Mixture of 1,2-Ethanediol + 1,3-Butanediol

Datasets

1. Mole fraction
2. T_boil(P) - Boiling temperature at pressure P, K

Mole fraction of 1,2-Ethanediol (1) [ref]

Operational condition: Pressure, kPa = 10 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Mole fraction of 1,2-Ethanediol (1) - Gas
1.0000	1.0000
0.9640	0.9700
0.9090	0.9240
0.8240	0.8690
0.7680	0.8250
0.7100	0.7970
0.6540	0.7560
0.6170	0.7270
0.5950	0.7100
0.5540	0.6750
0.5190	0.6470
0.4910	0.6240
0.4670	0.6020
0.4580	0.5940
0.4270	0.5640
0.3590	0.4940
0.3160	0.4430
0.2740	0.4040
0.2330	0.3540
0.2090	0.3240
0.0880	0.1610
0.0400	0.0730
0.0000	0.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 10 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	406.09
0.9640	406.22
0.9090	406.46
0.8240	406.92
0.7680	407.28
0.7100	407.60
0.6540	408.05
0.6170	408.40
0.5950	408.62
0.5540	409.10
0.5190	409.39
0.4910	409.59
0.4670	409.91
0.4580	410.03
0.4270	410.41
0.3590	411.21
0.3160	411.81
0.2740	412.40
0.2330	412.98
0.2090	413.34
0.0880	415.33
0.0400	416.18
0.0000	416.91

Sources

• Isobaric Vapor Liquid Equilibria for the Binary Mixtures Composed of Ethylene Glycol, 1,2-Propylene Glycol, 1,2-Butanediol, and 1,3-Butanediol at 10.00 kPa

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