[Matlab] Add missing PureFluid constructors for fluids defined in liquidvapor.xml
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interfaces/matlab/toolbox/CarbonDioxide.m
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interfaces/matlab/toolbox/CarbonDioxide.m
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function c = CarbonDioxide()
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% CARBONDIOXIDE Return an object representing carbon dioxide.
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% c = CarbonDioxide
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% The object returned by this method implements an accurate equation of
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% state for carbon dioxide that can be used in the liquid, vapor, saturated
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% liquid/vapor, and supercritical regions of the phase diagram. The
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% equation of state is taken from
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%
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% Reynolds, W. C. *Thermodynamic Properties in SI: graphs, tables, and
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% computational equations for forty substances.* Stanford: Stanford
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% University, 1979. Print.
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%
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% For more details, see classes Cantera::PureFluid and tpx::CarbonDioxide in the
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% Cantera C++ source code documentation.
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%
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% :return:
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% Instance of class :mat:func:`Solution`
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%
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c = Solution('liquidvapor.xml', 'carbondioxide');
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interfaces/matlab/toolbox/HFC134a.m
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interfaces/matlab/toolbox/HFC134a.m
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function h = HFC134a()
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% HFC134A Return an object representing refrigerant HFC134a.
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% h = HFC134a()
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% The object returned by this method implements an accurate equation of
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% state for refrigerant HFC134a (R134a) that can be used in the liquid,
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% vapor, saturated liquid/vapor, and supercritical regions of the phase
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% diagram. Implements the equation of state given in:
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% R. Tillner-Roth and H.D. Baehr. "An International Standard Formulation for
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% The Thermodynamic Properties of 1,1,1,2-Tetrafluoroethane (HFC-134a) for
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% Temperatures From 170 K to 455 K and Pressures up to 70 MPa". J. Phys.
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% Chem. Ref. Data, Vol. 23, No. 5, 1994. pp. 657--729.
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% http://dx.doi.org/10.1063/1.555958
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%
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% For more details, see classes Cantera::PureFluid and tpx::HFC134a in the
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% Cantera C++ source code documentation.
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%
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% :return:
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% Instance of class :mat:func:`Solution`
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%
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h = Solution('liquidvapor.xml', 'hfc134a');
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interfaces/matlab/toolbox/Heptane.m
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interfaces/matlab/toolbox/Heptane.m
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function h = Heptane()
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% HEPTANE Return an object representing n-heptane.
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% h = Heptane()
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% The object returned by this method implements an accurate equation of
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% state for n-heptane that can be used in the liquid, vapor, saturated
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% liquid/vapor, and supercritical regions of the phase diagram. The
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% equation of state is taken from
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%
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% Reynolds, W. C. *Thermodynamic Properties in SI: graphs, tables, and
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% computational equations for forty substances.* Stanford: Stanford
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% University, 1979. Print.
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%
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% For more details, see classes Cantera::PureFluid and tpx::Heptane in the
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% Cantera C++ source code documentation.
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%
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% :return:
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% Instance of class :mat:func:`Solution`
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%
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h = Solution('liquidvapor.xml', 'heptane');
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