Mixture of n-Hexane + Butane, 2-methoxy-2-methyl-

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. Interfacial tension, N/m (2)
5. ρ_l - Mass density, kg/m3 (4)
6. c_sound,fluid - Speed of Sound, m/s (2)
7. γ - Surface tension liquid-gas, N/m (2)
8. Excess molar volume, m3/mol (2)

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Pressure, kPa - Gas	Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid
50.00	321.03	1.0000
50.00	321.61	0.9410
50.00	322.21	0.8860
50.00	322.81	0.8320
50.00	323.38	0.7810
50.00	323.94	0.7320
50.00	324.59	0.6800
50.00	325.25	0.6290
50.00	325.94	0.5780
50.00	326.66	0.5290
50.00	327.44	0.4780
50.00	328.26	0.4260
50.00	328.98	0.3830
50.00	329.84	0.3330
50.00	330.69	0.2880
50.00	331.60	0.2410
50.00	332.64	0.1920
50.00	333.66	0.1490
50.00	334.79	0.1030
50.00	336.07	0.0530
50.00	337.67	0.0000
75.00	332.65	1.0000
75.00	333.23	0.9400
75.00	333.87	0.8850
75.00	334.49	0.8310
75.00	335.08	0.7810
75.00	335.68	0.7330
75.00	336.36	0.6790
75.00	337.05	0.6290
75.00	337.77	0.5780
75.00	338.53	0.5300
75.00	339.33	0.4760
75.00	340.18	0.4240
75.00	340.91	0.3820
75.00	341.82	0.3320
75.00	342.70	0.2870
75.00	343.65	0.2400
75.00	344.71	0.1920
75.00	345.72	0.1490
75.00	346.90	0.1030
75.00	348.15	0.0540
75.00	349.76	0.0000
94.00	339.58	1.0000
94.00	340.13	0.9400
94.00	340.79	0.8850
94.00	341.44	0.8300
94.00	342.05	0.7800
94.00	342.66	0.7320
94.00	343.37	0.6770
94.00	344.06	0.6260
94.00	344.81	0.5760
94.00	345.57	0.5260
94.00	346.39	0.4750
94.00	347.27	0.4230
94.00	348.02	0.3800
94.00	348.94	0.3310
94.00	349.84	0.2870
94.00	350.83	0.2400
94.00	351.88	0.1910
94.00	352.88	0.1490
94.00	354.07	0.1030
94.00	355.34	0.0540
94.00	356.96	0.0000

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Pressure, kPa - Gas	Temperature, K - Gas	Mole fraction of n-Hexane (1) - Gas
50.00	321.03	1.0000
50.00	321.61	0.9620
50.00	322.21	0.9270
50.00	322.81	0.8920
50.00	323.38	0.8580
50.00	323.94	0.8270
50.00	324.59	0.7890
50.00	325.25	0.7530
50.00	325.94	0.7120
50.00	326.66	0.6730
50.00	327.44	0.6260
50.00	328.26	0.5800
50.00	328.98	0.5390
50.00	329.84	0.4900
50.00	330.69	0.4390
50.00	331.60	0.3850
50.00	332.64	0.3220
50.00	333.66	0.2620
50.00	334.79	0.1900
50.00	336.07	0.1050
50.00	337.67	0.0000
75.00	332.65	1.0000
75.00	333.23	0.9610
75.00	333.87	0.9250
75.00	334.49	0.8890
75.00	335.08	0.8550
75.00	335.68	0.8220
75.00	336.36	0.7840
75.00	337.05	0.7470
75.00	337.77	0.7050
75.00	338.53	0.6650
75.00	339.33	0.6190
75.00	340.18	0.5730
75.00	340.91	0.5330
75.00	341.82	0.4810
75.00	342.70	0.4310
75.00	343.65	0.3770
75.00	344.71	0.3150
75.00	345.72	0.2560
75.00	346.90	0.1820
75.00	348.15	0.1030
75.00	349.76	0.0000
94.00	339.58	1.0000
94.00	340.13	0.9600
94.00	340.79	0.9240
94.00	341.44	0.8870
94.00	342.05	0.8530
94.00	342.66	0.8200
94.00	343.37	0.7810
94.00	344.06	0.7430
94.00	344.81	0.7000
94.00	345.57	0.6600
94.00	346.39	0.6150
94.00	347.27	0.5670
94.00	348.02	0.5270
94.00	348.94	0.4760
94.00	349.84	0.4260
94.00	350.83	0.3710
94.00	351.88	0.3090
94.00	352.88	0.2510
94.00	354.07	0.1790
94.00	355.34	0.1010
94.00	356.96	0.0000

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Pressure, kPa - Gas	Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Liquid
50.00	321.03	1.0000
50.00	321.61	0.9410
50.00	322.21	0.8860
50.00	322.81	0.8320
50.00	323.38	0.7810
50.00	323.94	0.7320
50.00	324.59	0.6800
50.00	325.25	0.6290
50.00	325.94	0.5780
50.00	326.66	0.5290
50.00	327.44	0.4780
50.00	328.26	0.4260
50.00	328.98	0.3830
50.00	329.84	0.3330
50.00	330.69	0.2880
50.00	331.60	0.2410
50.00	332.64	0.1920
50.00	333.66	0.1490
50.00	334.79	0.1030
50.00	336.07	0.0530
50.00	337.67	0.0000
75.00	332.65	1.0000
75.00	333.23	0.9400
75.00	333.87	0.8850
75.00	334.49	0.8310
75.00	335.08	0.7810
75.00	335.68	0.7330
75.00	336.36	0.6790
75.00	337.05	0.6290
75.00	337.77	0.5780
75.00	338.53	0.5300
75.00	339.33	0.4760
75.00	340.18	0.4240
75.00	340.91	0.3820
75.00	341.82	0.3320
75.00	342.70	0.2870
75.00	343.65	0.2400
75.00	344.71	0.1920
75.00	345.72	0.1490
75.00	346.90	0.1030
75.00	348.15	0.0540
75.00	349.76	0.0000
94.00	339.58	1.0000
94.00	340.13	0.9400
94.00	340.79	0.8850
94.00	341.44	0.8300
94.00	342.05	0.7800
94.00	342.66	0.7320
94.00	343.37	0.6770
94.00	344.06	0.6260
94.00	344.81	0.5760
94.00	345.57	0.5260
94.00	346.39	0.4750
94.00	347.27	0.4230
94.00	348.02	0.3800
94.00	348.94	0.3310
94.00	349.84	0.2870
94.00	350.83	0.2400
94.00	351.88	0.1910
94.00	352.88	0.1490
94.00	354.07	0.1030
94.00	355.34	0.0540
94.00	356.96	0.0000

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Pressure, kPa - Gas	Temperature, K - Gas	Mole fraction of n-Hexane (1) - Gas
50.00	321.03	1.0000
50.00	321.61	0.9620
50.00	322.21	0.9270
50.00	322.81	0.8920
50.00	323.38	0.8580
50.00	323.94	0.8270
50.00	324.59	0.7890
50.00	325.25	0.7530
50.00	325.94	0.7120
50.00	326.66	0.6730
50.00	327.44	0.6260
50.00	328.26	0.5800
50.00	328.98	0.5390
50.00	329.84	0.4900
50.00	330.69	0.4390
50.00	331.60	0.3850
50.00	332.64	0.3220
50.00	333.66	0.2620
50.00	334.79	0.1900
50.00	336.07	0.1050
50.00	337.67	0.0000
75.00	332.65	1.0000
75.00	333.23	0.9610
75.00	333.87	0.9250
75.00	334.49	0.8890
75.00	335.08	0.8550
75.00	335.68	0.8220
75.00	336.36	0.7840
75.00	337.05	0.7470
75.00	337.77	0.7050
75.00	338.53	0.6650
75.00	339.33	0.6190
75.00	340.18	0.5730
75.00	340.91	0.5330
75.00	341.82	0.4810
75.00	342.70	0.4310
75.00	343.65	0.3770
75.00	344.71	0.3150
75.00	345.72	0.2560
75.00	346.90	0.1820
75.00	348.15	0.1030
75.00	349.76	0.0000
94.00	339.58	1.0000
94.00	340.13	0.9600
94.00	340.79	0.9240
94.00	341.44	0.8870
94.00	342.05	0.8530
94.00	342.66	0.8200
94.00	343.37	0.7810
94.00	344.06	0.7430
94.00	344.81	0.7000
94.00	345.57	0.6600
94.00	346.39	0.6150
94.00	347.27	0.5670
94.00	348.02	0.5270
94.00	348.94	0.4760
94.00	349.84	0.4260
94.00	350.83	0.3710
94.00	351.88	0.3090
94.00	352.88	0.2510
94.00	354.07	0.1790
94.00	355.34	0.1010
94.00	356.96	0.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0003
298.15	0.1632	0.0003
298.15	0.2584	0.0003
298.15	0.3742	0.0003
298.15	0.4276	0.0003
298.15	0.5464	0.0003
298.15	0.6121	0.0004
298.15	0.7457	0.0004
298.15	0.8625	0.0004
298.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.1632	0.0003
308.15	0.2584	0.0003
308.15	0.3742	0.0003
308.15	0.4276	0.0003
308.15	0.5464	0.0003
308.15	0.6121	0.0003
308.15	0.7457	0.0003
308.15	0.8625	0.0004
308.15	1.0000	0.0004
318.15	0.0000	0.0002
318.15	0.1632	0.0002
318.15	0.2584	0.0003
318.15	0.3742	0.0003
318.15	0.4276	0.0003
318.15	0.5464	0.0003
318.15	0.6121	0.0003
318.15	0.7457	0.0003
318.15	0.8625	0.0003
318.15	1.0000	0.0004
323.15	0.0000	0.0002
323.15	0.1632	0.0002
323.15	0.2584	0.0002
323.15	0.3742	0.0003
323.15	0.4276	0.0003
323.15	0.5464	0.0003
323.15	0.6121	0.0003
323.15	0.7457	0.0003
323.15	0.8625	0.0003
323.15	1.0000	0.0003
328.15	0.0000	0.0002
328.15	0.1632	0.0002
328.15	0.2584	0.0002
328.15	0.3742	0.0002
328.15	0.4276	0.0002
328.15	0.5464	0.0003
328.15	0.6121	0.0003
328.15	0.7457	0.0003
328.15	0.8625	0.0003
328.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0003
298.15	0.1632	0.0003
298.15	0.2584	0.0003
298.15	0.3742	0.0003
298.15	0.4276	0.0003
298.15	0.5464	0.0003
298.15	0.6121	0.0004
298.15	0.7457	0.0004
298.15	0.8625	0.0004
298.15	1.0000	0.0004
308.15	0.0000	0.0003
308.15	0.1632	0.0003
308.15	0.2584	0.0003
308.15	0.3742	0.0003
308.15	0.4276	0.0003
308.15	0.5464	0.0003
308.15	0.6121	0.0003
308.15	0.7457	0.0003
308.15	0.8625	0.0004
308.15	1.0000	0.0004
318.15	0.0000	0.0002
318.15	0.1632	0.0002
318.15	0.2584	0.0003
318.15	0.3742	0.0003
318.15	0.4276	0.0003
318.15	0.5464	0.0003
318.15	0.6121	0.0003
318.15	0.7457	0.0003
318.15	0.8625	0.0003
318.15	1.0000	0.0004
323.15	0.0000	0.0002
323.15	0.1632	0.0002
323.15	0.2584	0.0002
323.15	0.3742	0.0003
323.15	0.4276	0.0003
323.15	0.5464	0.0003
323.15	0.6121	0.0003
323.15	0.7457	0.0003
323.15	0.8625	0.0003
323.15	1.0000	0.0003
328.15	0.0000	0.0002
328.15	0.1632	0.0002
328.15	0.2584	0.0002
328.15	0.3742	0.0002
328.15	0.4276	0.0002
328.15	0.5464	0.0003
328.15	0.6121	0.0003
328.15	0.7457	0.0003
328.15	0.8625	0.0003
328.15	1.0000	0.0003

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2960	32.98
0.6980	26.12

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2960	32.98
0.6980	26.12

Interfacial tension, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Interfacial tension, N/m - Liquid
0.0000	0.0220
0.0510	0.0216
0.1000	0.0211
0.2090	0.0206
0.3050	0.0201
0.3990	0.0198
0.5060	0.0191
0.6110	0.0187
0.7140	0.0183
0.8130	0.0180
0.9140	0.0177
0.9600	0.0175
1.0000	0.0174

Interfacial tension, N/m [ref]

Operational condition: Temperature, K = 303.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Interfacial tension, N/m - Liquid
0.0000	0.0220
0.0510	0.0216
0.1000	0.0211
0.2090	0.0206
0.3050	0.0201
0.3990	0.0198
0.5060	0.0191
0.6110	0.0187
0.7140	0.0183
0.8130	0.0180
0.9140	0.0177
0.9600	0.0175
1.0000	0.0174

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	765.8
0.0380	761.49
0.0920	755.29
0.1450	749.34
0.1940	743.82
0.2470	737.76
0.3460	726.73
0.4430	715.93
0.4970	709.95
0.5520	703.83
0.5970	698.92
0.6440	693.78
0.6960	688.15
0.7450	682.72
0.7950	677.33
0.8520	671.14
0.9010	665.86
0.9520	660.3
1.0000	655.19

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	654.7
298.15	0.1632	672.8
298.15	0.2584	683.2
298.15	0.3742	695.5
298.15	0.4276	701.6
298.15	0.5464	714.8
298.15	0.6121	722.3
298.15	0.7457	737.2
298.15	0.8625	750.1
298.15	1.0000	765.6
308.15	0.0000	645.4
308.15	0.1632	663.2
308.15	0.2584	673.8
308.15	0.3742	686.5
308.15	0.4276	692.3
308.15	0.5464	705.2
308.15	0.6121	712.5
308.15	0.7457	727.4
308.15	0.8625	740.7
308.15	1.0000	756.3
318.15	0.0000	636.2
318.15	0.1632	653.5
318.15	0.2584	663.8
318.15	0.3742	676.6
318.15	0.4276	682.4
318.15	0.5464	695.3
318.15	0.6121	702.5
318.15	0.7457	717.7
318.15	0.8625	730.6
318.15	1.0000	746.3
323.15	0.0000	631.2
323.15	0.1632	648.6
323.15	0.2584	658.8
323.15	0.3742	671.5
323.15	0.4276	677.3
323.15	0.5464	690.4
323.15	0.6121	697.6
323.15	0.7457	712.5
323.15	0.8625	725.8
323.15	1.0000	741.4
328.15	0.0000	626.4
328.15	0.1632	643.6
328.15	0.2584	653.7
328.15	0.3742	666.5
328.15	0.4276	672.3
328.15	0.5464	685.3
328.15	0.6121	692.6
328.15	0.7457	707.5
328.15	0.8625	720.8
328.15	1.0000	736.5

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	765.8
0.0380	761.49
0.0920	755.29
0.1450	749.34
0.1940	743.82
0.2470	737.76
0.3460	726.73
0.4430	715.93
0.4970	709.95
0.5520	703.83
0.5970	698.92
0.6440	693.78
0.6960	688.15
0.7450	682.72
0.7950	677.33
0.8520	671.14
0.9010	665.86
0.9520	660.3
1.0000	655.19

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	654.7
298.15	0.1632	672.8
298.15	0.2584	683.2
298.15	0.3742	695.5
298.15	0.4276	701.6
298.15	0.5464	714.8
298.15	0.6121	722.3
298.15	0.7457	737.2
298.15	0.8625	750.1
298.15	1.0000	765.6
308.15	0.0000	645.4
308.15	0.1632	663.2
308.15	0.2584	673.8
308.15	0.3742	686.5
308.15	0.4276	692.3
308.15	0.5464	705.2
308.15	0.6121	712.5
308.15	0.7457	727.4
308.15	0.8625	740.7
308.15	1.0000	756.3
318.15	0.0000	636.2
318.15	0.1632	653.5
318.15	0.2584	663.8
318.15	0.3742	676.6
318.15	0.4276	682.4
318.15	0.5464	695.3
318.15	0.6121	702.5
318.15	0.7457	717.7
318.15	0.8625	730.6
318.15	1.0000	746.3
323.15	0.0000	631.2
323.15	0.1632	648.6
323.15	0.2584	658.8
323.15	0.3742	671.5
323.15	0.4276	677.3
323.15	0.5464	690.4
323.15	0.6121	697.6
323.15	0.7457	712.5
323.15	0.8625	725.8
323.15	1.0000	741.4
328.15	0.0000	626.4
328.15	0.1632	643.6
328.15	0.2584	653.7
328.15	0.3742	666.5
328.15	0.4276	672.3
328.15	0.5464	685.3
328.15	0.6121	692.6
328.15	0.7457	707.5
328.15	0.8625	720.8
328.15	1.0000	736.5

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1073.24
298.15	0.1632	1077.82
298.15	0.2584	1082.18
298.15	0.3742	1087.54
298.15	0.4276	1088.6
298.15	0.5464	1092.82
298.15	0.6121	1096.13
298.15	0.7457	1103.52
298.15	0.8625	1112.19
298.15	1.0000	1118.05
308.15	0.0000	1031.24
308.15	0.1632	1035.51
308.15	0.2584	1039.38
308.15	0.3742	1045.13
308.15	0.4276	1046.8
308.15	0.5464	1049.64
308.15	0.6121	1053.15
308.15	0.7457	1060.41
308.15	0.8625	1069.18
308.15	1.0000	1075.6
318.15	0.0000	981.23
318.15	0.1632	984.7
318.15	0.2584	988.75
318.15	0.3742	994.36
318.15	0.4276	996.61
318.15	0.5464	1002.42
318.15	0.6121	1006.78
318.15	0.7457	1013.83
318.15	0.8625	1022.8
318.15	1.0000	1030.24
323.15	0.0000	960.75
323.15	0.1632	963.82
323.15	0.2584	967.24
323.15	0.3742	971.83
323.15	0.4276	973.34
323.15	0.5464	977.27
323.15	0.6121	980.49
323.15	0.7457	984.8
323.15	0.8625	994.84
323.15	1.0000	1003.02
328.15	0.0000	940.35
328.15	0.1632	942.3
328.15	0.2584	945.14
328.15	0.3742	949.52
328.15	0.4276	951.24
328.15	0.5464	955.05
328.15	0.6121	958.72
328.15	0.7457	963.63
328.15	0.8625	974.08
328.15	1.0000	985.22

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1073.24
298.15	0.1632	1077.82
298.15	0.2584	1082.18
298.15	0.3742	1087.54
298.15	0.4276	1088.6
298.15	0.5464	1092.82
298.15	0.6121	1096.13
298.15	0.7457	1103.52
298.15	0.8625	1112.19
298.15	1.0000	1118.05
308.15	0.0000	1031.24
308.15	0.1632	1035.51
308.15	0.2584	1039.38
308.15	0.3742	1045.13
308.15	0.4276	1046.8
308.15	0.5464	1049.64
308.15	0.6121	1053.15
308.15	0.7457	1060.41
308.15	0.8625	1069.18
308.15	1.0000	1075.6
318.15	0.0000	981.23
318.15	0.1632	984.7
318.15	0.2584	988.75
318.15	0.3742	994.36
318.15	0.4276	996.61
318.15	0.5464	1002.42
318.15	0.6121	1006.78
318.15	0.7457	1013.83
318.15	0.8625	1022.8
318.15	1.0000	1030.24
323.15	0.0000	960.75
323.15	0.1632	963.82
323.15	0.2584	967.24
323.15	0.3742	971.83
323.15	0.4276	973.34
323.15	0.5464	977.27
323.15	0.6121	980.49
323.15	0.7457	984.8
323.15	0.8625	994.84
323.15	1.0000	1003.02
328.15	0.0000	940.35
328.15	0.1632	942.3
328.15	0.2584	945.14
328.15	0.3742	949.52
328.15	0.4276	951.24
328.15	0.5464	955.05
328.15	0.6121	958.72
328.15	0.7457	963.63
328.15	0.8625	974.08
328.15	1.0000	985.22

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0177
298.15	0.1632	0.0180
298.15	0.2584	0.0182
298.15	0.3742	0.0185
298.15	0.4276	0.0186
298.15	0.5464	0.0187
298.15	0.6121	0.0189
298.15	0.7457	0.0192
298.15	0.8625	0.0194
298.15	1.0000	0.0197
308.15	0.0000	0.0166
308.15	0.1632	0.0169
308.15	0.2584	0.0171
308.15	0.3742	0.0174
308.15	0.4276	0.0175
308.15	0.5464	0.0176
308.15	0.6121	0.0178
308.15	0.7457	0.0181
308.15	0.8625	0.0184
308.15	1.0000	0.0187
318.15	0.0000	0.0155
318.15	0.1632	0.0158
318.15	0.2584	0.0160
318.15	0.3742	0.0163
318.15	0.4276	0.0165
318.15	0.5464	0.0166
318.15	0.6121	0.0167
318.15	0.7457	0.0170
318.15	0.8625	0.0173
318.15	1.0000	0.0176
323.15	0.0000	0.0150
323.15	0.1632	0.0152
323.15	0.2584	0.0155
323.15	0.3742	0.0158
323.15	0.4276	0.0159
323.15	0.5464	0.0160
323.15	0.6121	0.0162
323.15	0.7457	0.0165
323.15	0.8625	0.0168
323.15	1.0000	0.0171
328.15	0.0000	0.0144
328.15	0.1632	0.0147
328.15	0.2584	0.0149
328.15	0.3742	0.0152
328.15	0.4276	0.0154
328.15	0.5464	0.0155
328.15	0.6121	0.0157
328.15	0.7457	0.0160
328.15	0.8625	0.0163
328.15	1.0000	0.0166

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 2-methoxy-2-methyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0177
298.15	0.1632	0.0180
298.15	0.2584	0.0182
298.15	0.3742	0.0185
298.15	0.4276	0.0186
298.15	0.5464	0.0187
298.15	0.6121	0.0189
298.15	0.7457	0.0192
298.15	0.8625	0.0194
298.15	1.0000	0.0197
308.15	0.0000	0.0166
308.15	0.1632	0.0169
308.15	0.2584	0.0171
308.15	0.3742	0.0174
308.15	0.4276	0.0175
308.15	0.5464	0.0176
308.15	0.6121	0.0178
308.15	0.7457	0.0181
308.15	0.8625	0.0184
308.15	1.0000	0.0187
318.15	0.0000	0.0155
318.15	0.1632	0.0158
318.15	0.2584	0.0160
318.15	0.3742	0.0163
318.15	0.4276	0.0165
318.15	0.5464	0.0166
318.15	0.6121	0.0167
318.15	0.7457	0.0170
318.15	0.8625	0.0173
318.15	1.0000	0.0176
323.15	0.0000	0.0150
323.15	0.1632	0.0152
323.15	0.2584	0.0155
323.15	0.3742	0.0158
323.15	0.4276	0.0159
323.15	0.5464	0.0160
323.15	0.6121	0.0162
323.15	0.7457	0.0165
323.15	0.8625	0.0168
323.15	1.0000	0.0171
328.15	0.0000	0.0144
328.15	0.1632	0.0147
328.15	0.2584	0.0149
328.15	0.3742	0.0152
328.15	0.4276	0.0154
328.15	0.5464	0.0155
328.15	0.6121	0.0157
328.15	0.7457	0.0160
328.15	0.8625	0.0163
328.15	1.0000	0.0166

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0000	0.0000
0.0380	3.1000e-08
0.0920	7.7000e-08
0.1450	1.1600e-07
0.1940	1.3800e-07
0.2470	1.8000e-07
0.3460	2.1300e-07
0.4430	2.3400e-07
0.4970	2.3900e-07
0.5520	2.3400e-07
0.5970	2.2800e-07
0.6440	2.1900e-07
0.6960	2.0200e-07
0.7450	1.9000e-07
0.7950	1.5300e-07
0.8520	1.1900e-07
0.9010	8.3000e-08
0.9520	5.3000e-08
1.0000	0.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0000	0.0000
0.0380	3.1000e-08
0.0920	7.7000e-08
0.1450	1.1600e-07
0.1940	1.3800e-07
0.2470	1.8000e-07
0.3460	2.1300e-07
0.4430	2.3400e-07
0.4970	2.3900e-07
0.5520	2.3400e-07
0.5970	2.2800e-07
0.6440	2.1900e-07
0.6960	2.0200e-07
0.7450	1.9000e-07
0.7950	1.5300e-07
0.8520	1.1900e-07
0.9010	8.3000e-08
0.9520	5.3000e-08
1.0000	0.0000

Sources

• Vapour liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K
• Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
• Thermophysical Study of Binary Systems of tert-Amyl Methyl Ether with n-Hexane and m-Xylene