Mixture of 3-Heptanone + Decane

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 Decane (2) [ref]

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Decane (2) - Liquid
40.00	0.0200

Mole fraction of Decane (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Decane (2) - Liquid	Mole fraction of Decane (2) - Gas
1.0000	1.0000
0.9890	0.9590
0.9420	0.8060
0.9110	0.7390
0.8970	0.6890
0.8850	0.6590
0.8440	0.5940
0.8400	0.5730
0.8090	0.5090
0.8020	0.5220
0.7920	0.5160
0.7850	0.4940
0.7620	0.4480
0.7530	0.4550
0.7190	0.4290
0.6780	0.4060
0.6780	0.3880
0.6520	0.3850
0.6310	0.3590
0.6060	0.3300
0.6050	0.3350
0.5940	0.3350
0.5900	0.3380
0.5260	0.2740
0.4470	0.2330
0.3850	0.2060
0.3180	0.1770
0.2700	0.1710
0.2530	0.1530
0.2240	0.1400
0.2080	0.1340
0.1670	0.1090
0.1360	0.0930
0.1210	0.0780
0.0690	0.0520
0.0580	0.0430
0.0250	0.0280
0.0000	0.0000

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

Pressure, kPa - Liquid	Azeotropic composition: mole fraction of Decane (2) - Liquid
40.00	0.0200

Mole fraction of Decane (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Decane (2) - Liquid	Mole fraction of Decane (2) - Gas
1.0000	1.0000
0.9890	0.9590
0.9420	0.8060
0.9110	0.7390
0.8970	0.6890
0.8850	0.6590
0.8440	0.5940
0.8400	0.5730
0.8090	0.5090
0.8020	0.5220
0.7920	0.5160
0.7850	0.4940
0.7620	0.4480
0.7530	0.4550
0.7190	0.4290
0.6780	0.4060
0.6780	0.3880
0.6520	0.3850
0.6310	0.3590
0.6060	0.3300
0.6050	0.3350
0.5940	0.3350
0.5900	0.3380
0.5260	0.2740
0.4470	0.2330
0.3850	0.2060
0.3180	0.1770
0.2700	0.1710
0.2530	0.1530
0.2240	0.1400
0.2080	0.1340
0.1670	0.1090
0.1360	0.0930
0.1210	0.0780
0.0690	0.0520
0.0580	0.0430
0.0250	0.0280
0.0000	0.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Decane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	413.88
0.9890	413.40
0.9420	410.11
0.9110	408.41
0.8970	407.06
0.8850	406.83
0.8440	404.85
0.8400	404.40
0.8090	403.22
0.8020	402.87
0.7920	402.59
0.7850	402.20
0.7620	401.36
0.7530	400.88
0.7190	399.83
0.6780	398.57
0.6780	398.14
0.6520	397.83
0.6310	397.29
0.6060	396.53
0.6050	396.68
0.5940	396.26
0.5900	396.15
0.5260	394.90
0.4470	393.48
0.3850	392.69
0.3180	391.60
0.2700	391.15
0.2530	390.93
0.2240	390.57
0.2080	390.38
0.1670	389.80
0.1360	389.54
0.1210	389.40
0.0690	389.05
0.0580	388.77
0.0250	388.93
0.0000	388.67

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of Decane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	413.88
0.9890	413.40
0.9420	410.11
0.9110	408.41
0.8970	407.06
0.8850	406.83
0.8440	404.85
0.8400	404.40
0.8090	403.22
0.8020	402.87
0.7920	402.59
0.7850	402.20
0.7620	401.36
0.7530	400.88
0.7190	399.83
0.6780	398.57
0.6780	398.14
0.6520	397.83
0.6310	397.29
0.6060	396.53
0.6050	396.68
0.5940	396.26
0.5900	396.15
0.5260	394.90
0.4470	393.48
0.3850	392.69
0.3180	391.60
0.2700	391.15
0.2530	390.93
0.2240	390.57
0.2080	390.38
0.1670	389.80
0.1360	389.54
0.1210	389.40
0.0690	389.05
0.0580	388.77
0.0250	388.93
0.0000	388.67

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
40.00	388.60

Azeotropic temperature, K [ref]

Pressure, kPa - Liquid	Azeotropic temperature, K - Liquid
40.00	388.60

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