This documentation is for an old version of Cantera. You can find docs for newer versions here.

Migrating from the Old Python Module

With the introduction of the new Cython-based Python module in Cantera 2.1, there are a number of changes to the interface which require modifications to scripts in order for them to work with the new module. Broadly speaking, the changes to the interface are intended to make the Cantera Python module easier to use, and provide a more “Pythonic” interface by making use of common Python language idioms, language features, and style guidelines.

This document describes the changes to the Python module which are likely to require modifications to existing code.

Importing the Python Module

The name of the Python module is now cantera with a lowercase “c”. This change is made partly for compliance with PEP8.

Furthermore, the various submodules, e.g. Cantera.Reactor have been eliminated. All classes and functions are available directly in the cantera module.

To avoid the namespace clutter introduced by using import *, the following syntax is preferred:

>>> import cantera as ct

Naming Conventions

Generally, the names used in the Cantera Python module have been changed to follow the recommendations of PEP8. This means that the names of methods and properties are generally written as lowercase_with_underscores instead of capitalizingEachWord. Also, some abbreviated names have been expanded. For example, the following function calls:

>>> gas.speciesName(0)
>>> gas.nAtoms('H2', 'H')
>>> gas.reactionEqn(3)

should be replaced with:

>>> gas.species_name(0)
>>> gas.n_atoms('H2', 'H')
>>> gas.reaction_equation(3)

Importing Phases

The functions importPhase and IdealGasMix have been removed. Solution objects, which represent the phase (regardless of the underlying thermodynamic model) as well as providing access to kinetics and transport properties, are created directly using the Solution class. For example:

>>> gas = Solution('h2o2.xml')

Creates an object which represents an IdealGasPhase mixture with a GasKinetics reaction mechansm and a MixTransport transport model, based on the parameters specified in the input file.

For importing multiple phases from a single file, the importPhases function has been retained with the new name import_phases:

>>> gas, anode_bulk, oxide = ct.import_phases('sofc.cti',
                                              ['gas', 'metal', 'oxide_bulk'])

Interfaces and edges are created using the Interface class, which represents both 1D and 2D interfaces, rather than using the importEdge and importInterface functions:

>>> anode_surf = ct.Interface('sofc.cti', 'metal_surface', [gas])
>>> oxide_surf = ct.Interface('sofc.cti', 'oxide_surface', [gas, oxide])
>>> tpb = ct.Interface('sofc.cti', 'tpb', [anode_bulk, anode_surf, oxide_surf])

Accessing Properties

Most methods for accessing and setting the properties of objects have been replaced with Python “properties” which do not need to be “called” in order to accessed or changed. For example, the following:

>>> u = gas.intEnergy_mass()
>>> Wmx = gas.meanMolecularWeight()
>>> kf = gas.fwdRateConstants()
>>> gas.setName('foo')

should be replaced with:

>>> u = gas.int_energy_mass
>>> Wmx = gas.mean_molecular_weight
>>> kf = gas.forward_rate_constants
>>> gas.name = 'foo'

Some common properties have been renamed according to the variable that is typically used to represent them:

>>> gas.temperature()
>>> gas.pressure()
>>> gas.massFractions()

should be replaced with:

>>> gas.T
>>> gas.P
>>> gas.Y

For pure fluid phases, the property X refers to the vapor mass fraction or “quality” of the phase. The following:

>>> w = Cantera.liquidvapor.Water()
>>> w.set(T=400, Vapor=0.5)

should be replaced with:

>>> w = ct.Water()
>>> w.TX = 400, 0.5

Setting Thermodynamic State

The set method has been removed in favor of property pairs or triplets. The following:

>>> gas.setMoleFractions('CH4:1.0, O2:0.1')
>>> gas.set(X='CH4:1.0, O2:0.1')
>>> gas.set(U=-1.1e6, V=5.5)
>>> gas.set(T=300, P=101325, Y='H2:1.0')

should be replaced with:

>>> gas.X = 'CH4:1.0, O2:0.1'
>>> gas.X = 'CH4:1.0, O2:0.1'
>>> gas.UV = -1.1e6, 5.5
>>> gas.TPY = 300, 101325, 'H2:1.0'

The saveState and restoreState methods have been removed. Their functionality can be replicated as follows:

>>> state = gas.TDY
>>> # (operations that modify gas)
>>> gas.TDY = state

Printing Phase Summaries

Solution objects no longer print out a verbose summary as their string representation. Instead, the summary report can be generated using the report() method, which returns a string, or by calling the Solution object to print the report to the screen. The following are equivalent:

>>> print(gas.report())
>>> gas()

Getting Properties for a Subset of Species

Some methods previously accepted an optional list of species as a filter, e.g.:

>>> gas.massFractions(['OH','H'])

This is not compatible with the Python “property” syntax, so the following alternative is used instead:

>>> gas['OH','H2'].Y
array([ 0.,  1.])

This works for any property which returns a value for each species, and works with species names, indices, and index ranges:

>>> gas[1,2,6].partial_molar_cp
array([ 20786.15525072,  21900.30946418,  34929.99146762])

>>> gas[3:6].species_names
['O2', 'OH', 'H2O']

Furthermore, the “sliced” object itself can be saved and used without needing to specify the species list again:

>>> reactants = gas['H2','O2']
>>> reactants.X
array([ 1.,  0.])

Transport Models

The old method for setting the transport model, switchTransportModel has been replaced with the transport_model property. To use the multicomponent transport model:

>>> gas.transport_model = 'Multi'

Note that unlike the previous implementation, only one transport model can be associated with a Solution object at a time, so there is a larger cost with switching models. If you need to alternate between transport models, it is generally better to use two different Solution objects.

Reactor Networks

As with the Solution class, properties are now used to get and set most parameters of reactors, flow devices, walls, etc. The following old code:

>>> Y = reactor.massFractions()
>>> X = reactor.contents().moleFractions()
>>> wall.setArea(2.0)

>>> net.setTolerances(1e-8, 1e-14)

should be replaced with:

>>> Y = reactor.Y
>>> X = reactor.thermo.X
>>> wall.area = 2.0

>>> net.rtol = 1e-8
>>> net.atol = 1e-14

Time-varying parameters have not been replaced with properties, since they need to be evaluated at a particular time.

Elimination of the Func Module

The Func module is no longer necessary, as the Cython module allows any callable Python object (lambda, function, or class) to be used in places where a function of a single variable are needed. For example, to set the velocity of a wall as a function of time, the following are equivalent:

>>> wall.set_velocity(lambda t: np.cos(3*t))

>>> def myfunc(z):
...     return np.cos(3*z)
>>> wall.set_velocity(myfunc)

One-Dimensional Reacting Flows

As elsewhere, the set method has been eliminated. The following old usage:

>>> f.fuel_inlet.set(massflux=mdot_f,
>>>                  mole_fractions=comp_f,
>>>                  temperature=tin_f)

>>> f.set(energy = 'off')

should be replaced with:

>>> f.fuel_inlet.mdot = mdot_f
>>> f.fuel_inlet.X = comp_f
>>> f.fuel_inlet.T = tin_f

>>> f.energy_enabled = False

However, the methods for setting tolerances and refinement criteria have been retained in slightly modified forms. The following:

>>> f.set(tol=tol_ss, tol_time=tol_ts)
>>> f.setRefineCriteria(ratio=4, slope=0.2, curve=0.3, prune=0.04)

should be replaced with:

>>> f.flame.set_steady_tolerances(default=tol_ss)
>>> f.flame.set_transient_tolerances(default=tol_ts)
>>> f.set_refine_criteria(ratio=4, slope=0.2, curve=0.3, prune=0.04)

To change the transport model and enable calculation of the Soret diffusion term, the following:

>>> gas.addTransportModel('Multi')
>>> gas.switchTransportModel('Multi')
>>> f.flame.setTransportModel(gas)
>>> f.flame.enableSoret()

should be replaced with:

>>> f.transport_model = 'Multi'
>>> f.soret_enabled = True