Setting up a Reactor Network #. First, let’s take a look at a basic example to see how we might utilize Cantera’s time integration functionality. We’ll simulate an isolated reactor in Python that is filled with a homogeneous gas mixture. The gas state used in this example is arbitrary, but interesting because it’s explosive.
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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First, let’s take a look at a basic example to see how we might utilize Cantera’s time integration functionality. We’ll simulate an isolated reactor in Python that is filled with a
Constant Pressure Reactor For this reactor model, the pressure is held constant. The energy equation is defined by the total enthalpy. A Constant Pressure Reactor is defined by the three state variables: \(m\), the mass of the reactor's contents (in kg) \(H\), the total enthalpy of the reactor's contents (in J)
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
(almost) every function in Cantera right here. This is the documentation for the current stable release, Cantera 3.0.0. For other versions, see the links at the bottom of the page. Search the documentation Python
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You'll find documentation for (almost) every function in Cantera right here. This is the documentation for the current stable release, Cantera 3.0.0. For other versions, see the
Continuous Reactor ¶. In this example we will illustrate how Cantera can be used to simulate a Continuously Stirred Tank Reactor (CSTR), also interchangeably referred to as a Perfectly Stirred Reactor or a Well Stirred Reactor, a Jet Stirred Reactor or a Longwell Reactor (there may well be more "aliases"). A cartoon of such a reactor is shown
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
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For those new to Cantera, we present here a set of short tutorials to familiarize you with Cantera's basic functionality and basic capabilities, give some examples of how to work Cantera within your preferred interface language—basic function calls and a few simple applications—and demonstrate some basic troubleshooting. After installing
Here, we'll create a gas mixture. Start MATLAB, and at the prompt type: >>>. >> gas1 = GRI30. If you have successfully installed the Cantera toolbox, you should see something like this: gri30: temperature 300 K. pressure 101325 Pa. density 0.0818891 kg/m^3.
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Bases: object. Transport data for a single gas-phase species which can be used in mixture-averaged or multicomponent transport models. The arguments passed to the constructor are equivalent to the properties of the object, with values in MKS units. To set properties in non-MKS units, use the set_customary_units method.
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macOS (64-bit Intel and 64-bit ARM (Apple Silicon)) Option 1: Create a new environment for Cantera. The following instructions will create a conda environment where you can use Cantera from Python. For this example, the environment is named ct-env. From the command line (or the Anaconda Prompt on Windows), run:
demo_ftnlib.cpp. This file is an example of how to write an interface to use Cantera in Fortran 77 programs. The basic idea is to store pointers to Cantera objects in global storage, and then create Fortran-callable functions
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)
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.
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 #.