2528df0f75
These changes make it unnecessary to copy header files around during the build process, which tends to confuse IDEs and debuggers. The headers which comprise Cantera's external C++ interface are now in the 'include' directory. All of the samples and demos are now in the 'samples' subdirectory.
86 lines
2.5 KiB
Python
Executable file
86 lines
2.5 KiB
Python
Executable file
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import os
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from constants import *
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from ThermoPhase import ThermoPhase
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from Kinetics import Kinetics
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from Transport import Transport
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from set import setByName
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import XML
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import _cantera
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class Solution(ThermoPhase, Kinetics, Transport):
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"""
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A class for chemically-reacting solutions.
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Instances can be created to represent any type of solution -- a
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mixture of gases, a liquid solution, or a solid solution, for
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example.
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Class Solution derives from classes ThermoPhase, Kinetics, and
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Transport. It defines very few methods of its own, and is
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provided largely for convenience, so that a single object can be
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used to compute thermodynamic, kinetic, and transport properties
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of a solution. Functions like IdealGasMix and others defined in
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module gases return objects of class Solution.
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"""
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def __init__(self, src="", id="", loglevel = 0, debug = 0):
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self.ckin = 0
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self._owner = 0
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self.verbose = 1
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fname = os.path.basename(src)
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ff = os.path.splitext(fname)
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if src:
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root = XML.XML_Node(name = 'doc', src = src,
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preprocess = 1, debug = debug)
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if id:
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s = root.child(id = id)
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else:
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s = root.child(name = "phase")
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self._name = s['id']
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# initialize the equation of state
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ThermoPhase.__init__(self, xml_phase=s)
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# initialize the kinetics model
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ph = [self]
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Kinetics.__init__(self, xml_phase=s, phases=ph)
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# initialize the transport model
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Transport.__init__(self, xml_phase=s, phase=self,
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model = '', loglevel=loglevel)
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def __del__(self):
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Transport.__del__(self)
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Kinetics.__del__(self)
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ThermoPhase.__del__(self)
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def __repr__(self):
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return _cantera.phase_report(self._phase_id, self.verbose)
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def name(self):
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return self._name
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def set(self, **options):
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"""Set various properties.
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T --- temperature [K]
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P --- pressure [Pa]
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Rho --- density [kg/m3]
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V --- specific volume [m3/kg]
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H --- specific enthalpy [J/kg]
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U --- specific internal energy [J/kg]
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S --- specific entropy [J/kg/K]
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X --- mole fractions (string or array)
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Y --- mass fractions (string or array)
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Vapor --- saturated vapor fraction
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Liquid --- saturated liquid fraction
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"""
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setByName(self, options)
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