R1233zd(E)

References

Equation of State

María E. Mondejár, Mark O. McLinden, and Eric W. Lemmon. Thermodynamic Properties of trans-1-Chloro-3,3,3-trifluoropropene (R1233zd(E)): Vapor Pressure, ($p$, ρ, $T$) Behavior, and Speed of Sound Measurements, and Equation of State. J. Chem. Eng. Data, 60:2477–2489, 2015. doi:10.1021/acs.jced.5b00348.

Viscosity

Ian H. Bell and Arno Laesecke. Viscosity of refrigerants and other working fluids from residual entropy scaling . In 16th International Refrigeration and Air Conditioning Conference at Purdue, July 11-14, 2016. 2016.

Surface Tension

Chieko Kondou, Ryuichi Nagata, Noriko Nii, Shigeru Koyama, and Yukihiro Higashi. Surface tension of low GWP refrigerants R1243zf, R1234ze(Z), and R1233zd(E). Int. J. Refrig., 53:80–89, 2015. doi:10.1016/j.ijrefrig.2015.01.005.

Aliases

R1233zdE, R1233ZDE, R1233ZD(E), R1233ZD

Fluid Information

Parameter, Value
General
Molar mass [kg/mol]	0.1304944
CAS number	102687-65-0
ASHRAE class
Formula	C3ClF3H2
Acentric factor	0.3024522935802516
InChI	InChI=1S/C3H2ClF3/c4-2-1-3(5,6)7/h1-2H/b2-1+
InChIKey	LDTMPQQAWUMPKS-OWOJBTEDSA-N
SMILES	C(=C/Cl)C(F)(F)F
ChemSpider ID	4647642
Limits
Maximum temperature [K]	550.0
Maximum pressure [Pa]	100000000.0
Triple point
Triple point temperature [K]	195.15
Triple point pressure [Pa]	273.3075826995413
Critical point
Critical point temperature [K]	439.60083307567265
Critical point density [kg/m3]	480.2202426778309
Critical point density [mol/m3]	3680.0065188838057
Critical point pressure [Pa]	3623689.2162298746

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.

Superancillary Plots

The following figure shows the accuracy of the superancillary functions relative to extended precision calculations carried out in C++ with the teqp library. The results of the iterative calculations with REFPROP and CoolProp are also shown.

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.