Mixture of 3-Heptanone + Nonane

Datasets

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

Azeotropic composition: mole fraction of Nonane (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Nonane (2) - Liquid
40.00	0.4400

Mole fraction of Nonane (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Nonane (2) - Liquid	Mole fraction of Nonane (2) - Gas
1.0000	1.0000
0.9570	0.9240
0.9410	0.8890
0.9200	0.8560
0.8890	0.8120
0.8830	0.8050
0.8560	0.7690
0.8510	0.7680
0.8120	0.7260
0.8040	0.7100
0.7760	0.6840
0.7450	0.6550
0.6430	0.5700
0.6000	0.5440
0.5760	0.5290
0.5330	0.5050
0.5110	0.4900
0.4840	0.4700
0.4590	0.4550
0.4270	0.4320
0.3470	0.3750
0.2860	0.3290
0.2480	0.3060
0.2240	0.2790
0.2200	0.2780
0.1890	0.2500
0.1730	0.2350
0.1650	0.2240
0.1390	0.1970
0.1140	0.1680
0.1010	0.1510
0.0750	0.1160
0.0490	0.0900
0.0000	0.0000

Azeotropic composition: mole fraction of Nonane (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Nonane (2) - Liquid
40.00	0.4400

Mole fraction of Nonane (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Nonane (2) - Liquid	Mole fraction of Nonane (2) - Gas
1.0000	1.0000
0.9570	0.9240
0.9410	0.8890
0.9200	0.8560
0.8890	0.8120
0.8830	0.8050
0.8560	0.7690
0.8510	0.7680
0.8120	0.7260
0.8040	0.7100
0.7760	0.6840
0.7450	0.6550
0.6430	0.5700
0.6000	0.5440
0.5760	0.5290
0.5330	0.5050
0.5110	0.4900
0.4840	0.4700
0.4590	0.4550
0.4270	0.4320
0.3470	0.3750
0.2860	0.3290
0.2480	0.3060
0.2240	0.2790
0.2200	0.2780
0.1890	0.2500
0.1730	0.2350
0.1650	0.2240
0.1390	0.1970
0.1140	0.1680
0.1010	0.1510
0.0750	0.1160
0.0490	0.0900
0.0000	0.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Nonane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	391.87
0.9570	390.66
0.9410	390.37
0.9200	389.71
0.8890	389.11
0.8830	389.09
0.8560	388.55
0.8510	388.49
0.8120	387.93
0.8040	387.76
0.7760	387.54
0.7450	387.13
0.6430	386.29
0.6000	386.25
0.5760	386.15
0.5330	386.02
0.5110	385.88
0.4840	385.87
0.4590	385.85
0.4270	385.72
0.3470	385.79
0.2860	386.07
0.2480	386.10
0.2240	386.33
0.2200	386.20
0.1890	386.43
0.1730	386.59
0.1650	386.57
0.1390	386.82
0.1140	387.25
0.1010	387.29
0.0750	387.48
0.0490	387.72
0.0000	388.36

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Nonane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	391.87
0.9570	390.66
0.9410	390.37
0.9200	389.71
0.8890	389.11
0.8830	389.09
0.8560	388.55
0.8510	388.49
0.8120	387.93
0.8040	387.76
0.7760	387.54
0.7450	387.13
0.6430	386.29
0.6000	386.25
0.5760	386.15
0.5330	386.02
0.5110	385.88
0.4840	385.87
0.4590	385.85
0.4270	385.72
0.3470	385.79
0.2860	386.07
0.2480	386.10
0.2240	386.33
0.2200	386.20
0.1890	386.43
0.1730	386.59
0.1650	386.57
0.1390	386.82
0.1140	387.25
0.1010	387.29
0.0750	387.48
0.0490	387.72
0.0000	388.36

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
40.00	385.70

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
40.00	385.70

Sources

• Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane