lib.mEoS.C3
===========

Fluid info
----------

* CAS Number: 74-98-6
* Formula: CH3CH2CH3
* Synonym: R-290
* Molecular weigth: 44.09562 g/mol
* Tc:  369.8900 K
* Pc:  4.2512 MPa
* ρc:  220.4781 kg/m³
* Tt:  85.5250 K
* Tb:  231.0360 K
* Acentric factor: 0.1521
* Dipole moment:  0.0840 Debye

Equation of state
-----------------

* Lemmon, E.W., McLinden, M.O., Wagner, W.; Thermodynamic Properties of Propane.  III.  A Reference Equation of State for Temperatures from the Melting Line to 650 K and Pressures up to 1000 MPa. J. Chem. Eng. Data, 54(12) (2009) 3141-3180, http://dx.doi.org/10.1021/je900217v
* Younglove, B.A., Ely, J.F.; Thermophysical Properties of Fluids. II. Methane, Ethane, Propane, Isobutane, and Normal Butane. J. Phys. Chem. Ref. Data 16(4) (1987) 577-798, http://dx.doi.org/10.1063/1.555785
* Bücker, D., Wagner, W.; Reference Equations of State for the Thermodynamic Properties of Fluid Phase n-Butane and Isobutane. J. Phys. Chem. Ref. Data 35(2) (2006) 929-1019, http://dx.doi.org/10.1063/1.1901687
* Kunz, O., Wagner, W.; The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004. J. Chem.Eng. Data 57(11) (2012) 3032-3091, http://dx.doi.org/10.1021/je300655b
* Miyamoto, H., Watanabe, K.; A Thermodynamic Property Model for Fluid-Phase Propane. Int. J. Thermophys., 21(5) (2000) 1045-1072, http://dx.doi.org/10.1023/A:1026441903474
* Span, R., Wagner, W.; Equations of state for technical applications. II. Results for nonpolar fluids.. Int. J. Thermophys. 24 (1) (2003) 41-109, http://dx.doi.org/10.1023/A:1022310214958
* Sun, L., Ely, J.F.; Universal equation of state for engineering application: Algorithm and  application to non-polar and polar fluids. Fluid Phase Equilib., 222-223 (2004) 107-118, http://dx.doi.org/10.1016/j.fluid.2004.06.028
* Astina, I.M., Firmansyah, J.; Thermodynamic Property Model of Wide-Fluid Phase Propane. ITB J.Eng.Sci. 39(1) (2007) 43-65, http://dx.doi.org/10.5614/itbj.eng.sci.2007.39.1.4


Viscosity
---------

* Vogel, E., Herrmann, S.; New Formulation for the Viscosity of Propane. J. Phys. Chem. Ref. Data 45(4) (2016) 043103, http://dx.doi.org/10.1063/1.4966928

* Vogel, E., Küchenmeister, C., Bich, E., Laesecke, A.; Reference Correlation of the Viscosity of Propane. J. Phys. Chem. Ref. Data 27(5) (1998) 947-970, http://dx.doi.org/10.1063/1.556025

* Younglove, B.A., Ely, J.F.; Thermophysical Properties of Fluids. II. Methane, Ethane, Propane, Isobutane, and Normal Butane. J. Phys. Chem. Ref. Data 16(4) (1987) 577-798, http://dx.doi.org/10.1063/1.555785

* Quiñones-Cisneros, S.E., Deiters, U.K.; Generalization of the Friction Theory for Viscosity Modeling. J. Phys. Chem. B, 110(25) (2006) 12820-12834, http://dx.doi.org/10.1021/jp0618577

Thermal Conductivity
--------------------

* Marsh, K.N., Perkins, R.A., Ramires, M.L.V.; Measurement and Correlation of the Thermal Conductivity of Propane from 86 to 600 K at Pressures to 70 MPa. J. Chem. Eng. Data 47(4) (2002) 932-940, http://dx.doi.org/10.1021/je010001m

* Younglove, B.A., Ely, J.F.; Thermophysical Properties of Fluids. II. Methane, Ethane, Propane, Isobutane, and Normal Butane. J. Phys. Chem. Ref. Data 16(4) (1987) 577-798, http://dx.doi.org/10.1063/1.555785


Calculation example
-------------------

Using the first option for equation of state, we can get this diagram plots with the liquid-gas saturation region:

.. image:: images/C3.png

The diagram is generated with :download:`this module <../.script/plotMEoS.py>` running with the compound name as parameter or edited in file

.. code-block:: bash

    python3 plotMEoS.py C3