R1336mzz(E)

References

Equation of State

Ryo Akasaka, Marcia L. Huber, Luke Simoni, and Eric W. Lemmon. A Helmholtz Energy Equation of State for trans-1,1,1,4,4,4-Hexafluoro-2-butene [R-1336mzz(E)]. International Journal of Thermophysics, 44:1003–1013, 2023. doi:10.1007/s10765-022-03143-5.

Aliases

(E)-1,1,1,4,4,4-HEXAFLUORO-2-BUTENE, r1336mzz(e), R1336mzz(E), (E)-1,1,1,4,4,4-Hexafluoro-2-butene, R1336MZZ(E), (e)-1,1,1,4,4,4-hexafluoro-2-butene, R1336MZZE

Fluid Information

Parameter, Value

General

Molar mass [kg/mol]

0.1640491

CAS number

66711-86-2

ASHRAE class

A1

Formula

C4H2F6

Acentric factor

0.4127686952181142

InChI

InChI=1S/C4H2F6/c5-3(6,7)1-2-4(8,9)10/h1-2H/b2-1+

InChIKey

NLOLSXYRJFEOTA-OWOJBTEDSA-N

SMILES

?

ChemSpider ID

-1

Limits

Maximum temperature [K]

410.0

Maximum pressure [Pa]

5700000.0

Triple point

Triple point temperature [K]

200.15

Triple point pressure [Pa]

649.2743290501494

Critical point

Critical point temperature [K]

403.5300000000283

Critical point density [kg/m3]

513.3096339006798

Critical point density [mol/m3]

3129.000000004144

Critical point pressure [Pa]

2779002.215494328

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/R1336mzz%28E%29.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.

fluid_properties/fluids/Consistencyplots/R1336mzz(E).png

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.

../../_images/R1336mzz%28E%291.png