Mixture of Pentanoic acid, ethyl ester + Ethanol

Datasets

1. T_boil - Boiling temperature at pressure P, K

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
91.40	1.0000	349.10
91.40	0.8940	350.70
91.40	0.7850	352.20
91.40	0.6950	353.70
91.40	0.6450	354.80
91.40	0.5930	355.90
91.40	0.5420	357.40
91.40	0.4920	359.60
91.40	0.4360	359.70
91.40	0.3580	361.90
91.40	0.3030	362.60
91.40	0.2250	369.90
91.40	0.1860	374.60
91.40	0.0980	386.20
91.40	0.0630	394.70
91.40	0.0320	401.10
91.40	0.0240	405.10
91.40	0.0190	404.90
91.40	0.0050	410.30
91.40	0.0030	414.10
91.40	0.0000	414.40
6.90	0.8010	301.50
6.90	0.6000	301.90
6.90	0.5000	302.10
6.90	0.2040	305.30
6.90	0.0330	316.80
6.90	0.0000	341.00
8.90	1.0000	303.30
8.90	0.8010	305.70
8.90	0.6000	305.50
8.90	0.5000	306.10
8.90	0.2040	309.50
8.90	0.0330	322.50
8.90	0.0000	345.50
13.70	1.0000	309.90
13.70	0.8010	312.70
13.70	0.6000	314.30
13.70	0.5000	313.70
13.70	0.2040	318.30
13.70	0.0330	333.90
13.70	0.0000	354.10
23.90	1.0000	320.00
23.90	0.8010	323.90
23.90	0.6000	324.00
23.90	0.5000	324.50
23.90	0.2040	329.80
23.90	0.0000	367.50
39.10	1.0000	330.10
39.10	0.8010	333.80
39.10	0.6000	334.50
39.10	0.5000	335.10
39.10	0.2040	341.30
39.10	0.0330	358.10
39.10	0.0000	383.00
54.00	1.0000	337.50
54.00	0.8010	341.00
54.00	0.6000	341.90
54.00	0.5000	342.30
54.00	0.2040	348.50
54.00	0.0330	368.40
54.00	0.0000	393.50
69.50	1.0000	342.80
69.50	0.8010	347.30
69.50	0.6000	348.10
69.50	0.5000	348.30
69.50	0.2040	354.30
69.50	0.0330	386.00
69.50	0.0000	401.50

Sources

• Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state

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