For those new to Cantera, we present here a set of short tutorials to familiarize you with Cantera’s basic functionality and capabilities, give some examples of how to work
Instances of class Kinetics are responsible for evaluating reaction rates of progress, species production rates, and other quantities pertaining to a reaction mechanism. Add a new reaction to this phase. Creation rates for each species. [kmol/m^3/s] for bulk phases or [kmol/m^2/s] for surface phases.
In this example we simulate a freely-propagating, adiabatic, 1-D flame, calculate its laminar burning velocity and perform a sensitivity analysis of its kinetics. The figure below illustrates the setup, in a flame-fixed co-ordinate system. The reactants enter with density \rho_ {u} ρu, temperature T_ {u} T u and speed S_ {u} S u.
Cantera 3.0.0 Cantera 2.6.0 Cantera 2.5.1 Cantera 2.4.0 Cantera 2.3.0 Cantera 2.2.1 Cantera 2.1.2 Cantera 2.0.2 Science Reference Thermodynamic Properties Species Thermodynamic Models Phase Thermodynamic Models Chemical Reactions Reaction Rates
Class ThermoPhase may be used to represent the intensive thermodynamic state of a phase of matter, which might be a gas, liquid, or solid. Class ThermoPhase is not usually instantiated directly. It is used as a base class for classes Solution and Interface. DP #. Get/Set density [kg/m^3] and pressure [Pa]. DPX #.
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Reactors ¶. A Cantera Reactor() represents the simplest form of a chemically reacting system. It corresponds to an extensive thermodynamic control volume V V, in which all state variables are homogeneously distributed. The system is generally unsteady -- that is, all states are functions of time. In particular, transient state changes due to
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Information on how to locate and work with Cantera input files (which contain the thermodynamic, transport, and chemical kinetic information for the phases of interest).
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In case of the Ideal Gas Reactor Model, the reactor temperature T T is used instead of the total internal energy U U as a state variable. For an ideal gas, we can rewrite the total internal energy in terms of the mass fractions and temperature: U = m \sum_k Y_k u_k (T) U = m k∑Y kuk(T)
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This pages provide detailed reference documentation for Cantera. Programming Reference # These sections document the classes and functions that define the Cantera interface
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Cantera is currently used for applications including combustion, detonations, electrochemical energy conversion and storage, fuel cells, batteries, aqueous electrolyte solutions, plasmas, and thin film deposition. Where do I get started? The tutorials linked below will get you started using Cantera on your own machine. Python Convert Input Files.
Getting Started ¶. First, you'll need to install Cantera on your computer. We have instructions for many platforms in our Installation section. Start by opening an interactive Python session, for example by running IPython. Import the Cantera Python module and NumPy by running: >>> importcanteraasct>>> importnumpyasnp.
Reactors and Reactor Networks. #. In Cantera, a reactor network represents a set of one or more homogeneous reactors and reacting surfaces that may be connected to each other and to the environment through devices representing mass flow, heat transfer, and moving walls. The system is generally unsteady – that is, all states are functions of time.
Handling Errors in Input Files. #. During processing of an input file, errors may be encountered. These could be syntax errors, or could be ones that are flagged as errors by Cantera due to some apparent inconsistency in the data—an unphysical value, a species that contains an undeclared element, a reaction that contains an undeclared species
In this section, we describe how Cantera uses species and phase information to calculate thermodynamic properties. Thermodynamic properties typically depend on information at both the species and phase levels. Generally, the species thermodynamic model and accompanying coefficient data specifies how the reference enthalpy and entropy values
Module-level documentation #. ck2yaml.py: Convert Chemkin-format mechanisms to Cantera YAML input files. If the output file name is not given, an output file with the same name as the input file, with the extension changed to ‘.yaml’. An input file containing only species definitions (which can be referenced from phase definitions in other
Currently, the identity of the reference velocity is coded into each transport object as a typedef named VelocityBasis, which is equated to an integer. Negative values of this variable refer to mass or mole-averaged velocities. Zero or positive quantities refers to the reference velocity being referenced to a particular species.
Here, we describe how Cantera uses species and phase information to calculate transport properties and rates. Similar to Cantera’s approach to thermodynamic properties, transport property calculations in Cantera depend on information at both the species and phase levels. The user must specify transport models for both levels, and these
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Sometimes you just need a little more detail. You'll find documentation for (almost) every function in Cantera right here. This is the documentation for the current stable release,
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One-Dimensional Flames. ¶. Cantera includes a set of models for representing steady-state, quasi-one- dimensional reacting flows. These models can be used to simulate a number of common flames, such as: freely-propagating premixed laminar flames. burner-stabilized premixed flames. counterflow diffusion flames.