemolar_excess()
FluidsList()
HAProps()
HAPropsSI()
HAProps_Aux()
PhaseSI()
Props()
PropsSI()
PyCriticalState
PyGuessesStructure
PyPhaseEnvelopeData
PyPhaseEnvelopeData.K
PyPhaseEnvelopeData.Q
PyPhaseEnvelopeData.T
PyPhaseEnvelopeData.TypeI
PyPhaseEnvelopeData.hmolar_liq
PyPhaseEnvelopeData.hmolar_vap
PyPhaseEnvelopeData.iTsat_max
PyPhaseEnvelopeData.icrit
PyPhaseEnvelopeData.ipsat_max
PyPhaseEnvelopeData.lnT
PyPhaseEnvelopeData.lnp
PyPhaseEnvelopeData.lnrhomolar_liq
PyPhaseEnvelopeData.lnrhomolar_vap
PyPhaseEnvelopeData.p
PyPhaseEnvelopeData.rhomolar_liq
PyPhaseEnvelopeData.rhomolar_vap
PyPhaseEnvelopeData.smolar_liq
PyPhaseEnvelopeData.smolar_vap
PyPhaseEnvelopeData.x
PyPhaseEnvelopeData.y
PySpinodalData
State
State.Fluid
State.MM
State.Phase()
State.Prandtl
State.Props()
State.Q
State.T
State.Tsat
State.copy()
State.cp
State.cp0
State.cv
State.dpdT
State.get_MM()
State.get_Q()
State.get_T()
State.get_Tsat()
State.get_cond()
State.get_cp()
State.get_cp0()
State.get_cv()
State.get_dpdT()
State.get_h()
State.get_p()
State.get_rho()
State.get_s()
State.get_speed_sound()
State.get_subcooling()
State.get_superheat()
State.get_u()
State.get_visc()
State.h
State.k
State.p
State.pAS
State.phase
State.rho
State.s
State.set_Fluid()
State.speed_test()
State.subcooling
State.superheat
State.u
State.update()
State.update_Trho()
State.update_ph()
State.visc
add_fluids_as_JSON()
apply_simple_mixing_rule()
cair_sat()
config_key_description()
extract_backend()
extract_fractions()
generate_update_pair()
get_BibTeXKey()
get_REFPROPname()
get_aliases()
get_config_as_json_string()
get_config_bool()
get_config_double()
get_config_int()
get_config_string()
get_debug_level()
get_errstr()
get_fluid_param_string()
get_global_param_string()
get_mixture_binary_pair_data()
get_mixture_binary_pair_pcsaft()
get_parameter_index()
get_parameter_information()
get_phase_index()
is_trivial_parameter()
rebuildState()
saturation_ancillary()
set_config_as_json_string()
set_config_bool()
set_config_double()
set_config_int()
set_config_string()
set_debug_level()
set_departure_functions()
set_interaction_parameters()
set_mixture_binary_pair_data()
set_mixture_binary_pair_pcsaft()
set_predefined_mixtures()
set_reference_state()
- CoolProp.HumidAirProp module
- CoolProp.State module
- CoolProp.constants module
- CoolProp.AbstractState module
- Module contents
- Subpackages