R11

References

Equation of State

R.T Jacobsen, S.G. Penoncello, and E.W. Lemmon. A Fundamental Equation for Trichlorofluoromethane (R-11). Fluid Phase Equilib., 80:45–56, 1992. doi:10.1016/0378-3812(92)87054-Q.

Ideal gas specific heat

R.T Jacobsen, S.G. Penoncello, and E.W. Lemmon. A Fundamental Equation for Trichlorofluoromethane (R-11). Fluid Phase Equilib., 80:45–56, 1992. doi:10.1016/0378-3812(92)87054-Q.

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]

0.137368

CAS number

75-69-4

ASHRAE class

A1

Formula

\(CCl_{3}F\)

Acentric factor

0.1887506482528083

InChI

InChI=1S/CCl3F/c2-1(3,4)5

InChIKey

CYRMSUTZVYGINF-UHFFFAOYSA-N

SMILES

C(F)(Cl)(Cl)Cl

ChemSpider ID

6149

2D image

http://www.chemspider.com/ImagesHandler.ashx?id=6149

Limits

Maximum temperature [K]

625.0

Maximum pressure [Pa]

100000000.0

Triple point

Triple point temperature [K]

162.68

Triple point pressure [Pa]

6.510089834177898

Critical point

Critical point temperature [K]

471.06

Critical point density [kg/m3]

565.0

Critical point density [mol/m3]

4113.0394269407725

Critical point pressure [Pa]

4394000.0

Reducing point

Reducing point temperature [K]

471.11

Reducing point density [mol/m3]

4032.962

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.

../../_images/R11.png

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.

../../_images/R111.png