Mixture of Acetic acid, pentyl ester + 1-Pentanol

Datasets

1. Azeotropic composition: mole fraction (4)
2. T_boil - Boiling temperature at pressure P, K (4)
3. Azeotropic temperature, K (2)

Azeotropic composition: mole fraction of 1-Pentanol (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of 1-Pentanol (2) - Liquid
26.66	0.6940
53.33	0.8620

Mole fraction of 1-Pentanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Mole fraction of 1-Pentanol (2) - Gas
0.0000	0.0000
0.0089	0.0160
0.0252	0.0430
0.0265	0.0450
0.0752	0.1200
0.1860	0.2660
0.3240	0.4140
0.3560	0.4460
0.3760	0.4630
0.4040	0.4900
0.4460	0.5260
0.4980	0.5700
0.5580	0.6230
0.6240	0.6750
0.7350	0.7690
0.7600	0.7890
0.7770	0.8030
0.8001	0.8240
0.8090	0.8300
0.8440	0.8600
0.9000	0.9080
0.9822	0.9830
1.0000	1.0000

Azeotropic composition: mole fraction of 1-Pentanol (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of 1-Pentanol (2) - Liquid
26.66	0.6940
53.33	0.8620

Mole fraction of 1-Pentanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Mole fraction of 1-Pentanol (2) - Gas
0.0000	0.0000
0.0089	0.0160
0.0252	0.0430
0.0265	0.0450
0.0752	0.1200
0.1860	0.2660
0.3240	0.4140
0.3560	0.4460
0.3760	0.4630
0.4040	0.4900
0.4460	0.5260
0.4980	0.5700
0.5580	0.6230
0.6240	0.6750
0.7350	0.7690
0.7600	0.7890
0.7770	0.8030
0.8001	0.8240
0.8090	0.8300
0.8440	0.8600
0.9000	0.9080
0.9822	0.9830
1.0000	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of 1-Pentanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
26.66	0.0000	380.05
26.66	0.1000	378.25
26.66	0.2000	376.97
26.66	0.3060	375.70
26.66	0.3910	375.08
26.66	0.4850	374.59
26.66	0.5930	374.40
26.66	0.6970	374.31
26.66	0.7850	374.38
26.66	0.8710	374.78
26.66	0.9280	375.09
26.66	1.0000	375.63
53.33	0.0000	400.72
53.33	0.1000	398.62
53.33	0.2000	397.00
53.33	0.3060	395.31
53.33	0.3910	394.41
53.33	0.4850	393.74
53.33	0.5930	393.00
53.33	0.6970	392.61
53.33	0.7850	392.44
53.33	0.8710	392.49
53.33	0.9280	392.58
53.33	1.0000	392.70
79.99	0.0000	414.20
79.99	0.1000	411.91
79.99	0.2000	410.07
79.99	0.3060	408.08
79.99	0.3910	406.98
79.99	0.4850	406.09
79.99	0.5930	405.12
79.99	0.6970	404.48
79.99	0.7850	404.14
79.99	0.8710	403.98
79.99	0.9280	403.96
79.99	1.0000	403.80
101.32	0.0000	422.59
101.32	0.1000	420.18
101.32	0.2000	418.16
101.32	0.3060	415.97
101.32	0.3910	414.80
101.32	0.4850	413.44
101.32	0.5930	412.60
101.32	0.6970	411.87
101.32	0.7850	411.37
101.32	0.8710	411.10
101.32	0.9280	410.98
101.32	1.0000	410.86

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	421.55
0.0089	421.35
0.0252	420.85
0.0265	420.75
0.0752	419.65
0.1860	417.35
0.3240	415.25
0.3560	414.85
0.3760	414.65
0.4040	414.35
0.4460	413.85
0.4980	413.35
0.5580	412.85
0.6240	412.35
0.7350	411.75
0.7600	411.65
0.7770	411.55
0.8001	411.45
0.8090	411.40
0.8440	411.30
0.9000	411.15
0.9822	410.95
1.0000	410.95

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of 1-Pentanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
26.66	0.0000	380.05
26.66	0.1000	378.25
26.66	0.2000	376.97
26.66	0.3060	375.70
26.66	0.3910	375.08
26.66	0.4850	374.59
26.66	0.5930	374.40
26.66	0.6970	374.31
26.66	0.7850	374.38
26.66	0.8710	374.78
26.66	0.9280	375.09
26.66	1.0000	375.63
53.33	0.0000	400.72
53.33	0.1000	398.62
53.33	0.2000	397.00
53.33	0.3060	395.31
53.33	0.3910	394.41
53.33	0.4850	393.74
53.33	0.5930	393.00
53.33	0.6970	392.61
53.33	0.7850	392.44
53.33	0.8710	392.49
53.33	0.9280	392.58
53.33	1.0000	392.70
79.99	0.0000	414.20
79.99	0.1000	411.91
79.99	0.2000	410.07
79.99	0.3060	408.08
79.99	0.3910	406.98
79.99	0.4850	406.09
79.99	0.5930	405.12
79.99	0.6970	404.48
79.99	0.7850	404.14
79.99	0.8710	403.98
79.99	0.9280	403.96
79.99	1.0000	403.80
101.32	0.0000	422.59
101.32	0.1000	420.18
101.32	0.2000	418.16
101.32	0.3060	415.97
101.32	0.3910	414.80
101.32	0.4850	413.44
101.32	0.5930	412.60
101.32	0.6970	411.87
101.32	0.7850	411.37
101.32	0.8710	411.10
101.32	0.9280	410.98
101.32	1.0000	410.86

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	421.55
0.0089	421.35
0.0252	420.85
0.0265	420.75
0.0752	419.65
0.1860	417.35
0.3240	415.25
0.3560	414.85
0.3760	414.65
0.4040	414.35
0.4460	413.85
0.4980	413.35
0.5580	412.85
0.6240	412.35
0.7350	411.75
0.7600	411.65
0.7770	411.55
0.8001	411.45
0.8090	411.40
0.8440	411.30
0.9000	411.15
0.9822	410.95
1.0000	410.95

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
26.66	374.30
53.33	392.40

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
26.66	374.30
53.33	392.40

Sources

• Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
• Isobaric Vapor-Liquid Equilibrium for Binary Mixtures of 3-Methyl-1-butanol + 3-Methyl-1-butyl Ethanoate and 1-Pentanol + Pentyl Ethanoate at 101.3 kPa