Mixture of 4-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	0.3400

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
0.9590	0.8970
0.9510	0.8920
0.9270	0.8640
0.9040	0.8150
0.8820	0.7810
0.8360	0.7220
0.8330	0.7220
0.8000	0.6930
0.7640	0.6470
0.7620	0.6480
0.7100	0.5940
0.6960	0.5830
0.6480	0.5430
0.6290	0.5300
0.6040	0.5190
0.5700	0.4980
0.5540	0.4860
0.5370	0.4730
0.5010	0.4410
0.4410	0.4090
0.4040	0.3810
0.3550	0.3490
0.3190	0.3250
0.3100	0.3170
0.2640	0.2850
0.2340	0.2650
0.2270	0.2520
0.2060	0.2320
0.1760	0.2080
0.1650	0.1990
0.1410	0.1740
0.1290	0.1620
0.1130	0.1460
0.0940	0.1230
0.0790	0.1030
0.0570	0.0800
0.0380	0.0530
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	0.3400

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
0.9590	0.8970
0.9510	0.8920
0.9270	0.8640
0.9040	0.8150
0.8820	0.7810
0.8360	0.7220
0.8330	0.7220
0.8000	0.6930
0.7640	0.6470
0.7620	0.6480
0.7100	0.5940
0.6960	0.5830
0.6480	0.5430
0.6290	0.5300
0.6040	0.5190
0.5700	0.4980
0.5540	0.4860
0.5370	0.4730
0.5010	0.4410
0.4410	0.4090
0.4040	0.3810
0.3550	0.3490
0.3190	0.3250
0.3100	0.3170
0.2640	0.2850
0.2340	0.2650
0.2270	0.2520
0.2060	0.2320
0.1760	0.2080
0.1650	0.1990
0.1410	0.1740
0.1290	0.1620
0.1130	0.1460
0.0940	0.1230
0.0790	0.1030
0.0570	0.0800
0.0380	0.0530
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	391.90
0.9590	390.84
0.9510	390.31
0.9270	389.71
0.9040	389.03
0.8820	388.63
0.8360	387.61
0.8330	387.60
0.8000	387.14
0.7640	386.59
0.7620	386.37
0.7100	385.92
0.6960	385.63
0.6480	385.26
0.6290	385.01
0.6040	384.91
0.5700	384.60
0.5540	384.52
0.5370	384.45
0.5010	384.26
0.4410	383.97
0.4040	383.93
0.3550	383.82
0.3190	383.83
0.3100	383.77
0.2640	383.85
0.2340	383.79
0.2270	383.88
0.2060	384.00
0.1760	384.05
0.1650	384.15
0.1410	384.42
0.1290	384.35
0.1130	384.54
0.0940	384.77
0.0790	384.91
0.0570	385.08
0.0380	385.28
0.0000	385.47

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	391.90
0.9590	390.84
0.9510	390.31
0.9270	389.71
0.9040	389.03
0.8820	388.63
0.8360	387.61
0.8330	387.60
0.8000	387.14
0.7640	386.59
0.7620	386.37
0.7100	385.92
0.6960	385.63
0.6480	385.26
0.6290	385.01
0.6040	384.91
0.5700	384.60
0.5540	384.52
0.5370	384.45
0.5010	384.26
0.4410	383.97
0.4040	383.93
0.3550	383.82
0.3190	383.83
0.3100	383.77
0.2640	383.85
0.2340	383.79
0.2270	383.88
0.2060	384.00
0.1760	384.05
0.1650	384.15
0.1410	384.42
0.1290	384.35
0.1130	384.54
0.0940	384.77
0.0790	384.91
0.0570	385.08
0.0380	385.28
0.0000	385.47

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
40.00	383.80

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
40.00	383.80

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