Neon#

References#

Equation of State#

M. Thol, R. Beckmüller, R. Weiss, A.H. Harvey, E.W. Lemmon, R.T. Jacobsen, and R. Span. Thermodynamic properties for neon for temperatures from the triple point to 700 k at pressures to 700 mpa. J. Phys. Chem Ref. Data, 2019, Submitted.

Melting Line#

Ian H. Bell. Melting line correlation for neon. 2026. Polynomial-in-theta correlation, p = p_t [1 + sum_i a_i (T/T_t - 1)^t_i], fit to the solid-liquid (crystal phase C1) melting data evaluated in the NIST ThermoData Engine (Frenkel et al., J. Chem. Inf. Model. 45, 816 (2005)). The triple point (T_t = 24.556 K, p_t = 43.417 kPa) and the saturated-liquid molar volume are taken from the Thol et al. neon EOS (J. Phys. Chem. Ref. Data 48, 023101 (2019)) as implemented in CoolProp. The leading linear term is constrained so that the slope at the triple point matches the Clausius-Clapeyron value dp/dT = dS_fus/dV_fus = 6.28 MPa/K, using dH_fus = 335 J/mol and a solid density of 1.444 g/cm^3. The correlation reproduces the experimental melting temperatures to 0.97 K RMS (3.0 K maximum) over 24.6-328 K, and supersedes the prior fit that was high by roughly a factor of 16. Crystal phase: neon has a single solid phase (fcc, C1) along the melting line in this range, so no phase ambiguity arises.

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.

Aliases#

neon, NEON, R720

Molecular Structure#

Neon — 2D structure (interactive: click and drag to rotate)

Fluid Information#

Parameter, Value

General

Molar mass [kg/mol]

0.020179

CAS number

7440-01-9

ASHRAE class

A1

Formula

Ne

Acentric factor

-0.03549258024442481

InChI

InChI=1S/Ne

InChIKey

GKAOGPIIYCISHV-UHFFFAOYSA-N

SMILES

[Ne]

ChemSpider ID

22377

Limits

Maximum temperature [K]

725.0

Maximum pressure [Pa]

1000000000.0

Triple point

Triple point temperature [K]

24.560000000000002

Triple point pressure [Pa]

43417.232458065846

Critical point

Critical point temperature [K]

44.39999970498691

Critical point density [kg/m3]

486.31370002144575

Critical point density [mol/m3]

24099.990089768857

Critical point pressure [Pa]

2661630.706279463

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/Neon.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/Neon1.png

Flash consistency (HEOS): 0 inconsistent, 21 exceptions, 0 bad-phase across 1 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

EXCEPTION

1phase

7.73136e+08

660.3

Dmolar

53459

P

7.73136e+08

The temperature of -4964.467257 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

7.73136e+08

676.475

Dmolar

52952.6

P

7.73136e+08

The temperature of -90.258805 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

7.73136e+08

692.65

Dmolar

52457.7

P

7.73136e+08

The temperature of -213.545794 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

7.73136e+08

708.825

Dmolar

51973.8

P

7.73136e+08

The temperature of -337.909846 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

7.73136e+08

725

Dmolar

51500.4

P

7.73136e+08

The temperature of -442.716051 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

488.372

Dmolar

66150

P

1e+09

The temperature of -353.686620 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

504.148

Dmolar

65508.3

P

1e+09

The temperature of -2811.822334 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

519.923

Dmolar

64882.6

P

1e+09

The temperature of -25482.380428 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

535.698

Dmolar

64272.3

P

1e+09

The temperature of -10391.808865 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

551.473

Dmolar

63677

P

1e+09

The temperature of -6778.930360 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

567.248

Dmolar

63095.9

P

1e+09

The temperature of -5165.648676 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

583.023

Dmolar

62528.6

P

1e+09

The temperature of -4257.286805 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

598.799

Dmolar

61974.4

P

1e+09

The temperature of -3678.529861 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

614.574

Dmolar

61433

P

1e+09

The temperature of -3280.385617 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

630.349

Dmolar

60903.8

P

1e+09

The temperature of -2991.929983 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

646.124

Dmolar

60386.4

P

1e+09

The temperature of -2775.093515 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

661.899

Dmolar

59880.3

P

1e+09

The temperature of -2607.610912 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

677.674

Dmolar

59385

P

1e+09

The temperature of -2475.592769 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

693.45

Dmolar

58900.3

P

1e+09

The temperature of -2369.929489 K is below the minimum of 0.000000 K

DmolarP

EXCEPTION

1phase

1e+09

709.225

Dmolar

58425.7

P

1e+09

The temperature of -2284.403949 K is below the minimum of 0.000000 K

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/Neon2.png