Legacy Chemicals (thermo.chemical)¶
- class thermo.chemical.Chemical(ID, T=298.15, P=101325, autocalc=True)[source]¶
Bases:
objectCreates a Chemical object which contains basic information such as molecular weight and the structure of the species, as well as thermodynamic and transport properties as a function of temperature and pressure.
- Parameters:
- ID
str - One of the following [-]:
Name, in IUPAC form or common form or a synonym registered in PubChem
InChI name, prefixed by ‘InChI=1S/’ or ‘InChI=1/’
InChI key, prefixed by ‘InChIKey=’
PubChem CID, prefixed by ‘PubChem=’
SMILES (prefix with ‘SMILES=’ to ensure smiles parsing)
CAS number
- T
float,optional Temperature of the chemical (default 298.15 K), [K]
- P
float,optional Pressure of the chemical (default 101325 Pa) [Pa]
- ID
- Attributes:
- T
float Temperature of the chemical, [K]
- P
float Pressure of the chemical, [Pa]
- phase
str Phase of the chemical; one of ‘s’, ‘l’, ‘g’, or ‘l/g’.
- ID
str User specified string by which the chemical’s CAS was looked up.
- CAS
str The CAS number of the chemical.
- PubChem
int PubChem Compound identifier (CID) of the chemical; all chemicals are sourced from their database. Chemicals can be looked at online at https://pubchem.ncbi.nlm.nih.gov.
- MW
float Molecular weight of the compound, [g/mol]
- formula
str Molecular formula of the compound.
- atoms
dict dictionary of counts of individual atoms, indexed by symbol with proper capitalization, [-]
- similarity_variable
float Similarity variable, see
chemicals.elements.similarity_variablefor the definition, [mol/g]- smiles
str Simplified molecular-input line-entry system representation of the compound.
- InChI
str IUPAC International Chemical Identifier of the compound.
- InChI_Key
str 25-character hash of the compound’s InChI.
- IUPAC_name
str Preferred IUPAC name for a compound.
- synonyms
listofstrings All synonyms for the compound found in PubChem, sorted by popularity.
- Tm
float Melting temperature [K]
- Tb
float Boiling temperature [K]
- Tc
float Critical temperature [K]
- Pc
float Critical pressure [Pa]
- Vc
float Critical volume [m^3/mol]
- Zc
float Critical compressibility [-]
- rhoc
float Critical density [kg/m^3]
- rhocm
float Critical molar density [mol/m^3]
- omega
float Acentric factor [-]
- StielPolar
float Stiel Polar factor, see
chemicals.acentric.Stiel_polar_factorfor the definition [-]- Tt
float Triple temperature, [K]
- Pt
float Triple pressure, [Pa]
- Hfus
float Enthalpy of fusion [J/kg]
- Hfusm
float Molar enthalpy of fusion [J/mol]
- Hsub
float Enthalpy of sublimation [J/kg]
- Hsubm
float Molar enthalpy of sublimation [J/mol]
- Hfm
float Standard state molar enthalpy of formation, [J/mol]
- Hf
float Standard enthalpy of formation in a mass basis, [J/kg]
- Hfgm
float Ideal-gas molar enthalpy of formation, [J/mol]
- Hfg
float Ideal-gas enthalpy of formation in a mass basis, [J/kg]
- Hcm
float Molar higher heat of combustion [J/mol]
- Hc
float Higher Heat of combustion [J/kg]
- Hcm_lower
float Molar lower heat of combustion [J/mol]
- Hc_lower
float Lower Heat of combustion [J/kg]
- S0m
float Standard state absolute molar entropy of the chemical, [J/mol/K]
- S0
float Standard state absolute entropy of the chemical, [J/kg/K]
- S0gm
float Absolute molar entropy in an ideal gas state of the chemical, [J/mol/K]
- S0g
float Absolute mass entropy in an ideal gas state of the chemical, [J/kg/K]
- Gfm
float Standard state molar change of Gibbs energy of formation [J/mol]
- Gf
float Standard state change of Gibbs energy of formation [J/kg]
- Gfgm
float Ideal-gas molar change of Gibbs energy of formation [J/mol]
- Gfg
float Ideal-gas change of Gibbs energy of formation [J/kg]
- Sfm
float Standard state molar change of entropy of formation, [J/mol/K]
- Sf
float Standard state change of entropy of formation, [J/kg/K]
- Sfgm
float Ideal-gas molar change of entropy of formation, [J/mol/K]
- Sfg
float Ideal-gas change of entropy of formation, [J/kg/K]
- Hcgm
float Higher molar heat of combustion of the chemical in the ideal gas state, [J/mol]
- Hcg
float Higher heat of combustion of the chemical in the ideal gas state, [J/kg]
- Hcgm_lower
float Lower molar heat of combustion of the chemical in the ideal gas state, [J/mol]
- Hcg_lower
float Lower heat of combustion of the chemical in the ideal gas state, [J/kg]
- Tflash
float Flash point of the chemical, [K]
- Tautoignition
float Autoignition point of the chemical, [K]
- LFL
float Lower flammability limit of the gas in an atmosphere at STP, mole fraction [-]
- UFL
float Upper flammability limit of the gas in an atmosphere at STP, mole fraction [-]
- TWA
tuple[quantity,unit] Time-Weighted Average limit on worker exposure to dangerous chemicals.
- STEL
tuple[quantity,unit] Short-term Exposure limit on worker exposure to dangerous chemicals.
- Ceiling
tuple[quantity,unit] Ceiling limits on worker exposure to dangerous chemicals.
- Skinbool
Whether or not a chemical can be absorbed through the skin.
- Carcinogen
strordict Carcinogen status information.
- dipole
float Dipole moment in debye, [3.33564095198e-30 ampere*second^2]
- Stockmayer
float Lennard-Jones depth of potential-energy minimum over k, [K]
- molecular_diameter
float Lennard-Jones molecular diameter, [angstrom]
- GWP
float Global warming potential (default 100-year outlook) (impact/mass chemical)/(impact/mass CO2), [-]
- ODP
float Ozone Depletion potential (impact/mass chemical)/(impact/mass CFC-11), [-]
- logP
float Octanol-water partition coefficient, [-]
legal_statusstrordictDictionary of legal status indicators for the chemical.
economic_statuslistDictionary of economic status indicators for the chemical.
- RI
float Refractive Index on the Na D line, [-]
- RIT
float Temperature at which refractive index reading was made
- conductivity
float Electrical conductivity of the fluid, [S/m]
- conductivityT
float Temperature at which conductivity measurement was made
- VaporPressure
object Instance of
thermo.vapor_pressure.VaporPressure, with data and methods loaded for the chemical; performs the actual calculations of vapor pressure of the chemical.- EnthalpyVaporization
object Instance of
thermo.phase_change.EnthalpyVaporization, with data and methods loaded for the chemical; performs the actual calculations of molar enthalpy of vaporization of the chemical.- VolumeSolid
object Instance of
thermo.volume.VolumeSolid, with data and methods loaded for the chemical; performs the actual calculations of molar volume of the solid phase of the chemical.- VolumeLiquid
object Instance of
thermo.volume.VolumeLiquid, with data and methods loaded for the chemical; performs the actual calculations of molar volume of the liquid phase of the chemical.- VolumeGas
object Instance of
thermo.volume.VolumeGas, with data and methods loaded for the chemical; performs the actual calculations of molar volume of the gas phase of the chemical.- HeatCapacitySolid
object Instance of
thermo.heat_capacity.HeatCapacitySolid, with data and methods loaded for the chemical; performs the actual calculations of molar heat capacity of the solid phase of the chemical.- HeatCapacityLiquid
object Instance of
thermo.heat_capacity.HeatCapacityLiquid, with data and methods loaded for the chemical; performs the actual calculations of molar heat capacity of the liquid phase of the chemical.- HeatCapacityGas
object Instance of
thermo.heat_capacity.HeatCapacityGas, with data and methods loaded for the chemical; performs the actual calculations of molar heat capacity of the gas phase of the chemical.- ViscosityLiquid
object Instance of
thermo.viscosity.ViscosityLiquid, with data and methods loaded for the chemical; performs the actual calculations of viscosity of the liquid phase of the chemical.- ViscosityGas
object Instance of
thermo.viscosity.ViscosityGas, with data and methods loaded for the chemical; performs the actual calculations of viscosity of the gas phase of the chemical.- ThermalConductivityLiquid
object Instance of
thermo.thermal_conductivity.ThermalConductivityLiquid, with data and methods loaded for the chemical; performs the actual calculations of thermal conductivity of the liquid phase of the chemical.- ThermalConductivityGas
object Instance of
thermo.thermal_conductivity.ThermalConductivityGas, with data and methods loaded for the chemical; performs the actual calculations of thermal conductivity of the gas phase of the chemical.- SurfaceTension
object Instance of
thermo.interface.SurfaceTension, with data and methods loaded for the chemical; performs the actual calculations of surface tension of the chemical.- Permittivity
object Instance of
thermo.permittivity.PermittivityLiquid, with data and methods loaded for the chemical; performs the actual calculations of permittivity of the chemical.- Psat_298
float Vapor pressure of the chemical at 298.15 K, [Pa]
- phase_STP
str Phase of the chemical at 298.15 K and 101325 Pa; one of ‘s’, ‘l’, ‘g’, or ‘l/g’.
- Vml_Tb
float Molar volume of liquid phase at the normal boiling point [m^3/mol]
- Vml_Tm
float Molar volume of liquid phase at the melting point [m^3/mol]
- Vml_STP
float Molar volume of liquid phase at 298.15 K and 101325 Pa [m^3/mol]
- rhoml_STP
float Molar density of liquid phase at 298.15 K and 101325 Pa [mol/m^3]
- Vmg_STP
float Molar volume of gas phase at 298.15 K and 101325 Pa according to the ideal gas law, [m^3/mol]
- Vms_Tm
float Molar volume of solid phase at the melting point [m^3/mol]
- rhos_Tm
float Mass density of solid phase at the melting point [kg/m^3]
- Hvap_Tbm
float Molar enthalpy of vaporization at the normal boiling point [J/mol]
- Hvap_Tb
float Mass enthalpy of vaporization at the normal boiling point [J/kg]
- Hvapm_298
float Molar enthalpy of vaporization at 298.15 K [J/mol]
- Hvap_298
float Mass enthalpy of vaporization at 298.15 K [J/kg]
alphaThermal diffusivity of the chemical at its current temperature, pressure, and phase in units of [m^2/s].
alphagThermal diffusivity of the gas phase of the chemical at its current temperature and pressure, in units of [m^2/s].
alphalThermal diffusivity of the liquid phase of the chemical at its current temperature and pressure, in units of [m^2/s].
APIAPI gravity of the liquid phase of the chemical, [degrees].
aromatic_ringsNumber of aromatic rings in a chemical, computed with RDKit from a chemical’s SMILES.
atom_fractionsDictionary of atom:fractional occurence of the elements in a chemical.
BvirialSecond virial coefficient of the gas phase of the chemical at its current temperature and pressure, in units of [mol/m^3].
chargeCharge of a chemical, computed with RDKit from a chemical’s SMILES.
CpMass heat capacity of the chemical at its current phase and temperature, in units of [J/kg/K].
CpgGas-phase heat capacity of the chemical at its current temperature, in units of [J/kg/K].
CpgmGas-phase ideal gas heat capacity of the chemical at its current temperature, in units of [J/mol/K].
CplLiquid-phase heat capacity of the chemical at its current temperature, in units of [J/kg/K].
CplmLiquid-phase heat capacity of the chemical at its current temperature, in units of [J/mol/K].
CpmMolar heat capacity of the chemical at its current phase and temperature, in units of [J/mol/K].
CpsSolid-phase heat capacity of the chemical at its current temperature, in units of [J/kg/K].
CpsmSolid-phase heat capacity of the chemical at its current temperature, in units of [J/mol/K].
CvgGas-phase ideal-gas contant-volume heat capacity of the chemical at its current temperature, in units of [J/kg/K].
CvgmGas-phase ideal-gas contant-volume heat capacity of the chemical at its current temperature, in units of [J/mol/K].
eosEquation of state object held by the chemical; used to calculate excess thermodynamic quantities, and also provides a vapor pressure curve, enthalpy of vaporization curve, fugacity, thermodynamic partial derivatives, and more; see
thermo.eosfor a full listing.HillHill formula of a compound.
HvapEnthalpy of vaporization of the chemical at its current temperature, in units of [J/kg].
HvapmEnthalpy of vaporization of the chemical at its current temperature, in units of [J/mol].
isentropic_exponentGas-phase ideal-gas isentropic exponent of the chemical at its current temperature, [dimensionless].
isobaric_expansionIsobaric (constant-pressure) expansion of the chemical at its current phase and temperature, in units of [1/K].
isobaric_expansion_gIsobaric (constant-pressure) expansion of the gas phase of the chemical at its current temperature and pressure, in units of [1/K].
isobaric_expansion_lIsobaric (constant-pressure) expansion of the liquid phase of the chemical at its current temperature and pressure, in units of [1/K].
JTJoule Thomson coefficient of the chemical at its current phase and temperature, in units of [K/Pa].
JTgJoule Thomson coefficient of the chemical in the gas phase at its current temperature and pressure, in units of [K/Pa].
JTlJoule Thomson coefficient of the chemical in the liquid phase at its current temperature and pressure, in units of [K/Pa].
kThermal conductivity of the chemical at its current phase, temperature, and pressure in units of [W/m/K].
kgThermal conductivity of the chemical in the gas phase at its current temperature and pressure, in units of [W/m/K].
klThermal conductivity of the chemical in the liquid phase at its current temperature and pressure, in units of [W/m/K].
mass_fractionsDictionary of atom:mass-weighted fractional occurence of elements.
muViscosity of the chemical at its current phase, temperature, and pressure in units of [Pa*s].
mugViscosity of the chemical in the gas phase at its current temperature and pressure, in units of [Pa*s].
mulViscosity of the chemical in the liquid phase at its current temperature and pressure, in units of [Pa*s].
nuKinematic viscosity of the the chemical at its current temperature, pressure, and phase in units of [m^2/s].
nugKinematic viscosity of the gas phase of the chemical at its current temperature and pressure, in units of [m^2/s].
nulKinematic viscosity of the liquid phase of the chemical at its current temperature and pressure, in units of [m^2/s].
ParachorParachor of the chemical at its current temperature and pressure, in units of [N^0.25*m^2.75/mol].
permittivityRelative permittivity (dielectric constant) of the chemical at its current temperature, [dimensionless].
PoyntingPoynting correction factor [dimensionless] for use in phase equilibria methods based on activity coefficients or other reference states.
PrPrandtl number of the chemical at its current temperature, pressure, and phase; [dimensionless].
PrgPrandtl number of the gas phase of the chemical at its current temperature and pressure, [dimensionless].
PrlPrandtl number of the liquid phase of the chemical at its current temperature and pressure, [dimensionless].
PsatVapor pressure of the chemical at its current temperature, in units of [Pa].
PSRK_groupsDictionary of PSRK subgroup: count groups for the PSRK subgroups, as determined by DDBST’s online service.
rdkitmolRDKit object of the chemical, without hydrogen.
rdkitmol_HsRDKit object of the chemical, with hydrogen.
rhoMass density of the chemical at its current phase and temperature and pressure, in units of [kg/m^3].
rhogGas-phase mass density of the chemical at its current temperature and pressure, in units of [kg/m^3].
rhogmMolar density of the chemical in the gas phase at the current temperature and pressure, in units of [mol/m^3].
rholLiquid-phase mass density of the chemical at its current temperature and pressure, in units of [kg/m^3].
rholmMolar density of the chemical in the liquid phase at the current temperature and pressure, in units of [mol/m^3].
rhomMolar density of the chemical at its current phase and temperature and pressure, in units of [mol/m^3].
rhosSolid-phase mass density of the chemical at its current temperature, in units of [kg/m^3].
rhosmMolar density of the chemical in the solid phase at the current temperature and pressure, in units of [mol/m^3].
ringsNumber of rings in a chemical, computed with RDKit from a chemical’s SMILES.
SGSpecific gravity of the chemical, [dimensionless].
SGgSpecific gravity of the gas phase of the chemical, [dimensionless].
SGlSpecific gravity of the liquid phase of the chemical at the specified temperature and pressure, [dimensionless].
SGsSpecific gravity of the solid phase of the chemical at the specified temperature and pressure, [dimensionless].
sigmaSurface tension of the chemical at its current temperature, in units of [N/m].
solubility_parameterSolubility parameter of the chemical at its current temperature and pressure, in units of [Pa^0.5].
UNIFAC_Dortmund_groupsDictionary of Dortmund UNIFAC subgroup: count groups for the Dortmund UNIFAC subgroups, as determined by DDBST’s online service.
UNIFAC_groupsDictionary of UNIFAC subgroup: count groups for the original UNIFAC subgroups, as determined by DDBST’s online service.
UNIFAC_RUNIFAC R (normalized Van der Waals volume), dimensionless.
UNIFAC_QUNIFAC Q (normalized Van der Waals area), dimensionless.
Van_der_Waals_areaUnnormalized Van der Waals area, in units of [m^2/mol].
Van_der_Waals_volumeUnnormalized Van der Waals volume, in units of [m^3/mol].
VmMolar volume of the chemical at its current phase and temperature and pressure, in units of [m^3/mol].
VmgGas-phase molar volume of the chemical at its current temperature and pressure, in units of [m^3/mol].
VmlLiquid-phase molar volume of the chemical at its current temperature and pressure, in units of [m^3/mol].
VmsSolid-phase molar volume of the chemical at its current temperature, in units of [m^3/mol].
ZCompressibility factor of the chemical at its current phase and temperature and pressure, [dimensionless].
ZgCompressibility factor of the chemical in the gas phase at the current temperature and pressure, [dimensionless].
ZlCompressibility factor of the chemical in the liquid phase at the current temperature and pressure, [dimensionless].
ZsCompressibility factor of the chemical in the solid phase at the current temperature and pressure, [dimensionless].
- T
Methods
Reynolds([V, D])draw_2d([width, height, Hs])Interface for drawing a 2D image of the molecule.
draw_3d([width, height, style, Hs, atom_labels])Interface for drawing an interactive 3D view of the molecule.
Bond
Capillary
Grashof
Jakob
Peclet_heat
Tsat
Weber
calc_H
calc_H_excess
calc_S
calc_S_excess
calculate
calculate_PH
calculate_PS
calculate_TH
calculate_TS
set_TP_sources
set_constant_sources
set_constants
set_eos
set_ref
set_thermo
Notes
Warning
The Chemical class is not designed for high-performance or the ability to use different thermodynamic models. It is especially limited in its multiphase support and the ability to solve with specifications other than temperature and pressure. It is impossible to change constant properties such as a compound’s critical temperature in this interface.
It is recommended to switch over to the
thermo.flashinterface which solves those problems and is better positioned to grow. That interface also requires users to be responsible for their chemical constants and pure component correlations; while default values can easily be loaded for most compounds, the user is ultimately responsible for them.Examples
Creating chemical objects:
>>> Chemical('hexane') <Chemical [hexane], T=298.15 K, P=101325 Pa>
>>> Chemical('CCCCCCCC', T=500, P=1E7) <Chemical [octane], T=500.00 K, P=10000000 Pa>
>>> Chemical('7440-36-0', P=1000) <Chemical [antimony], T=298.15 K, P=1000 Pa>
Getting basic properties:
>>> N2 = Chemical('Nitrogen') >>> N2.Tm, N2.Tb, N2.Tc # melting, boiling, and critical points [K] (63.15, 77.355, 126.2) >>> N2.Pt, N2.Pc # sublimation and critical pressure [Pa] (12526.9697368421, 3394387.5) >>> N2.CAS, N2.formula, N2.InChI, N2.smiles, N2.atoms # CAS number, formula, InChI string, smiles string, dictionary of atomic elements and their count ('7727-37-9', 'N2', 'N2/c1-2', 'N#N', {'N': 2})
Changing the T/P of the chemical, and gettign temperature-dependent properties:
>>> N2.Cp, N2.rho, N2.mu # Heat capacity [J/kg/K], density [kg/m^3], viscosity [Pa*s] (1039., 1.14, 1.78e-05) >>> N2.calculate(T=65, P=1E6) # set it to a liquid at 65 K and 1 MPa >>> N2.phase 'l' >>> N2.Cp, N2.rho, N2.mu # properties are now of the liquid phase (2002., 861., 0.000285)
Molar units are also available for properties:
>>> N2.Cpm, N2.Vm, N2.Hvapm # heat capacity [J/mol/K], molar volume [m^3/mol], enthalpy of vaporization [J/mol] (56., 3.25e-05, 5982.)
A great deal of properties are available; for a complete list look at the attributes list.
>>> N2.alpha, N2.JT # thermal diffusivity [m^2/s], Joule-Thompson coefficient [K/Pa] (9.87e-08, -4.0e-07)
>>> N2.isentropic_exponent, N2.isobaric_expansion (1.4, 0.0047)
For pure species, the phase is easily identified, allowing for properties to be obtained without needing to specify the phase. However, the properties are also available in the hypothetical gas phase (when under the boiling point) and in the hypothetical liquid phase (when above the boiling point) as these properties are needed to evaluate mixture properties. Specify the phase of a property to be retrieved by appending ‘l’ or ‘g’ or ‘s’ to the property.
>>> C50 = Chemical('pentacontane')
>>> C50.rhog, C50.Cpg, C50.kg, C50.mug (4.241646701894199, 1126.5533755283168, 0.00941385692301755, 6.973325939594919e-06)
Temperature dependent properties are calculated by objects which provide many useful features related to the properties. To determine the temperature at which nitrogen has a saturation pressure of 1 MPa:
>>> N2.VaporPressure.solve_property(1E6) 103.73528598652341
To compute an integral of the ideal-gas heat capacity of nitrogen to determine the enthalpy required for a given change in temperature. Note the thermodynamic objects calculate values in molar units always.
>>> N2.HeatCapacityGas.T_dependent_property_integral(100, 120) # J/mol/K 582.0121860897898
Derivatives of properties can be calculated as well, as may be needed by for example heat transfer calculations:
>>> N2.SurfaceTension.T_dependent_property_derivative(77) -0.00022695346296730534
If a property is needed at multiple temperatures or pressures, it is faster to use the object directly to perform the calculation rather than setting the conditions for the chemical.
>>> [N2.VaporPressure(T) for T in range(80, 120, 10)] [136979.4840843189, 360712.5746603142, 778846.276691705, 1466996.7208525643]
These objects are also how the methods by which the properties are calculated can be changed. To see the available methods for a property:
>>> N2.VaporPressure.all_methods set(['VDI_PPDS', 'BOILING_CRITICAL', 'WAGNER_MCGARRY', 'AMBROSE_WALTON', 'COOLPROP', 'LEE_KESLER_PSAT', 'EOS', 'ANTOINE_POLING', 'SANJARI', 'DIPPR_PERRY_8E', 'Edalat', 'WAGNER_POLING'])
To specify the method which should be used for calculations of a property. In the example below, the Lee-kesler correlation for vapor pressure is specified.
>>> N2.calculate(80) >>> N2.Psat 136979.4840843189 >>> N2.VaporPressure.method = 'LEE_KESLER_PSAT' >>> N2.Psat 134987.76815364443
Properties may also be plotted via these objects:
>>> N2.VaporPressure.plot_T_dependent_property() >>> N2.VolumeLiquid.plot_isotherm(T=77, Pmin=1E5, Pmax=1E7) >>> N2.VolumeLiquid.plot_isobar(P=1E6, Tmin=66, Tmax=120) >>> N2.VolumeLiquid.plot_TP_dependent_property(Tmin=60, Tmax=100, Pmin=1E5, Pmax=1E7)
- property A¶
Helmholtz energy of the chemical at its current temperature and pressure, in units of [J/kg].
This property requires that
thermo.chemical.set_thermoran successfully to be accurate. It also depends on the molar volume of the chemical at its current conditions.
- property API¶
API gravity of the liquid phase of the chemical, [degrees]. The reference condition is water at 15.6 °C (60 °F) and 1 atm (rho=999.016 kg/m^3, standardized).
Examples
>>> Chemical('water').API 10.
- property Am¶
Helmholtz energy of the chemical at its current temperature and pressure, in units of [J/mol].
This property requires that
thermo.chemical.set_thermoran successfully to be accurate. It also depends on the molar volume of the chemical at its current conditions.
- property Bvirial¶
Second virial coefficient of the gas phase of the chemical at its current temperature and pressure, in units of [mol/m^3].
This property uses the object-oriented interface
thermo.volume.VolumeGas, converting its result withthermo.utils.B_from_Z.Examples
>>> Chemical('water', T=500, P=1e5).Bvirial -0.00017
- property Cp¶
Mass heat capacity of the chemical at its current phase and temperature, in units of [J/kg/K].
Utilizes the object oriented interfaces
thermo.heat_capacity.HeatCapacitySolid,thermo.heat_capacity.HeatCapacityLiquid, andthermo.heat_capacity.HeatCapacityGasto perform the actual calculation of each property. Note that those interfaces provide output in molar units (J/mol/K).Examples
>>> w = Chemical('water') >>> w.Cp, w.phase (4180., 'l') >>> Chemical('palladium').Cp 234.
- property Cpg¶
Gas-phase heat capacity of the chemical at its current temperature, in units of [J/kg/K]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.heat_capacity.HeatCapacityGas; each Chemical instance creates one to actually perform the calculations. Note that that interface provides output in molar units.Examples
>>> w = Chemical('water', T=520) >>> w.Cpg 1967.
- property Cpgm¶
Gas-phase ideal gas heat capacity of the chemical at its current temperature, in units of [J/mol/K]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.heat_capacity.HeatCapacityGas; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water').Cpgm 33.58 >>> Chemical('water').HeatCapacityGas.T_dependent_property(320) 33.67 >>> Chemical('water').HeatCapacityGas.T_dependent_property_integral(300, 320) 672.
- property Cpl¶
Liquid-phase heat capacity of the chemical at its current temperature, in units of [J/kg/K]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.heat_capacity.HeatCapacityLiquid; each Chemical instance creates one to actually perform the calculations. Note that that interface provides output in molar units.Examples
>>> Chemical('water', T=320).Cpl 4177.
Ideal entropy change of water from 280 K to 340 K, output converted back to mass-based units of J/kg/K.
>>> dSm = Chemical('water').HeatCapacityLiquid.T_dependent_property_integral_over_T(280, 340) >>> property_molar_to_mass(dSm, Chemical('water').MW) 812.
- property Cplm¶
Liquid-phase heat capacity of the chemical at its current temperature, in units of [J/mol/K]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.heat_capacity.HeatCapacityLiquid; each Chemical instance creates one to actually perform the calculations.Notes
Some methods give heat capacity along the saturation line, some at 1 atm but only up to the normal boiling point, and some give heat capacity at 1 atm up to the normal boiling point and then along the saturation line. Real-liquid heat capacity is pressure dependent, but this interface is not.
Examples
>>> Chemical('water').Cplm 75.3 >>> Chemical('water').HeatCapacityLiquid.T_dependent_property(320) 75.2 >>> Chemical('water').HeatCapacityLiquid.T_dependent_property_integral(300, 320) 1505.
- property Cpm¶
Molar heat capacity of the chemical at its current phase and temperature, in units of [J/mol/K].
Utilizes the object oriented interfaces
thermo.heat_capacity.HeatCapacitySolid,thermo.heat_capacity.HeatCapacityLiquid, andthermo.heat_capacity.HeatCapacityGasto perform the actual calculation of each property.Examples
>>> Chemical('cubane').Cpm 137. >>> Chemical('ethylbenzene', T=550, P=3E6).Cpm 294.
- property Cps¶
Solid-phase heat capacity of the chemical at its current temperature, in units of [J/kg/K]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.heat_capacity.HeatCapacitySolid; each Chemical instance creates one to actually perform the calculations. Note that that interface provides output in molar units.Examples
>>> Chemical('palladium', T=400).Cps 241. >>> Pd = Chemical('palladium', T=400) >>> Cpsms = [Pd.HeatCapacitySolid.T_dependent_property(T) for T in np.linspace(300, 500, 2)] >>> [property_molar_to_mass(Cps, Pd.MW) for Cps in Cpsms] [234., 248.]
- property Cpsm¶
Solid-phase heat capacity of the chemical at its current temperature, in units of [J/mol/K]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.heat_capacity.HeatCapacitySolid; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('palladium').Cpsm 24.9 >>> Chemical('palladium').HeatCapacitySolid.T_dependent_property(320) 25. >>> sorted(Chemical('palladium').HeatCapacitySolid.all_methods) ['CRCSTD', 'LASTOVKA_S', 'PERRY151']
- property Cvg¶
Gas-phase ideal-gas contant-volume heat capacity of the chemical at its current temperature, in units of [J/kg/K]. Subtracts R from the ideal-gas heat capacity; does not include pressure-compensation from an equation of state.
Examples
>>> w = Chemical('water', T=520) >>> w.Cvg 1506.
- property Cvgm¶
Gas-phase ideal-gas contant-volume heat capacity of the chemical at its current temperature, in units of [J/mol/K]. Subtracts R from the ideal-gas heat capacity; does not include pressure-compensation from an equation of state.
Examples
>>> w = Chemical('water', T=520) >>> w.Cvgm 27.1
- property Hill¶
Hill formula of a compound. For a description of the Hill system, see
chemicals.elements.atoms_to_Hill.Examples
>>> Chemical('furfuryl alcohol').Hill 'C5H6O2'
- property Hvap¶
Enthalpy of vaporization of the chemical at its current temperature, in units of [J/kg].
This property uses the object-oriented interface
thermo.phase_change.EnthalpyVaporization, but converts its results from molar to mass units.Examples
>>> Chemical('water', T=320).Hvap 2389540.
- property Hvapm¶
Enthalpy of vaporization of the chemical at its current temperature, in units of [J/mol]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.phase_change.EnthalpyVaporization; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water', T=320).Hvapm 43048. >>> Chemical('water').EnthalpyVaporization.T_dependent_property(320) 43048. >>> sorted(Chemical('water').EnthalpyVaporization.all_methods) ['ALIBAKHSHI', 'CHEN', 'CLAPEYRON', 'COOLPROP', 'CRC_HVAP_298', 'CRC_HVAP_TB', 'DIPPR_PERRY_8E', 'LIU', 'MORGAN_KOBAYASHI', 'PITZER', 'RIEDEL', 'SIVARAMAN_MAGEE_KOBAYASHI', 'VDI_PPDS', 'VELASCO', 'VETERE']
- property JT¶
Joule Thomson coefficient of the chemical at its current phase and temperature, in units of [K/Pa].
Examples
>>> Chemical('water').JT -2.21e-07
- property JTg¶
Joule Thomson coefficient of the chemical in the gas phase at its current temperature and pressure, in units of [K/Pa].
Utilizes the temperature-derivative method of
thermo.volume.VolumeGasand the temperature-dependent heat capacity methodthermo.heat_capacity.HeatCapacityGasto obtain the properties required for the actual calculation.Examples
>>> Chemical('dodecane', T=400, P=1000).JTg 5.4e-05
- property JTl¶
Joule Thomson coefficient of the chemical in the liquid phase at its current temperature and pressure, in units of [K/Pa].
Utilizes the temperature-derivative method of
thermo.volume.VolumeLiquidand the temperature-dependent heat capacity methodthermo.heat_capacity.HeatCapacityLiquidto obtain the properties required for the actual calculation.Examples
>>> Chemical('dodecane', T=400).JTl -3.1e-07
- property PSRK_groups¶
Dictionary of PSRK subgroup: count groups for the PSRK subgroups, as determined by DDBST’s online service.
Examples
>>> Chemical('Cumene').PSRK_groups {1: 2, 9: 5, 13: 1}
- property Parachor¶
Parachor of the chemical at its current temperature and pressure, in units of [N^0.25*m^2.75/mol].
Calculated based on surface tension, density of the liquid phase, and molecular weight. For uses of this property, see
thermo.utils.Parachor.The gas density is calculated using the ideal-gas law.
Examples
>>> Chemical('octane').Parachor 6.2e-05
- property Poynting¶
Poynting correction factor [dimensionless] for use in phase equilibria methods based on activity coefficients or other reference states. Performs the shortcut calculation assuming molar volume is independent of pressure.
The full calculation normally returns values very close to the approximate ones. This property is defined in terms of pure components only.
Notes
The full equation shown below can be used as follows:
>>> from scipy.integrate import quad >>> c = Chemical('pentane', T=300, P=2e6) >>> exp(quad(lambda P : c.VolumeLiquid(c.T, P), c.Psat, c.P)[0]/R/c.T) 1.093
Examples
>>> Chemical('pentane', T=300, P=2e6).Poynting 1.09
- property Pr¶
Prandtl number of the chemical at its current temperature, pressure, and phase; [dimensionless].
Examples
>>> Chemical('acetone').Pr 4.1
- property Prg¶
Prandtl number of the gas phase of the chemical at its current temperature and pressure, [dimensionless].
Utilizes the temperature and pressure dependent object oriented interfaces
thermo.viscosity.ViscosityGas,thermo.thermal_conductivity.ThermalConductivityGas, andthermo.heat_capacity.HeatCapacityGasto calculate the actual properties.Examples
>>> Chemical('NH3').Prg 0.84
- property Prl¶
Prandtl number of the liquid phase of the chemical at its current temperature and pressure, [dimensionless].
Utilizes the temperature and pressure dependent object oriented interfaces
thermo.viscosity.ViscosityLiquid,thermo.thermal_conductivity.ThermalConductivityLiquid, andthermo.heat_capacity.HeatCapacityLiquidto calculate the actual properties.Examples
>>> Chemical('nitrogen', T=70).Prl 2.78
- property Psat¶
Vapor pressure of the chemical at its current temperature, in units of [Pa]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.vapor_pressure.VaporPressure; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water', T=320).Psat 10545. >>> Chemical('water').VaporPressure.T_dependent_property(320) 10545. >>> sorted(Chemical('water').VaporPressure.all_methods) ['AMBROSE_WALTON', 'ANTOINE_POLING', 'ANTOINE_WEBBOOK', 'BOILING_CRITICAL', 'COOLPROP', 'DIPPR_PERRY_8E', 'EDALAT', 'EOS', 'IAPWS', 'LEE_KESLER_PSAT', 'SANJARI', 'VDI_PPDS', 'WAGNER_MCGARRY']
- property R_specific¶
Specific gas constant, in units of [J/kg/K].
Examples
>>> Chemical('water').R_specific 461.5
- property SG¶
Specific gravity of the chemical, [dimensionless].
For gas-phase conditions, this is calculated at 15.6 °C (60 °F) and 1 atm for the chemical and the reference fluid, air. For liquid and solid phase conditions, this is calculated based on a reference fluid of water at 4°C at 1 atm, but the with the liquid or solid chemical’s density at the currently specified conditions.
Examples
>>> Chemical('MTBE').SG 0.73
- property SGg¶
Specific gravity of the gas phase of the chemical, [dimensionless]. The reference condition is air at 15.6 °C (60 °F) and 1 atm (rho=1.223 kg/m^3). The definition for gases uses the compressibility factor of the reference gas and the chemical both at the reference conditions, not the conditions of the chemical.
Examples
>>> Chemical('argon').SGg 1.3
- property SGl¶
Specific gravity of the liquid phase of the chemical at the specified temperature and pressure, [dimensionless]. The reference condition is water at 4 °C and 1 atm (rho=999.017 kg/m^3). For liquids, SG is defined that the reference chemical’s T and P are fixed, but the chemical itself varies with the specified T and P.
Examples
>>> Chemical('water', T=365).SGl 0.965
- property SGs¶
Specific gravity of the solid phase of the chemical at the specified temperature and pressure, [dimensionless]. The reference condition is water at 4 °C and 1 atm (rho=999.017 kg/m^3). The SG varries with temperature and pressure but only very slightly.
Examples
>>> Chemical('iron').SGs 7.8
- property U¶
Internal energy of the chemical at its current temperature and pressure, in units of [J/kg].
This property requires that
thermo.chemical.set_thermoran successfully to be accurate. It also depends on the molar volume of the chemical at its current conditions.
- property UNIFAC_Dortmund_groups¶
Dictionary of Dortmund UNIFAC subgroup: count groups for the Dortmund UNIFAC subgroups, as determined by DDBST’s online service.
Examples
>>> Chemical('Cumene').UNIFAC_Dortmund_groups {1: 2, 9: 5, 13: 1}
- property UNIFAC_Q¶
UNIFAC Q (normalized Van der Waals area), dimensionless. Used in the UNIFAC model.
Examples
>>> Chemical('decane').UNIFAC_Q 6.016
- property UNIFAC_R¶
UNIFAC R (normalized Van der Waals volume), dimensionless. Used in the UNIFAC model.
Examples
>>> Chemical('benzene').UNIFAC_R 3.1878
- property UNIFAC_groups¶
Dictionary of UNIFAC subgroup: count groups for the original UNIFAC subgroups, as determined by DDBST’s online service.
Examples
>>> Chemical('Cumene').UNIFAC_groups {1: 2, 9: 5, 13: 1}
- property Um¶
Internal energy of the chemical at its current temperature and pressure, in units of [J/mol].
This property requires that
thermo.chemical.set_thermoran successfully to be accurate. It also depends on the molar volume of the chemical at its current conditions.
- property Van_der_Waals_area¶
Unnormalized Van der Waals area, in units of [m^2/mol].
Examples
>>> Chemical('hexane').Van_der_Waals_area 964000.0
- property Van_der_Waals_volume¶
Unnormalized Van der Waals volume, in units of [m^3/mol].
Examples
>>> Chemical('hexane').Van_der_Waals_volume 6.8261966e-05
- property Vm¶
Molar volume of the chemical at its current phase and temperature and pressure, in units of [m^3/mol].
Utilizes the object oriented interfaces
thermo.volume.VolumeSolid,thermo.volume.VolumeLiquid, andthermo.volume.VolumeGasto perform the actual calculation of each property.Examples
>>> Chemical('ethylbenzene', T=550, P=3E6).Vm 0.00017
- property Vmg¶
Gas-phase molar volume of the chemical at its current temperature and pressure, in units of [m^3/mol]. For calculation of this property at other temperatures or pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.volume.VolumeGas; each Chemical instance creates one to actually perform the calculations.Examples
Estimate the molar volume of the core of the sun, at 15 million K and 26.5 PetaPascals, assuming pure helium (actually 68% helium):
>>> Chemical('helium', T=15E6, P=26.5E15).Vmg 4.7e-07
- property Vmg_ideal¶
Gas-phase molar volume of the chemical at its current temperature and pressure calculated with the ideal-gas law, in units of [m^3/mol].
Examples
>>> Chemical('helium', T=300.0, P=1e5).Vmg_ideal 0.0249433878544
- property Vml¶
Liquid-phase molar volume of the chemical at its current temperature and pressure, in units of [m^3/mol]. For calculation of this property at other temperatures or pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.volume.VolumeLiquid; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('cyclobutane', T=225).Vml 7.42395423425395e-05
- property Vms¶
Solid-phase molar volume of the chemical at its current temperature, in units of [m^3/mol]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.volume.VolumeSolid; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('iron').Vms 7.09e-06
- property Z¶
Compressibility factor of the chemical at its current phase and temperature and pressure, [dimensionless].
Examples
>>> Chemical('MTBE', T=900, P=1E-2).Z 1.
- property Zg¶
Compressibility factor of the chemical in the gas phase at the current temperature and pressure, [dimensionless].
Utilizes the object oriented interface and
thermo.volume.VolumeGasto perform the actual calculation of molar volume.Examples
>>> Chemical('sulfur hexafluoride', T=700, P=1E9).Zg 11.14
- property Zl¶
Compressibility factor of the chemical in the liquid phase at the current temperature and pressure, [dimensionless].
Utilizes the object oriented interface and
thermo.volume.VolumeLiquidto perform the actual calculation of molar volume.Examples
>>> Chemical('water').Zl 0.00073
- property Zs¶
Compressibility factor of the chemical in the solid phase at the current temperature and pressure, [dimensionless].
Utilizes the object oriented interface and
thermo.volume.VolumeSolidto perform the actual calculation of molar volume.Examples
>>> Chemical('palladium').Z 0.000362
- property absolute_permittivity¶
Absolute permittivity of the chemical at its current temperature, in units of [farad/meter]. Those units are equivalent to ampere^2*second^4/kg/m^3.
Examples
>>> Chemical('water', T=293.15).absolute_permittivity 7.1e-10
- property alpha¶
Thermal diffusivity of the chemical at its current temperature, pressure, and phase in units of [m^2/s].
Examples
>>> Chemical('furfural').alpha 8.7e-08
- property alphag¶
Thermal diffusivity of the gas phase of the chemical at its current temperature and pressure, in units of [m^2/s].
Utilizes the temperature and pressure dependent object oriented interfaces
thermo.volume.VolumeGas,thermo.thermal_conductivity.ThermalConductivityGas, andthermo.heat_capacity.HeatCapacityGasto calculate the actual properties.Examples
>>> Chemical('ammonia').alphag 1.69e-05
- property alphal¶
Thermal diffusivity of the liquid phase of the chemical at its current temperature and pressure, in units of [m^2/s].
Utilizes the temperature and pressure dependent object oriented interfaces
thermo.volume.VolumeLiquid,thermo.thermal_conductivity.ThermalConductivityLiquid, andthermo.heat_capacity.HeatCapacityLiquidto calculate the actual properties.Examples
>>> Chemical('nitrogen', T=70).alphal 9.4e-08
- property aromatic_rings¶
Number of aromatic rings in a chemical, computed with RDKit from a chemical’s SMILES. If RDKit is not available, holds None.
Examples
>>> Chemical('Paclitaxel').aromatic_rings 3
- property atom_fractions¶
Dictionary of atom:fractional occurence of the elements in a chemical. Useful when performing element balances. For mass-fraction occurences, see
mass_fractions.Examples
>>> Chemical('Ammonium aluminium sulfate').atom_fractions {'Al': 0.0625, 'H': 0.25, 'N': 0.0625, 'O': 0.5, 'S': 0.125}
- property charge¶
Charge of a chemical, computed with RDKit from a chemical’s SMILES. If RDKit is not available, holds None.
Examples
>>> Chemical('sodium ion').charge 1
- draw_2d(width=300, height=300, Hs=False)[source]¶
Interface for drawing a 2D image of the molecule. Requires an HTML5 browser, and the libraries RDKit and IPython. An exception is raised if either of these libraries is absent.
- Parameters:
Examples
>>> Chemical('decane').draw_2d() <PIL.PngImagePlugin.PngImageFile image mode=RGB size=300x300 at 0x...>
- draw_3d(width=300, height=500, style='stick', Hs=True, atom_labels=True)[source]¶
Interface for drawing an interactive 3D view of the molecule. Requires an HTML5 browser, and the libraries RDKit, pymol3D, and IPython. An exception is raised if all three of these libraries are not installed.
- Parameters:
Examples
>>> Chemical('cubane').draw_3d() None
- property economic_status¶
Dictionary of economic status indicators for the chemical.
Examples
>>> Chemical('benzene').economic_status ["US public: {'Manufactured': 6165232.1, 'Imported': 463146.474, 'Exported': 271908.252}", '1,000,000 - 10,000,000 tonnes per annum', 'Intermediate Use Only', 'OECD HPV Chemicals']
- property eos¶
Equation of state object held by the chemical; used to calculate excess thermodynamic quantities, and also provides a vapor pressure curve, enthalpy of vaporization curve, fugacity, thermodynamic partial derivatives, and more; see
thermo.eosfor a full listing.Examples
>>> Chemical('methane').eos.V_g 0.0244
- property is_acid¶
Method to return whether or not this chemical is in the category acid, [-]
- property is_acyl_halide¶
Method to return whether or not this chemical is in the category acyl_halide, [-]
- property is_alcohol¶
Method to return whether or not this chemical is in the category alcohol, [-]
- property is_aldehyde¶
Method to return whether or not this chemical is in the category aldehyde, [-]
- property is_alkane¶
Method to return whether or not this chemical is in the category alkane, [-]
- property is_alkene¶
Method to return whether or not this chemical is in the category alkene, [-]
- property is_alkylaluminium¶
Method to return whether or not this chemical is in the category alkylaluminium, [-]
- property is_alkyllithium¶
Method to return whether or not this chemical is in the category alkyllithium, [-]
- property is_alkylmagnesium_halide¶
Method to return whether or not this chemical is in the category alkylmagnesium_halide, [-]
- property is_alkyne¶
Method to return whether or not this chemical is in the category alkyne, [-]
- property is_amide¶
Method to return whether or not this chemical is in the category amide, [-]
- property is_amidine¶
Method to return whether or not this chemical is in the category amidine, [-]
- property is_amine¶
Method to return whether or not this chemical is in the category amine, [-]
- property is_anhydride¶
Method to return whether or not this chemical is in the category anhydride, [-]
- property is_aromatic¶
Method to return whether or not this chemical is in the category aromatic, [-]
- property is_azide¶
Method to return whether or not this chemical is in the category azide, [-]
- property is_azo¶
Method to return whether or not this chemical is in the category azo, [-]
- property is_borinic_acid¶
Method to return whether or not this chemical is in the category borinic_acid, [-]
- property is_borinic_ester¶
Method to return whether or not this chemical is in the category borinic_ester, [-]
- property is_boronic_acid¶
Method to return whether or not this chemical is in the category boronic_acid, [-]
- property is_boronic_ester¶
Method to return whether or not this chemical is in the category boronic_ester, [-]
- property is_branched_alkane¶
Method to return whether or not this chemical is in the category branched_alkane, [-]
- property is_bromoalkane¶
Method to return whether or not this chemical is in the category bromoalkane, [-]
- property is_carbamate¶
Method to return whether or not this chemical is in the category carbamate, [-]
- property is_carbodithio¶
Method to return whether or not this chemical is in the category carbodithio, [-]
- property is_carbodithioic_acid¶
Method to return whether or not this chemical is in the category carbodithioic_acid, [-]
- property is_carbonate¶
Method to return whether or not this chemical is in the category carbonate, [-]
- property is_carbothioic_o_acid¶
Method to return whether or not this chemical is in the category carbothioic_o_acid, [-]
- property is_carbothioic_s_acid¶
Method to return whether or not this chemical is in the category carbothioic_s_acid, [-]
- property is_carboxylate¶
Method to return whether or not this chemical is in the category carboxylate, [-]
- property is_carboxylic_acid¶
Method to return whether or not this chemical is in the category carboxylic_acid, [-]
- property is_carboxylic_anhydride¶
Method to return whether or not this chemical is in the category carboxylic_anhydride, [-]
- property is_chloroalkane¶
Method to return whether or not this chemical is in the category chloroalkane, [-]
- property is_cyanate¶
Method to return whether or not this chemical is in the category cyanate, [-]
- property is_cyanide¶
Method to return whether or not this chemical is in the category cyanide, [-]
- property is_cycloalkane¶
Method to return whether or not this chemical is in the category cycloalkane, [-]
- property is_disulfide¶
Method to return whether or not this chemical is in the category disulfide, [-]
- property is_ester¶
Method to return whether or not this chemical is in the category ester, [-]
- property is_ether¶
Method to return whether or not this chemical is in the category ether, [-]
- property is_fluoroalkane¶
Method to return whether or not this chemical is in the category fluoroalkane, [-]
- property is_haloalkane¶
Method to return whether or not this chemical is in the category haloalkane, [-]
- property is_hydroperoxide¶
Method to return whether or not this chemical is in the category hydroperoxide, [-]
- property is_imide¶
Method to return whether or not this chemical is in the category imide, [-]
- property is_imine¶
Method to return whether or not this chemical is in the category imine, [-]
- property is_inorganic¶
Method to return whether or not this chemical is in the category inorganic, [-]
- property is_iodoalkane¶
Method to return whether or not this chemical is in the category iodoalkane, [-]
- property is_is_hydrocarbon¶
Method to return whether or not this chemical is in the category is_hydrocarbon, [-]
- property is_isocyanate¶
Method to return whether or not this chemical is in the category isocyanate, [-]
- property is_isonitrile¶
Method to return whether or not this chemical is in the category isonitrile, [-]
- property is_isothiocyanate¶
Method to return whether or not this chemical is in the category isothiocyanate, [-]
- property is_ketone¶
Method to return whether or not this chemical is in the category ketone, [-]
- property is_mercaptan¶
Method to return whether or not this chemical is in the category mercaptan, [-]
- property is_methylenedioxy¶
Method to return whether or not this chemical is in the category methylenedioxy, [-]
- property is_nitrate¶
Method to return whether or not this chemical is in the category nitrate, [-]
- property is_nitrile¶
Method to return whether or not this chemical is in the category nitrile, [-]
- property is_nitrite¶
Method to return whether or not this chemical is in the category nitrite, [-]
- property is_nitro¶
Method to return whether or not this chemical is in the category nitro, [-]
- property is_nitroso¶
Method to return whether or not this chemical is in the category nitroso, [-]
- property is_organic¶
Method to return whether or not this chemical is in the category organic, [-]
- property is_orthocarbonate_ester¶
Method to return whether or not this chemical is in the category orthocarbonate_ester, [-]
- property is_orthoester¶
Method to return whether or not this chemical is in the category orthoester, [-]
- property is_oxime¶
Method to return whether or not this chemical is in the category oxime, [-]
- property is_peroxide¶
Method to return whether or not this chemical is in the category peroxide, [-]
- property is_phenol¶
Method to return whether or not this chemical is in the category phenol, [-]
- property is_phosphate¶
Method to return whether or not this chemical is in the category phosphate, [-]
- property is_phosphine¶
Method to return whether or not this chemical is in the category phosphine, [-]
- property is_phosphodiester¶
Method to return whether or not this chemical is in the category phosphodiester, [-]
- property is_phosphonic_acid¶
Method to return whether or not this chemical is in the category phosphonic_acid, [-]
- property is_polyol¶
Method to return whether or not this chemical is in the category polyol, [-]
- property is_primary_aldimine¶
Method to return whether or not this chemical is in the category primary_aldimine, [-]
- property is_primary_amine¶
Method to return whether or not this chemical is in the category primary_amine, [-]
- property is_primary_ketimine¶
Method to return whether or not this chemical is in the category primary_ketimine, [-]
- property is_pyridyl¶
Method to return whether or not this chemical is in the category pyridyl, [-]
- property is_quat¶
Method to return whether or not this chemical is in the category quat, [-]
- property is_secondary_aldimine¶
Method to return whether or not this chemical is in the category secondary_aldimine, [-]
- property is_secondary_amine¶
Method to return whether or not this chemical is in the category secondary_amine, [-]
- property is_secondary_ketimine¶
Method to return whether or not this chemical is in the category secondary_ketimine, [-]
- property is_siloxane¶
Method to return whether or not this chemical is in the category siloxane, [-]
- property is_silyl_ether¶
Method to return whether or not this chemical is in the category silyl_ether, [-]
- property is_sulfide¶
Method to return whether or not this chemical is in the category sulfide, [-]
- property is_sulfinic_acid¶
Method to return whether or not this chemical is in the category sulfinic_acid, [-]
- property is_sulfonate_ester¶
Method to return whether or not this chemical is in the category sulfonate_ester, [-]
- property is_sulfone¶
Method to return whether or not this chemical is in the category sulfone, [-]
- property is_sulfonic_acid¶
Method to return whether or not this chemical is in the category sulfonic_acid, [-]
- property is_sulfoxide¶
Method to return whether or not this chemical is in the category sulfoxide, [-]
- property is_tertiary_amine¶
Method to return whether or not this chemical is in the category tertiary_amine, [-]
- property is_thial¶
Method to return whether or not this chemical is in the category thial, [-]
- property is_thiocyanate¶
Method to return whether or not this chemical is in the category thiocyanate, [-]
- property is_thioketone¶
Method to return whether or not this chemical is in the category thioketone, [-]
- property is_thiolester¶
Method to return whether or not this chemical is in the category thiolester, [-]
- property is_thionoester¶
Method to return whether or not this chemical is in the category thionoester, [-]
- property isentropic_exponent¶
Gas-phase ideal-gas isentropic exponent of the chemical at its current temperature, [dimensionless]. Does not include pressure-compensation from an equation of state.
Examples
>>> Chemical('hydrogen').isentropic_exponent 1.40
- property isobaric_expansion¶
Isobaric (constant-pressure) expansion of the chemical at its current phase and temperature, in units of [1/K].
Examples
Radical change in value just above and below the critical temperature of water:
>>> Chemical('water', T=647.1, P=22048320.0).isobaric_expansion 0.77
>>> Chemical('water', T=647.2, P=22048320.0).isobaric_expansion 0.39
- property isobaric_expansion_g¶
Isobaric (constant-pressure) expansion of the gas phase of the chemical at its current temperature and pressure, in units of [1/K].
Utilizes the temperature-derivative method of
thermo.VolumeGasto perform the actual calculation. The derivatives are all numerical.Examples
>>> Chemical('Hexachlorobenzene', T=900).isobaric_expansion_g 0.00115
- property isobaric_expansion_l¶
Isobaric (constant-pressure) expansion of the liquid phase of the chemical at its current temperature and pressure, in units of [1/K].
Utilizes the temperature-derivative method of
thermo.volume.VolumeLiquidto perform the actual calculation. The derivatives are all numerical.Examples
>>> Chemical('dodecane', T=400).isobaric_expansion_l 0.00116
- property k¶
Thermal conductivity of the chemical at its current phase, temperature, and pressure in units of [W/m/K].
Utilizes the object oriented interfaces
thermo.thermal_conductivity.ThermalConductivityLiquidandthermo.thermal_conductivity.ThermalConductivityGasto perform the actual calculation of each property.Examples
>>> Chemical('ethanol', T=300).kl 0.16 >>> Chemical('ethanol', T=400).kg 0.026
- property kg¶
Thermal conductivity of the chemical in the gas phase at its current temperature and pressure, in units of [W/m/K].
For calculation of this property at other temperatures and pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.thermal_conductivity.ThermalConductivityGas; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water', T=320, P=100).kg 0.02
- property kl¶
Thermal conductivity of the chemical in the liquid phase at its current temperature and pressure, in units of [W/m/K].
For calculation of this property at other temperatures and pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.thermal_conductivity.ThermalConductivityLiquid; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water', T=320).kl 0.63
- property ks¶
Thermal conductivity of the chemical in the solid phase at its current temperature and pressure, in units of [W/m/K].
For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.thermal_conductivity.ThermalConductivitySolid; each Chemical instance creates one to actually perform the calculations.
- property legal_status¶
Dictionary of legal status indicators for the chemical.
Examples
>>> Chemical('benzene').legal_status {'DSL': 'LISTED', 'TSCA': 'LISTED', 'EINECS': 'LISTED', 'NLP': 'UNLISTED', 'SPIN': 'LISTED'}
- property mass_fractions¶
Dictionary of atom:mass-weighted fractional occurence of elements. Useful when performing mass balances. For atom-fraction occurences, see
atom_fractions.Examples
>>> Chemical('water').mass_fractions {'H': 0.11189834407236524, 'O': 0.8881016559276347}
- property mu¶
Viscosity of the chemical at its current phase, temperature, and pressure in units of [Pa*s].
Utilizes the object oriented interfaces
thermo.viscosity.ViscosityLiquidandthermo.viscosity.ViscosityGasto perform the actual calculation of each property.Examples
>>> Chemical('ethanol', T=300).mu 0.0010 >>> Chemical('ethanol', T=400).mu 1.18e-05
- property mug¶
Viscosity of the chemical in the gas phase at its current temperature and pressure, in units of [Pa*s].
For calculation of this property at other temperatures and pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.viscosity.ViscosityGas; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water', T=320, P=100).mug 1.04e-05
- property mul¶
Viscosity of the chemical in the liquid phase at its current temperature and pressure, in units of [Pa*s].
For calculation of this property at other temperatures and pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.viscosity.ViscosityLiquid; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water', T=320).mul 0.000576
- property nu¶
Kinematic viscosity of the the chemical at its current temperature, pressure, and phase in units of [m^2/s].
Examples
>>> Chemical('argon').nu 1.38e-05
- property nug¶
Kinematic viscosity of the gas phase of the chemical at its current temperature and pressure, in units of [m^2/s].
Utilizes the temperature and pressure dependent object oriented interfaces
thermo.volume.VolumeGas,thermo.viscosity.ViscosityGasto calculate the actual properties.Examples
>>> Chemical('methane', T=115).nug 2.5e-06
- property nul¶
Kinematic viscosity of the liquid phase of the chemical at its current temperature and pressure, in units of [m^2/s].
Utilizes the temperature and pressure dependent object oriented interfaces
thermo.volume.VolumeLiquid,thermo.viscosity.ViscosityLiquidto calculate the actual properties.Examples
>>> Chemical('methane', T=110).nul 2.858e-07
- property permittivity¶
Relative permittivity (dielectric constant) of the chemical at its current temperature, [dimensionless].
For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.permittivity.PermittivityLiquid; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('toluene', T=250).permittivity 2.497
- property rdkitmol¶
RDKit object of the chemical, without hydrogen. If RDKit is not available, holds None.
For examples of what can be done with RDKit, see their website.
- property rdkitmol_Hs¶
RDKit object of the chemical, with hydrogen. If RDKit is not available, holds None.
For examples of what can be done with RDKit, see their website.
- property rho¶
Mass density of the chemical at its current phase and temperature and pressure, in units of [kg/m^3].
Utilizes the object oriented interfaces
thermo.volume.VolumeSolid,thermo.volume.VolumeLiquid, andthermo.volume.VolumeGasto perform the actual calculation of each property. Note that those interfaces provide output in units of m^3/mol.Examples
>>> Chemical('decane', T=550, P=2E6).rho 498.
- property rhog¶
Gas-phase mass density of the chemical at its current temperature and pressure, in units of [kg/m^3]. For calculation of this property at other temperatures or pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.volume.VolumeGas; each Chemical instance creates one to actually perform the calculations. Note that that interface provides output in molar units.Examples
Estimate the density of the core of the sun, at 15 million K and 26.5 PetaPascals, assuming pure helium (actually 68% helium):
>>> Chemical('helium', T=15E6, P=26.5E15).rhog 8519.
Compared to a result on Wikipedia of 150000 kg/m^3, the fundamental equation of state performs poorly.
>>> He = Chemical('helium', T=15E6, P=26.5E15) >>> He.VolumeGas.method_P = 'IDEAL' >>> He.rhog 850477.
The ideal-gas law performs somewhat better, but vastly overshoots the density prediction.
- property rhogm¶
Molar density of the chemical in the gas phase at the current temperature and pressure, in units of [mol/m^3].
Utilizes the object oriented interface and
thermo.volume.VolumeGasto perform the actual calculation of molar volume.Examples
>>> Chemical('tungsten hexafluoride').rhogm 42.
- property rhol¶
Liquid-phase mass density of the chemical at its current temperature and pressure, in units of [kg/m^3]. For calculation of this property at other temperatures and pressures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.volume.VolumeLiquid; each Chemical instance creates one to actually perform the calculations. Note that that interface provides output in molar units.Examples
>>> Chemical('o-xylene', T=297).rhol 876.9946785618097
- property rholm¶
Molar density of the chemical in the liquid phase at the current temperature and pressure, in units of [mol/m^3].
Utilizes the object oriented interface and
thermo.volume.VolumeLiquidto perform the actual calculation of molar volume.Examples
>>> Chemical('nitrogen', T=70).rholm 29937.
- property rhom¶
Molar density of the chemical at its current phase and temperature and pressure, in units of [mol/m^3].
Utilizes the object oriented interfaces
thermo.volume.VolumeSolid,thermo.volume.VolumeLiquid, andthermo.volume.VolumeGasto perform the actual calculation of each property. Note that those interfaces provide output in units of m^3/mol.Examples
>>> Chemical('1-hexanol').rhom 7986.
- property rhos¶
Solid-phase mass density of the chemical at its current temperature, in units of [kg/m^3]. For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.volume.VolumeSolid; each Chemical instance creates one to actually perform the calculations. Note that that interface provides output in molar units.Examples
>>> Chemical('iron').rhos 7870.
- property rhosm¶
Molar density of the chemical in the solid phase at the current temperature and pressure, in units of [mol/m^3].
Utilizes the object oriented interface and
thermo.volume.VolumeSolidto perform the actual calculation of molar volume.Examples
>>> Chemical('palladium').rhosm 112760.
- property rings¶
Number of rings in a chemical, computed with RDKit from a chemical’s SMILES. If RDKit is not available, holds None.
Examples
>>> Chemical('Paclitaxel').rings 7
- property sigma¶
Surface tension of the chemical at its current temperature, in units of [N/m].
For calculation of this property at other temperatures, or specifying manually the method used to calculate it, and more - see the object oriented interface
thermo.interface.SurfaceTension; each Chemical instance creates one to actually perform the calculations.Examples
>>> Chemical('water', T=320).sigma 0.068 >>> Chemical('water', T=320).SurfaceTension.solve_property(0.05) 417.2
- property solubility_parameter¶
Solubility parameter of the chemical at its current temperature and pressure, in units of [Pa^0.5].
Calculated based on enthalpy of vaporization and molar volume. Normally calculated at STP. For uses of this property, see
thermo.solubility.solubility_parameter.Examples
>>> Chemical('NH3', T=200).solubility_parameter 31712.