# R12¶

## References¶

### Equation of State¶

Volker Marx, Andreas Pruss, and Wolfgang Wagner. Neue Zustandsgleichung für R 12, R 22, R 11 und R 113 - Beschreibung des therodynamischen Zustandsverhaltens bei Temperaturen bis 525 K und Druücken bis 200 MPa. volume 19. VDI Verlag, 1992.

### Thermal Conductivity¶

Mark O. McLinden, Sanford A. Klein, and Richard A. Perkins. An extended corresponding states model for the thermal conductivity of refrigerants and refrigerant mixtures. Int. J. Refrig., 23:43–63, 2000. doi:10.1016/S0140-7007(99)00024-9.

### Viscosity¶

S.A. Klein, M.O. McLinden, and A. Laesecke. An improved extended corresponding states method for estimation of viscosity of pure refrigerants and mixtures. Int. J. Refrig., 20:208–217, 1997. doi:10.1016/S0140-7007(96)00073-4.

### Surface Tension¶

A. Mulero, I. Cachadiña, and M. I. Parra. Recommended Correlations for the Surface Tension of Common Fluids. J. Phys. Chem. Ref. Data, 41(4):043105–1:13, 2012. doi:10.1063/1.4768782.

## Fluid Information¶

Parameter, Value
General
Molar mass [kg/mol] 0.120913
CAS number 75-71-8
ASHRAE class A1
Formula $$CCl_{2}F_{2}$$
Acentric factor 0.179478317344
InChI InChI=1/CCl2F2/c2-1(3,4)5
InChIKey PXBRQCKWGAHEHS-UHFFFAOYAX
SMILES C(F)(F)(Cl)Cl
ChemSpider ID 6151
2D image
Limits
Maximum temperature [K] 525.0
Maximum pressure [Pa] 200000000.0
Triple point
Triple point temperature [K] 116.099
Triple point pressure [Pa] 0.242550800688
Critical point
Critical point temperature [K] 385.12
Critical point density [kg/m3] 565.0
Critical point density [mol/m3] 4672.78125594
Critical point pressure [Pa] 4136100.0

## REFPROP Validation Data¶

Note

This figure compares the results generated from CoolProp and those generated from REFPROP. They are all results obtained in the form $$Y(T,\rho)$$, where $$Y$$ is the parameter of interest and which for all EOS is a direct evaluation of the EOS

You can download the script that generated the following figure here: (link to script), right-click the link and then save as... or the equivalent in your browser. You can also download this figure as a PDF.

## Consistency Plots¶

The following figure shows all the flash routines that are available for this fluid. A red + is a failure of the flash routine, a black dot is a success. Hopefully you will only see black dots. The red curve is the maximum temperature curve, and the blue curve is the melting line if one is available for the fluid.

In this figure, we start off with a state point given by T,P and then we calculate each of the other possible output pairs in turn, and then try to re-calculate T,P from the new input pair. If we don’t arrive back at the original T,P values, there is a problem in the flash routine in CoolProp. For more information on how these figures were generated, see CoolProp.Plots.ConsistencyPlots

Note

You can download the script that generated the following figure here: (link to script), right-click the link and then save as... or the equivalent in your browser. You can also download this figure as a PDF.