Mixture of Propane + Tetracontane

Datasets

1. T_fus - Solid-liquid equilibrium temperature, K

Solid-liquid equilibrium temperature, K [ref]

Fixed		Measured
Mole fraction of Tetracontane (2) - Liquid	Pressure, kPa - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0050	2630.00	323.75
0.0050	5040.00	322.96
0.0050	10070.00	322.26
0.0050	20030.00	322.15
0.0050	30050.00	322.68
0.0050	40040.00	323.57
0.0050	50010.00	324.71
0.0050	60090.00	325.90
0.0050	70090.00	327.29
0.0050	80020.00	328.59
0.0050	95210.00	330.86
0.0070	2580.00	325.46
0.0070	5250.00	324.94
0.0070	10060.00	324.33
0.0070	20040.00	324.17
0.0070	30010.00	324.83
0.0070	40060.00	325.86
0.0070	50110.00	326.90
0.0070	60890.00	328.25
0.0070	71050.00	329.63
0.0070	81260.00	330.98
0.0070	95240.00	333.20
0.0080	3160.00	325.95
0.0080	5110.00	325.14
0.0080	10070.00	324.72
0.0080	20090.00	325.14
0.0080	25050.00	325.33
0.0080	30090.00	325.55
0.0080	40090.00	326.58
0.0080	50050.00	327.48
0.0080	70100.00	330.05
0.0080	90160.00	333.22
0.0080	106130.00	336.20
0.0100	2540.00	327.97
0.0100	5060.00	326.82
0.0100	9980.00	326.31
0.0100	20110.00	326.24
0.0100	30030.00	327.00
0.0100	40070.00	328.17
0.0100	50030.00	329.53
0.0100	70060.00	332.51
0.0100	95100.00	336.04
0.0170	2780.00	328.21
0.0170	5020.00	328.09
0.0170	10090.00	327.88
0.0170	20060.00	328.30
0.0170	30190.00	329.23
0.0170	40050.00	330.43
0.0170	50050.00	331.90
0.0170	60110.00	333.44
0.0170	70230.00	334.97
0.0170	80100.00	336.52
0.0170	95120.00	338.90
0.0390	2460.00	330.14
0.0390	3070.00	330.30
0.0390	3080.00	330.35
0.0390	5100.00	330.39
0.0390	5210.00	330.24
0.0390	10100.00	330.61
0.0390	20190.00	331.77
0.0390	30130.00	333.20
0.0390	40180.00	334.77
0.0390	50200.00	336.43
0.0390	60200.00	338.24
0.0390	70220.00	339.86
0.0390	80240.00	341.57
0.0390	95350.00	344.23

Sources

• Phase behaviour in the vicinity of the three-phase solid liquid vapour line in asymmetric nonpolar systems at high pressures

Note: These property values are available through the Cheméo API. A free account gives you an access key.