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diffusion_flame.py. (Source) """ An opposed-flow ethane/air diffusion flame Requires: cantera >= 3.0, matplotlib >= 2.0 Keywords: combustion, 1D flow, diffusion flame, strained flame, plotting, saving output """ from pathlib import Path import cantera as ct import matplotlib.pyplot as plt # Input parameters p = ct.one_atm # pressure tin_f = 300
Prerequisites The first step in installing the Cantera Python module using pip is to make sure you have a compatible version of Python installed and are able to run pip from the command line. Packages for Cantera 3.0.0 are available for Python versions 3.8, 3.9, 3.10
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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_test.py:. """ Compute the "equilibrium" and "frozen" sound speeds for a gas Requires: cantera >= 2.5.0 Keywords: thermodynamics, equilibrium """ import cantera as ct import math def equilSoundSpeeds(gas, rtol=1.0e-6, max_iter=5000): """ Returns a tuple containing the equilibrium and frozen sound
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.
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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.
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First, you'll need to install Cantera on your computer. We have instructions for many platforms in our Installation section. When using Cantera, the first thing you usually need is an object representing some phase of matter. Here, we'll create a gas mixture. Start MATLAB, and at the prompt type: >>>. >> gas1 = GRI30.
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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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Option 3: Install the development version of Cantera. To install a recent development snapshot (that is, an alpha or beta version) of Cantera, use the cantera/label/dev channel. Assuming you have an environment named ct-dev, you can type: conda activate ct-dev. conda install --channel cantera/label/dev cantera.
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.
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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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A three-body reaction is a gas-phase reaction of the form: \mathrm {A + B + M \rightleftharpoons AB + M} A+ B+M ⇌ AB+ M. Here \mathrm {M} M is an unspecified collision partner that carries away excess energy to stabilize the \mathrm {AB} AB molecule (forward direction) or supplies energy to break the \mathrm {AB} AB bond (reverse
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Published on August 22, 2023 | Full release on GitHub. The Cantera development team is pleased to announce the availability of Cantera 3.0.0. There have been over 1400
This example solves a plug flow reactor problem with surface chemistry. The specific problem simulated is the partial oxidation of methane over a platinum catalyst in a packed bed reactor. This example solves the DAE system directly, using the FlowReactor class and the SUNDIALS IDA solver, in contrast to the approximation as a chain of steady
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.