R1224YDZ#

References#

Equation of State#

Ryo Akasaka and Eric W. Lemmon. A Helmholtz Energy Equation of State for cis-1-Chloro-2,3,3,3-tetrafluoro-1-propene [R-1224yd(Z)]. International Journal of Thermophysics, 2023. doi:10.1007/s10765-023-03266-3.

Ideal gas specific heat#

Ryo Akasaka and Eric W. Lemmon. A Helmholtz Energy Equation of State for cis-1-Chloro-2,3,3,3-tetrafluoro-1-propene [R-1224yd(Z)]. International Journal of Thermophysics, 2023. doi:10.1007/s10765-023-03266-3.

Molecular Structure#

R1224YDZ — 3D conformer (interactive: click and drag to rotate)

Fluid Information#

Parameter, Value

General

Molar mass [kg/mol]

0.14848670000000003

CAS number

111512-60-8

ASHRAE class

?

Formula

CF3CF=CHCl (cis)

Acentric factor

0.325

InChI

InChI=1S/C3HClF4/c4-1-2(5)3(6,7)8/h1H/b2-1-

InChIKey

GDPWRLVSJWKGPJ-UPHRSURJSA-N

SMILES

?

ChemSpider ID

-1

Limits

Maximum temperature [K]

473.15

Maximum pressure [Pa]

35200000.0

Triple point

Triple point temperature [K]

157.8

Triple point pressure [Pa]

2.536605496114026

Critical point

Critical point temperature [K]

428.6900000000627

Critical point density [kg/m3]

539.3036944019578

Critical point density [mol/m3]

3632.000000013185

Critical point pressure [Pa]

3334038.4705547076

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/R1224YDZ.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/R1224YDZ1.png

Flash consistency (HEOS): 3 inconsistent, 0 exceptions, 0 bad-phase across 2 input pair(s).

Download full failure list (CSV)

Failing state points (sample, up to 20 per pair/class)

Pair

Class

Region

P [Pa]

T [K]

In1

Val1

In2

Val2

Error

DmolarP

INCONSISTENT

1phase

3.9048

158.9

Dmolar

11472.3

P

3.9049

DmolarP

INCONSISTENT

1phase

32.1161

175.015

Dmolar

11211.2

P

32.1165

HmolarSmolar

INCONSISTENT

2phase

2.98998

158.8

Hmolar

12082.1

Smolar

65.289

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/R1224YDZ2.png