Mixture of Ethanol + 2-Methyl-1-butanol

Datasets

1. Mole fraction (6)
2. ν - Kinematic viscosity, m2/s (2)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (4)
5. c_sound,fluid - Speed of Sound, m/s (2)
6. γ - Surface tension liquid-gas, N/m (2)
7. T_boil - Boiling temperature at pressure P, K (4)

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 332.95 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0098	0.1165
0.0300	0.2580
0.0511	0.3693
0.0722	0.4519
0.0998	0.5368
0.1396	0.6340
0.1907	0.7150
0.2303	0.7565
0.2696	0.7913
0.3486	0.8405
0.3903	0.8606
0.4298	0.8777
0.4787	0.8948
0.5292	0.9121
0.6286	0.9399
0.7306	0.9592
0.7800	0.9675
0.8301	0.9754
0.8806	0.9829
0.9296	0.9896
0.9806	0.9971

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	33.30	0.0000
0.0000	66.60	0.0000
0.0000	101.30	0.0000
0.0630	66.60	0.3120
0.0650	101.30	0.3080
0.0760	33.30	0.3930
0.0760	66.60	0.3590
0.1250	33.30	0.5410
0.1260	101.30	0.4860
0.1820	66.60	0.6170
0.1920	101.30	0.6150
0.2240	66.60	0.6790
0.2240	101.30	0.6610
0.2420	101.30	0.6850
0.2460	33.30	0.7480
0.2790	66.60	0.7430
0.2940	33.30	0.7980
0.3110	101.30	0.7560
0.3360	33.30	0.8280
0.3840	33.30	0.8580
0.3940	66.60	0.8350
0.3950	101.30	0.8170
0.4220	33.30	0.8780
0.4380	66.60	0.8600
0.4770	66.60	0.8780
0.4780	101.30	0.8650
0.4880	33.30	0.9070
0.5410	66.60	0.9040
0.5510	101.30	0.8960
0.5620	33.30	0.9310
0.6060	101.30	0.9160
0.6280	66.60	0.9330
0.6430	33.30	0.9510
0.7330	66.60	0.9580
0.7520	101.30	0.9550
0.7740	33.30	0.9740
0.8810	101.30	0.9810
0.8850	66.60	0.9850
0.8870	33.30	0.9880
0.9070	33.30	0.9900
0.9080	101.30	0.9860
0.9100	66.60	0.9890
1.0000	33.30	1.0000
1.0000	66.60	1.0000
1.0000	101.30	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.0210	0.1180
0.0620	0.2860
0.1020	0.4050
0.1410	0.4880
0.1750	0.5590
0.2160	0.6240
0.2740	0.6920
0.3280	0.7550
0.3850	0.7950
0.4160	0.8170
0.4460	0.8370
0.4760	0.8520
0.5160	0.8710
0.5500	0.8870
0.5800	0.8980
0.6950	0.9370
0.8170	0.9670
0.9220	0.9870
0.9720	0.9970
0.9930	0.9990
1.0000	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Temperature, K = 332.95 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0098	0.1165
0.0300	0.2580
0.0511	0.3693
0.0722	0.4519
0.0998	0.5368
0.1396	0.6340
0.1907	0.7150
0.2303	0.7565
0.2696	0.7913
0.3486	0.8405
0.3903	0.8606
0.4298	0.8777
0.4787	0.8948
0.5292	0.9121
0.6286	0.9399
0.7306	0.9592
0.7800	0.9675
0.8301	0.9754
0.8806	0.9829
0.9296	0.9896
0.9806	0.9971

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	33.30	0.0000
0.0000	66.60	0.0000
0.0000	101.30	0.0000
0.0630	66.60	0.3120
0.0650	101.30	0.3080
0.0760	33.30	0.3930
0.0760	66.60	0.3590
0.1250	33.30	0.5410
0.1260	101.30	0.4860
0.1820	66.60	0.6170
0.1920	101.30	0.6150
0.2240	66.60	0.6790
0.2240	101.30	0.6610
0.2420	101.30	0.6850
0.2460	33.30	0.7480
0.2790	66.60	0.7430
0.2940	33.30	0.7980
0.3110	101.30	0.7560
0.3360	33.30	0.8280
0.3840	33.30	0.8580
0.3940	66.60	0.8350
0.3950	101.30	0.8170
0.4220	33.30	0.8780
0.4380	66.60	0.8600
0.4770	66.60	0.8780
0.4780	101.30	0.8650
0.4880	33.30	0.9070
0.5410	66.60	0.9040
0.5510	101.30	0.8960
0.5620	33.30	0.9310
0.6060	101.30	0.9160
0.6280	66.60	0.9330
0.6430	33.30	0.9510
0.7330	66.60	0.9580
0.7520	101.30	0.9550
0.7740	33.30	0.9740
0.8810	101.30	0.9810
0.8850	66.60	0.9850
0.8870	33.30	0.9880
0.9070	33.30	0.9900
0.9080	101.30	0.9860
0.9100	66.60	0.9890
1.0000	33.30	1.0000
1.0000	66.60	1.0000
1.0000	101.30	1.0000

Mole fraction of Ethanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Ethanol (1) - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	0.0000
0.0210	0.1180
0.0620	0.2860
0.1020	0.4050
0.1410	0.4880
0.1750	0.5590
0.2160	0.6240
0.2740	0.6920
0.3280	0.7550
0.3850	0.7950
0.4160	0.8170
0.4460	0.8370
0.4760	0.8520
0.5160	0.8710
0.5500	0.8870
0.5800	0.8980
0.6950	0.9370
0.8170	0.9670
0.9220	0.9870
0.9720	0.9970
0.9930	0.9990
1.0000	1.0000

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 2-Methyl-1-butanol (2) - Liquid	Temperature, K - Liquid	Kinematic viscosity, m2/s - Liquid
0.0000	293.15	1.5248e-06
0.0000	298.15	1.3895e-06
0.0000	303.15	1.2261e-06
0.0000	308.15	1.1278e-06
0.0000	313.15	1.0250e-06
0.0000	318.15	9.3990e-07
0.0000	323.15	8.2820e-07
0.0915	293.15	1.6616e-06
0.0915	298.15	1.5003e-06
0.0915	303.15	1.3164e-06
0.0915	308.15	1.1983e-06
0.0915	313.15	1.0785e-06
0.0915	318.15	9.7970e-07
0.0915	323.15	8.5860e-07
0.1753	293.15	1.7965e-06
0.1753	298.15	1.6110e-06
0.1753	303.15	1.4077e-06
0.1753	308.15	1.2717e-06
0.1753	313.15	1.1367e-06
0.1753	318.15	1.0251e-06
0.1753	323.15	8.9580e-07
0.2524	293.15	1.9181e-06
0.2524	298.15	1.7130e-06
0.2524	303.15	1.4954e-06
0.2524	308.15	1.3437e-06
0.2524	313.15	1.1960e-06
0.2524	318.15	1.0735e-06
0.2524	323.15	9.3680e-07
0.3235	293.15	2.0393e-06
0.3235	298.15	1.8161e-06
0.3235	303.15	1.5851e-06
0.3235	308.15	1.4194e-06
0.3235	313.15	1.2589e-06
0.3235	318.15	1.1264e-06
0.3235	323.15	9.8330e-07
0.3894	293.15	2.1715e-06
0.3894	298.15	1.9295e-06
0.3894	303.15	1.6846e-06
0.3894	308.15	1.5037e-06
0.3894	313.15	1.3306e-06
0.3894	318.15	1.1865e-06
0.3894	323.15	1.0363e-06
0.4505	293.15	2.3219e-06
0.4505	298.15	2.0592e-06
0.4505	303.15	1.7984e-06
0.4505	308.15	1.5994e-06
0.4505	313.15	1.4108e-06
0.4505	318.15	1.2547e-06
0.4505	323.15	1.0957e-06
0.5605	293.15	2.6732e-06
0.5605	298.15	2.3576e-06
0.5605	303.15	2.0569e-06
0.5605	308.15	1.8187e-06
0.5605	313.15	1.5954e-06
0.5605	318.15	1.4116e-06
0.5605	323.15	1.2327e-06
0.6567	293.15	3.0617e-06
0.6567	298.15	2.6912e-06
0.6567	303.15	2.3483e-06
0.6567	308.15	2.0654e-06
0.6567	313.15	1.8039e-06
0.6567	318.15	1.5898e-06
0.6567	323.15	1.3881e-06
0.7416	293.15	3.4735e-06
0.7416	298.15	3.0445e-06
0.7416	303.15	2.6577e-06
0.7416	308.15	2.3298e-06
0.7416	313.15	2.0281e-06
0.7416	318.15	1.7823e-06
0.7416	323.15	1.5575e-06
0.8170	293.15	3.9200e-06
0.8170	298.15	3.4317e-06
0.8170	303.15	2.9992e-06
0.8170	308.15	2.6223e-06
0.8170	313.15	2.2786e-06
0.8170	318.15	1.9989e-06
0.8170	323.15	1.7485e-06
0.8844	293.15	4.4525e-06
0.8844	298.15	3.8929e-06
0.8844	303.15	3.4069e-06
0.8844	308.15	2.9705e-06
0.8844	313.15	2.5770e-06
0.8844	318.15	2.2582e-06
0.8844	323.15	1.9780e-06
0.9451	293.15	5.1446e-06
0.9451	298.15	4.4938e-06
0.9451	303.15	3.9396e-06
0.9451	308.15	3.4295e-06
0.9451	313.15	2.9727e-06
0.9451	318.15	2.6012e-06
0.9451	323.15	2.2830e-06
1.0000	293.15	6.1084e-06
1.0000	298.15	5.3379e-06
1.0000	303.15	4.6898e-06
1.0000	308.15	4.0827e-06
1.0000	313.15	3.5374e-06
1.0000	318.15	3.0938e-06
1.0000	323.15	2.7215e-06

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 2-Methyl-1-butanol (2) - Liquid	Temperature, K - Liquid	Kinematic viscosity, m2/s - Liquid
0.0000	293.15	1.5248e-06
0.0000	298.15	1.3895e-06
0.0000	303.15	1.2261e-06
0.0000	308.15	1.1278e-06
0.0000	313.15	1.0250e-06
0.0000	318.15	9.3990e-07
0.0000	323.15	8.2820e-07
0.0915	293.15	1.6616e-06
0.0915	298.15	1.5003e-06
0.0915	303.15	1.3164e-06
0.0915	308.15	1.1983e-06
0.0915	313.15	1.0785e-06
0.0915	318.15	9.7970e-07
0.0915	323.15	8.5860e-07
0.1753	293.15	1.7965e-06
0.1753	298.15	1.6110e-06
0.1753	303.15	1.4077e-06
0.1753	308.15	1.2717e-06
0.1753	313.15	1.1367e-06
0.1753	318.15	1.0251e-06
0.1753	323.15	8.9580e-07
0.2524	293.15	1.9181e-06
0.2524	298.15	1.7130e-06
0.2524	303.15	1.4954e-06
0.2524	308.15	1.3437e-06
0.2524	313.15	1.1960e-06
0.2524	318.15	1.0735e-06
0.2524	323.15	9.3680e-07
0.3235	293.15	2.0393e-06
0.3235	298.15	1.8161e-06
0.3235	303.15	1.5851e-06
0.3235	308.15	1.4194e-06
0.3235	313.15	1.2589e-06
0.3235	318.15	1.1264e-06
0.3235	323.15	9.8330e-07
0.3894	293.15	2.1715e-06
0.3894	298.15	1.9295e-06
0.3894	303.15	1.6846e-06
0.3894	308.15	1.5037e-06
0.3894	313.15	1.3306e-06
0.3894	318.15	1.1865e-06
0.3894	323.15	1.0363e-06
0.4505	293.15	2.3219e-06
0.4505	298.15	2.0592e-06
0.4505	303.15	1.7984e-06
0.4505	308.15	1.5994e-06
0.4505	313.15	1.4108e-06
0.4505	318.15	1.2547e-06
0.4505	323.15	1.0957e-06
0.5605	293.15	2.6732e-06
0.5605	298.15	2.3576e-06
0.5605	303.15	2.0569e-06
0.5605	308.15	1.8187e-06
0.5605	313.15	1.5954e-06
0.5605	318.15	1.4116e-06
0.5605	323.15	1.2327e-06
0.6567	293.15	3.0617e-06
0.6567	298.15	2.6912e-06
0.6567	303.15	2.3483e-06
0.6567	308.15	2.0654e-06
0.6567	313.15	1.8039e-06
0.6567	318.15	1.5898e-06
0.6567	323.15	1.3881e-06
0.7416	293.15	3.4735e-06
0.7416	298.15	3.0445e-06
0.7416	303.15	2.6577e-06
0.7416	308.15	2.3298e-06
0.7416	313.15	2.0281e-06
0.7416	318.15	1.7823e-06
0.7416	323.15	1.5575e-06
0.8170	293.15	3.9200e-06
0.8170	298.15	3.4317e-06
0.8170	303.15	2.9992e-06
0.8170	308.15	2.6223e-06
0.8170	313.15	2.2786e-06
0.8170	318.15	1.9989e-06
0.8170	323.15	1.7485e-06
0.8844	293.15	4.4525e-06
0.8844	298.15	3.8929e-06
0.8844	303.15	3.4069e-06
0.8844	308.15	2.9705e-06
0.8844	313.15	2.5770e-06
0.8844	318.15	2.2582e-06
0.8844	323.15	1.9780e-06
0.9451	293.15	5.1446e-06
0.9451	298.15	4.4938e-06
0.9451	303.15	3.9396e-06
0.9451	308.15	3.4295e-06
0.9451	313.15	2.9727e-06
0.9451	318.15	2.6012e-06
0.9451	323.15	2.2830e-06
1.0000	293.15	6.1084e-06
1.0000	298.15	5.3379e-06
1.0000	303.15	4.6898e-06
1.0000	308.15	4.0827e-06
1.0000	313.15	3.5374e-06
1.0000	318.15	3.0938e-06
1.0000	323.15	2.7215e-06

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0486	1.4073
0.1013	1.4058
0.1523	1.4042
0.1987	1.4028
0.2503	1.4011
0.3004	1.3993
0.3486	1.3976
0.4003	1.3955
0.4502	1.3934
0.5004	1.3912
0.5502	1.389
0.6004	1.3864
0.6503	1.3837
0.7000	1.3811
0.8009	1.3747
0.8503	1.3713
0.9002	1.3676
0.9503	1.3636

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0486	1.4073
0.1013	1.4058
0.1523	1.4042
0.1987	1.4028
0.2503	1.4011
0.3004	1.3993
0.3486	1.3976
0.4003	1.3955
0.4502	1.3934
0.5004	1.3912
0.5502	1.389
0.6004	1.3864
0.6503	1.3837
0.7000	1.3811
0.8009	1.3747
0.8503	1.3713
0.9002	1.3676
0.9503	1.3636

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0486	814.11
0.1013	813.23
0.1523	812.31
0.1987	811.39
0.2503	810.38
0.3004	809.33
0.3486	808.22
0.4003	807.02
0.4502	805.74
0.5004	804.41
0.5502	803.01
0.6004	801.43
0.6503	799.81
0.7000	798.1
0.8009	794.32
0.8503	792.34
0.9002	790.13
0.9503	787.77

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 2-Methyl-1-butanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	789.7
0.0000	298.15	785.3
0.0000	303.15	780.9
0.0000	308.15	776.5
0.0000	313.15	772.2
0.0000	318.15	767.9
0.0000	323.15	763.5
0.0268	293.15	790.9
0.0268	298.15	786.6
0.0268	303.15	782.3
0.0268	308.15	778.0
0.0268	313.15	773.7
0.0268	318.15	769.4
0.0268	323.15	765.1
0.0549	293.15	792.1
0.0549	298.15	787.9
0.0549	303.15	783.7
0.0549	308.15	779.4
0.0549	313.15	775.2
0.0549	318.15	771.0
0.0549	323.15	766.7
0.0845	293.15	793.4
0.0845	298.15	789.2
0.0845	303.15	785.0
0.0845	308.15	780.9
0.0845	313.15	776.7
0.0845	318.15	772.5
0.0845	323.15	768.3
0.1156	293.15	794.7
0.1156	298.15	790.6
0.1156	303.15	786.4
0.1156	308.15	782.3
0.1156	313.15	778.2
0.1156	318.15	774.1
0.1156	323.15	769.9
0.1484	293.15	795.9
0.1484	298.15	791.9
0.1484	303.15	787.8
0.1484	308.15	783.8
0.1484	313.15	779.7
0.1484	318.15	775.6
0.1484	323.15	771.5
0.1830	293.15	797.2
0.1830	298.15	793.2
0.1830	303.15	789.2
0.1830	308.15	785.2
0.1830	313.15	781.2
0.1830	318.15	777.2
0.1830	323.15	773.1
0.2584	293.15	799.9
0.2584	298.15	796.0
0.2584	303.15	792.0
0.2584	308.15	788.1
0.2584	313.15	784.2
0.2584	318.15	780.3
0.2584	323.15	776.3
0.3433	293.15	802.7
0.3433	298.15	798.8
0.3433	303.15	795.0
0.3433	308.15	791.2
0.3433	313.15	787.3
0.3433	318.15	783.5
0.3433	323.15	779.6
0.4395	293.15	805.5
0.4395	298.15	801.8
0.4395	303.15	798.0
0.4395	308.15	794.3
0.4395	313.15	790.5
0.4395	318.15	786.8
0.4395	323.15	782.9
0.5495	293.15	808.4
0.5495	298.15	804.8
0.5495	303.15	801.1
0.5495	308.15	797.5
0.5495	313.15	793.8
0.5495	318.15	790.1
0.5495	323.15	786.3
0.6765	293.15	811.4
0.6765	298.15	807.9
0.6765	303.15	804.2
0.6765	308.15	800.7
0.6765	313.15	797.0
0.6765	318.15	793.4
0.6765	323.15	789.7
0.8247	293.15	814.5
0.8247	298.15	811.0
0.8247	303.15	807.4
0.8247	308.15	803.9
0.8247	313.15	800.3
0.8247	318.15	796.7
0.8247	323.15	793.2
1.0000	293.15	817.6
1.0000	298.15	814.1
1.0000	303.15	810.5
1.0000	308.15	807.1
1.0000	313.15	803.6
1.0000	318.15	800.1
1.0000	323.15	796.6

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0486	814.11
0.1013	813.23
0.1523	812.31
0.1987	811.39
0.2503	810.38
0.3004	809.33
0.3486	808.22
0.4003	807.02
0.4502	805.74
0.5004	804.41
0.5502	803.01
0.6004	801.43
0.6503	799.81
0.7000	798.1
0.8009	794.32
0.8503	792.34
0.9002	790.13
0.9503	787.77

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 2-Methyl-1-butanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	789.7
0.0000	298.15	785.3
0.0000	303.15	780.9
0.0000	308.15	776.5
0.0000	313.15	772.2
0.0000	318.15	767.9
0.0000	323.15	763.5
0.0268	293.15	790.9
0.0268	298.15	786.6
0.0268	303.15	782.3
0.0268	308.15	778.0
0.0268	313.15	773.7
0.0268	318.15	769.4
0.0268	323.15	765.1
0.0549	293.15	792.1
0.0549	298.15	787.9
0.0549	303.15	783.7
0.0549	308.15	779.4
0.0549	313.15	775.2
0.0549	318.15	771.0
0.0549	323.15	766.7
0.0845	293.15	793.4
0.0845	298.15	789.2
0.0845	303.15	785.0
0.0845	308.15	780.9
0.0845	313.15	776.7
0.0845	318.15	772.5
0.0845	323.15	768.3
0.1156	293.15	794.7
0.1156	298.15	790.6
0.1156	303.15	786.4
0.1156	308.15	782.3
0.1156	313.15	778.2
0.1156	318.15	774.1
0.1156	323.15	769.9
0.1484	293.15	795.9
0.1484	298.15	791.9
0.1484	303.15	787.8
0.1484	308.15	783.8
0.1484	313.15	779.7
0.1484	318.15	775.6
0.1484	323.15	771.5
0.1830	293.15	797.2
0.1830	298.15	793.2
0.1830	303.15	789.2
0.1830	308.15	785.2
0.1830	313.15	781.2
0.1830	318.15	777.2
0.1830	323.15	773.1
0.2584	293.15	799.9
0.2584	298.15	796.0
0.2584	303.15	792.0
0.2584	308.15	788.1
0.2584	313.15	784.2
0.2584	318.15	780.3
0.2584	323.15	776.3
0.3433	293.15	802.7
0.3433	298.15	798.8
0.3433	303.15	795.0
0.3433	308.15	791.2
0.3433	313.15	787.3
0.3433	318.15	783.5
0.3433	323.15	779.6
0.4395	293.15	805.5
0.4395	298.15	801.8
0.4395	303.15	798.0
0.4395	308.15	794.3
0.4395	313.15	790.5
0.4395	318.15	786.8
0.4395	323.15	782.9
0.5495	293.15	808.4
0.5495	298.15	804.8
0.5495	303.15	801.1
0.5495	308.15	797.5
0.5495	313.15	793.8
0.5495	318.15	790.1
0.5495	323.15	786.3
0.6765	293.15	811.4
0.6765	298.15	807.9
0.6765	303.15	804.2
0.6765	308.15	800.7
0.6765	313.15	797.0
0.6765	318.15	793.4
0.6765	323.15	789.7
0.8247	293.15	814.5
0.8247	298.15	811.0
0.8247	303.15	807.4
0.8247	308.15	803.9
0.8247	313.15	800.3
0.8247	318.15	796.7
0.8247	323.15	793.2
1.0000	293.15	817.6
1.0000	298.15	814.1
1.0000	303.15	810.5
1.0000	308.15	807.1
1.0000	313.15	803.6
1.0000	318.15	800.1
1.0000	323.15	796.6

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
0.0486	1247.7
0.1013	1245.0
0.1523	1241.4
0.1987	1237.6
0.2503	1233.6
0.3004	1229.6
0.3486	1225.3
0.4003	1221.0
0.4502	1215.9
0.5004	1210.5
0.5502	1205.4
0.6004	1199.4
0.6503	1193.1
0.7000	1186.9
0.8009	1173.0
0.8503	1166.0
0.9002	1158.2
0.9503	1150.2

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
0.0486	1247.7
0.1013	1245.0
0.1523	1241.4
0.1987	1237.6
0.2503	1233.6
0.3004	1229.6
0.3486	1225.3
0.4003	1221.0
0.4502	1215.9
0.5004	1210.5
0.5502	1205.4
0.6004	1199.4
0.6503	1193.1
0.7000	1186.9
0.8009	1173.0
0.8503	1166.0
0.9002	1158.2
0.9503	1150.2

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Methyl-1-butanol (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.15	0.0000	0.0223
293.15	0.0268	0.0225
293.15	0.0549	0.0226
293.15	0.0845	0.0228
293.15	0.1156	0.0229
293.15	0.1484	0.0230
293.15	0.1830	0.0230
293.15	0.2584	0.0232
293.15	0.3433	0.0233
293.15	0.4395	0.0234
293.15	0.5495	0.0236
293.15	0.6765	0.0237
293.15	0.8247	0.0239
293.15	1.0000	0.0241
298.15	0.0000	0.0218
298.15	0.0268	0.0221
298.15	0.0549	0.0222
298.15	0.0845	0.0224
298.15	0.1156	0.0225
298.15	0.1484	0.0225
298.15	0.1830	0.0226
298.15	0.2584	0.0227
298.15	0.3433	0.0229
298.15	0.4395	0.0230
298.15	0.5495	0.0231
298.15	0.6765	0.0232
298.15	0.8247	0.0234
298.15	1.0000	0.0236
303.15	0.0000	0.0214
303.15	0.0268	0.0217
303.15	0.0549	0.0219
303.15	0.0845	0.0220
303.15	0.1156	0.0221
303.15	0.1484	0.0222
303.15	0.1830	0.0222
303.15	0.2584	0.0223
303.15	0.3433	0.0225
303.15	0.4395	0.0226
303.15	0.5495	0.0227
303.15	0.6765	0.0228
303.15	0.8247	0.0230
303.15	1.0000	0.0231
308.15	0.0000	0.0210
308.15	0.0268	0.0214
308.15	0.0549	0.0216
308.15	0.0845	0.0217
308.15	0.1156	0.0217
308.15	0.1484	0.0218
308.15	0.1830	0.0219
308.15	0.2584	0.0220
308.15	0.3433	0.0221
308.15	0.4395	0.0222
308.15	0.5495	0.0223
308.15	0.6765	0.0224
308.15	0.8247	0.0225
308.15	1.0000	0.0227
313.15	0.0000	0.0206
313.15	0.0268	0.0210
313.15	0.0549	0.0212
313.15	0.0845	0.0213
313.15	0.1156	0.0214
313.15	0.1484	0.0215
313.15	0.1830	0.0215
313.15	0.2584	0.0216
313.15	0.3433	0.0218
313.15	0.4395	0.0218
313.15	0.5495	0.0219
313.15	0.6765	0.0220
313.15	0.8247	0.0221
313.15	1.0000	0.0223
318.15	0.0000	0.0202
318.15	0.0268	0.0207
318.15	0.0549	0.0209
318.15	0.0845	0.0210
318.15	0.1156	0.0211
318.15	0.1484	0.0211
318.15	0.1830	0.0212
318.15	0.2584	0.0212
318.15	0.3433	0.0214
318.15	0.4395	0.0214
318.15	0.5495	0.0215
318.15	0.6765	0.0216
318.15	0.8247	0.0217
318.15	1.0000	0.0219
323.15	0.0000	0.0198
323.15	0.0268	0.0204
323.15	0.0549	0.0205
323.15	0.0845	0.0206
323.15	0.1156	0.0207
323.15	0.1484	0.0208
323.15	0.1830	0.0209
323.15	0.2584	0.0209
323.15	0.3433	0.0210
323.15	0.4395	0.0210
323.15	0.5495	0.0211
323.15	0.6765	0.0213
323.15	0.8247	0.0213
323.15	1.0000	0.0214

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Methyl-1-butanol (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.15	0.0000	0.0223
293.15	0.0268	0.0225
293.15	0.0549	0.0226
293.15	0.0845	0.0228
293.15	0.1156	0.0229
293.15	0.1484	0.0230
293.15	0.1830	0.0230
293.15	0.2584	0.0232
293.15	0.3433	0.0233
293.15	0.4395	0.0234
293.15	0.5495	0.0236
293.15	0.6765	0.0237
293.15	0.8247	0.0239
293.15	1.0000	0.0241
298.15	0.0000	0.0218
298.15	0.0268	0.0221
298.15	0.0549	0.0222
298.15	0.0845	0.0224
298.15	0.1156	0.0225
298.15	0.1484	0.0225
298.15	0.1830	0.0226
298.15	0.2584	0.0227
298.15	0.3433	0.0229
298.15	0.4395	0.0230
298.15	0.5495	0.0231
298.15	0.6765	0.0232
298.15	0.8247	0.0234
298.15	1.0000	0.0236
303.15	0.0000	0.0214
303.15	0.0268	0.0217
303.15	0.0549	0.0219
303.15	0.0845	0.0220
303.15	0.1156	0.0221
303.15	0.1484	0.0222
303.15	0.1830	0.0222
303.15	0.2584	0.0223
303.15	0.3433	0.0225
303.15	0.4395	0.0226
303.15	0.5495	0.0227
303.15	0.6765	0.0228
303.15	0.8247	0.0230
303.15	1.0000	0.0231
308.15	0.0000	0.0210
308.15	0.0268	0.0214
308.15	0.0549	0.0216
308.15	0.0845	0.0217
308.15	0.1156	0.0217
308.15	0.1484	0.0218
308.15	0.1830	0.0219
308.15	0.2584	0.0220
308.15	0.3433	0.0221
308.15	0.4395	0.0222
308.15	0.5495	0.0223
308.15	0.6765	0.0224
308.15	0.8247	0.0225
308.15	1.0000	0.0227
313.15	0.0000	0.0206
313.15	0.0268	0.0210
313.15	0.0549	0.0212
313.15	0.0845	0.0213
313.15	0.1156	0.0214
313.15	0.1484	0.0215
313.15	0.1830	0.0215
313.15	0.2584	0.0216
313.15	0.3433	0.0218
313.15	0.4395	0.0218
313.15	0.5495	0.0219
313.15	0.6765	0.0220
313.15	0.8247	0.0221
313.15	1.0000	0.0223
318.15	0.0000	0.0202
318.15	0.0268	0.0207
318.15	0.0549	0.0209
318.15	0.0845	0.0210
318.15	0.1156	0.0211
318.15	0.1484	0.0211
318.15	0.1830	0.0212
318.15	0.2584	0.0212
318.15	0.3433	0.0214
318.15	0.4395	0.0214
318.15	0.5495	0.0215
318.15	0.6765	0.0216
318.15	0.8247	0.0217
318.15	1.0000	0.0219
323.15	0.0000	0.0198
323.15	0.0268	0.0204
323.15	0.0549	0.0205
323.15	0.0845	0.0206
323.15	0.1156	0.0207
323.15	0.1484	0.0208
323.15	0.1830	0.0209
323.15	0.2584	0.0209
323.15	0.3433	0.0210
323.15	0.4395	0.0210
323.15	0.5495	0.0211
323.15	0.6765	0.0213
323.15	0.8247	0.0213
323.15	1.0000	0.0214

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	33.30	372.95
0.0000	66.60	390.35
0.0000	101.30	402.45
0.0630	66.60	382.15
0.0650	101.30	393.45
0.0760	33.30	363.55
0.0760	66.60	380.75
0.1250	33.30	358.85
0.1260	101.30	387.25
0.1820	66.60	371.25
0.1920	101.30	381.75
0.2240	66.60	368.25
0.2240	101.30	379.45
0.2420	101.30	378.35
0.2460	33.30	349.85
0.2790	66.60	364.85
0.2940	33.30	347.15
0.3110	101.30	374.15
0.3360	33.30	345.25
0.3840	33.30	343.15
0.3940	66.60	358.85
0.3950	101.30	370.05
0.4220	33.30	341.45
0.4380	66.60	356.85
0.4770	66.60	355.35
0.4780	101.30	366.25
0.4880	33.30	338.85
0.5410	66.60	352.95
0.5510	101.30	363.55
0.5620	33.30	336.35
0.6060	101.30	361.65
0.6280	66.60	350.05
0.6430	33.30	333.85
0.7330	66.60	347.05
0.7520	101.30	357.35
0.7740	33.30	330.55
0.8810	101.30	353.95
0.8850	66.60	343.35
0.8870	33.30	328.05
0.9070	33.30	327.65
0.9080	101.30	353.35
0.9100	66.60	342.85
1.0000	33.30	325.75
1.0000	66.60	341.15
1.0000	101.30	351.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	401.86
0.0210	398.77
0.0620	393.79
0.1020	389.90
0.1410	386.61
0.1750	383.66
0.2160	380.78
0.2740	377.18
0.3280	373.73
0.3850	371.02
0.4160	369.67
0.4460	368.20
0.4760	366.72
0.5160	365.22
0.5500	363.97
0.5800	362.95
0.6950	359.39
0.8170	355.97
0.9220	353.32
0.9720	352.08
0.9930	351.61
1.0000	351.50

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	33.30	372.95
0.0000	66.60	390.35
0.0000	101.30	402.45
0.0630	66.60	382.15
0.0650	101.30	393.45
0.0760	33.30	363.55
0.0760	66.60	380.75
0.1250	33.30	358.85
0.1260	101.30	387.25
0.1820	66.60	371.25
0.1920	101.30	381.75
0.2240	66.60	368.25
0.2240	101.30	379.45
0.2420	101.30	378.35
0.2460	33.30	349.85
0.2790	66.60	364.85
0.2940	33.30	347.15
0.3110	101.30	374.15
0.3360	33.30	345.25
0.3840	33.30	343.15
0.3940	66.60	358.85
0.3950	101.30	370.05
0.4220	33.30	341.45
0.4380	66.60	356.85
0.4770	66.60	355.35
0.4780	101.30	366.25
0.4880	33.30	338.85
0.5410	66.60	352.95
0.5510	101.30	363.55
0.5620	33.30	336.35
0.6060	101.30	361.65
0.6280	66.60	350.05
0.6430	33.30	333.85
0.7330	66.60	347.05
0.7520	101.30	357.35
0.7740	33.30	330.55
0.8810	101.30	353.95
0.8850	66.60	343.35
0.8870	33.30	328.05
0.9070	33.30	327.65
0.9080	101.30	353.35
0.9100	66.60	342.85
1.0000	33.30	325.75
1.0000	66.60	341.15
1.0000	101.30	351.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	401.86
0.0210	398.77
0.0620	393.79
0.1020	389.90
0.1410	386.61
0.1750	383.66
0.2160	380.78
0.2740	377.18
0.3280	373.73
0.3850	371.02
0.4160	369.67
0.4460	368.20
0.4760	366.72
0.5160	365.22
0.5500	363.97
0.5800	362.95
0.6950	359.39
0.8170	355.97
0.9220	353.32
0.9720	352.08
0.9930	351.61
1.0000	351.50

Sources

• Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
• Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Methanol + 2-Methyl-1-butanol and Ethanol + 2-Methyl-1-butanol
• Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
• Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K