Mixture of Ethanol + 1-Butanol, 3-methyl-

Datasets

1. Mole fraction (4)
2. ν - Kinematic viscosity, m2/s (2)
3. ρ_l - Mass density, kg/m3 (2)
4. γ - Surface tension liquid-gas, N/m (2)
5. T_boil - Boiling temperature at pressure P, K (2)

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
0.0217	0.2135
0.0448	0.3585
0.0925	0.5607
0.1403	0.6603
0.1496	0.6803
0.1786	0.7178
0.1835	0.7223
0.2201	0.7674
0.2940	0.8345
0.3652	0.8682
0.4001	0.8871
0.5011	0.9211
0.5367	0.9339
0.6788	0.9588
0.7502	0.9696
0.8186	0.9791
0.8901	0.9860
0.9195	0.9874
0.9598	0.9938

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethanol (1) - Gas
0.0697	50.66	0.3849
0.2336	50.66	0.7298
0.2951	50.66	0.7901
0.4911	50.66	0.8990
0.7153	50.66	0.9606
0.8182	50.66	0.9772
0.0740	101.33	0.3854
0.1372	101.33	0.5558
0.3643	101.33	0.8189
0.4133	101.33	0.8489
0.4940	101.33	0.8860
0.6053	101.33	0.9254
0.6730	101.33	0.9433
0.8825	101.33	0.9836
0.1887	151.99	0.6189
0.3729	151.99	0.8074
0.4265	151.99	0.8385
0.6166	151.99	0.9192
0.6578	151.99	0.9311
0.7068	151.99	0.9433
0.9940	151.99	0.9990

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
0.0217	0.2135
0.0448	0.3585
0.0925	0.5607
0.1403	0.6603
0.1496	0.6803
0.1786	0.7178
0.1835	0.7223
0.2201	0.7674
0.2940	0.8345
0.3652	0.8682
0.4001	0.8871
0.5011	0.9211
0.5367	0.9339
0.6788	0.9588
0.7502	0.9696
0.8186	0.9791
0.8901	0.9860
0.9195	0.9874
0.9598	0.9938

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethanol (1) - Gas
0.0697	50.66	0.3849
0.2336	50.66	0.7298
0.2951	50.66	0.7901
0.4911	50.66	0.8990
0.7153	50.66	0.9606
0.8182	50.66	0.9772
0.0740	101.33	0.3854
0.1372	101.33	0.5558
0.3643	101.33	0.8189
0.4133	101.33	0.8489
0.4940	101.33	0.8860
0.6053	101.33	0.9254
0.6730	101.33	0.9433
0.8825	101.33	0.9836
0.1887	151.99	0.6189
0.3729	151.99	0.8074
0.4265	151.99	0.8385
0.6166	151.99	0.9192
0.6578	151.99	0.9311
0.7068	151.99	0.9433
0.9940	151.99	0.9990

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Butanol, 3-methyl- (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	1.5522e-06
0.0915	298.15	1.4246e-06
0.0915	303.15	1.2658e-06
0.0915	308.15	1.1694e-06
0.0915	313.15	1.0673e-06
0.0915	318.15	9.7990e-07
0.0915	323.15	8.7150e-07
0.1753	293.15	1.6131e-06
0.1753	298.15	1.4819e-06
0.1753	303.15	1.3220e-06
0.1753	308.15	1.2213e-06
0.1753	313.15	1.1174e-06
0.1753	318.15	1.0257e-06
0.1753	323.15	9.1270e-07
0.2524	293.15	1.6775e-06
0.2524	298.15	1.5419e-06
0.2524	303.15	1.3815e-06
0.2524	308.15	1.2749e-06
0.2524	313.15	1.1661e-06
0.2524	318.15	1.0700e-06
0.2524	323.15	9.5280e-07
0.3235	293.15	1.7481e-06
0.3235	298.15	1.6077e-06
0.3235	303.15	1.4476e-06
0.3235	308.15	1.3327e-06
0.3235	313.15	1.2177e-06
0.3235	318.15	1.1172e-06
0.3235	323.15	9.9610e-07
0.3894	293.15	1.8311e-06
0.3894	298.15	1.6859e-06
0.3894	303.15	1.5230e-06
0.3894	308.15	1.3985e-06
0.3894	313.15	1.2772e-06
0.3894	318.15	1.1705e-06
0.3894	323.15	1.0456e-06
0.4505	293.15	1.9316e-06
0.4505	298.15	1.7785e-06
0.4505	303.15	1.6087e-06
0.4505	308.15	1.4737e-06
0.4505	313.15	1.3460e-06
0.4505	318.15	1.2315e-06
0.4505	323.15	1.1022e-06
0.5605	293.15	2.1884e-06
0.5605	298.15	2.0061e-06
0.5605	303.15	1.8112e-06
0.5605	308.15	1.6525e-06
0.5605	313.15	1.5077e-06
0.5605	318.15	1.3739e-06
0.5605	323.15	1.2344e-06
0.6567	293.15	2.5104e-06
0.6567	298.15	2.2811e-06
0.6567	303.15	2.0519e-06
0.6567	308.15	1.8635e-06
0.6567	313.15	1.6935e-06
0.6567	318.15	1.5377e-06
0.6567	323.15	1.3854e-06
0.7416	293.15	2.8877e-06
0.7416	298.15	2.5971e-06
0.7416	303.15	2.3282e-06
0.7416	308.15	2.1026e-06
0.7416	313.15	1.8994e-06
0.7416	318.15	1.7188e-06
0.7416	323.15	1.5485e-06
0.8170	293.15	3.3143e-06
0.8170	298.15	2.9584e-06
0.8170	303.15	2.6408e-06
0.8170	308.15	2.3675e-06
0.8170	313.15	2.1269e-06
0.8170	318.15	1.9171e-06
0.8170	323.15	1.7215e-06
0.8844	293.15	3.7958e-06
0.8844	298.15	3.3721e-06
0.8844	303.15	2.9915e-06
0.8844	308.15	2.6601e-06
0.8844	313.15	2.3802e-06
0.8844	318.15	2.1336e-06
0.8844	323.15	1.9041e-06
0.9451	293.15	4.3509e-06
0.9451	298.15	3.8414e-06
0.9451	303.15	3.3834e-06
0.9451	308.15	2.9814e-06
0.9451	313.15	2.6556e-06
0.9451	318.15	2.3629e-06
0.9451	323.15	2.0943e-06
1.0000	293.15	5.0041e-06
1.0000	298.15	4.3550e-06
1.0000	303.15	3.8147e-06
1.0000	308.15	3.3305e-06
1.0000	313.15	2.9366e-06
1.0000	318.15	2.5896e-06
1.0000	323.15	2.2863e-06

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Butanol, 3-methyl- (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	1.5522e-06
0.0915	298.15	1.4246e-06
0.0915	303.15	1.2658e-06
0.0915	308.15	1.1694e-06
0.0915	313.15	1.0673e-06
0.0915	318.15	9.7990e-07
0.0915	323.15	8.7150e-07
0.1753	293.15	1.6131e-06
0.1753	298.15	1.4819e-06
0.1753	303.15	1.3220e-06
0.1753	308.15	1.2213e-06
0.1753	313.15	1.1174e-06
0.1753	318.15	1.0257e-06
0.1753	323.15	9.1270e-07
0.2524	293.15	1.6775e-06
0.2524	298.15	1.5419e-06
0.2524	303.15	1.3815e-06
0.2524	308.15	1.2749e-06
0.2524	313.15	1.1661e-06
0.2524	318.15	1.0700e-06
0.2524	323.15	9.5280e-07
0.3235	293.15	1.7481e-06
0.3235	298.15	1.6077e-06
0.3235	303.15	1.4476e-06
0.3235	308.15	1.3327e-06
0.3235	313.15	1.2177e-06
0.3235	318.15	1.1172e-06
0.3235	323.15	9.9610e-07
0.3894	293.15	1.8311e-06
0.3894	298.15	1.6859e-06
0.3894	303.15	1.5230e-06
0.3894	308.15	1.3985e-06
0.3894	313.15	1.2772e-06
0.3894	318.15	1.1705e-06
0.3894	323.15	1.0456e-06
0.4505	293.15	1.9316e-06
0.4505	298.15	1.7785e-06
0.4505	303.15	1.6087e-06
0.4505	308.15	1.4737e-06
0.4505	313.15	1.3460e-06
0.4505	318.15	1.2315e-06
0.4505	323.15	1.1022e-06
0.5605	293.15	2.1884e-06
0.5605	298.15	2.0061e-06
0.5605	303.15	1.8112e-06
0.5605	308.15	1.6525e-06
0.5605	313.15	1.5077e-06
0.5605	318.15	1.3739e-06
0.5605	323.15	1.2344e-06
0.6567	293.15	2.5104e-06
0.6567	298.15	2.2811e-06
0.6567	303.15	2.0519e-06
0.6567	308.15	1.8635e-06
0.6567	313.15	1.6935e-06
0.6567	318.15	1.5377e-06
0.6567	323.15	1.3854e-06
0.7416	293.15	2.8877e-06
0.7416	298.15	2.5971e-06
0.7416	303.15	2.3282e-06
0.7416	308.15	2.1026e-06
0.7416	313.15	1.8994e-06
0.7416	318.15	1.7188e-06
0.7416	323.15	1.5485e-06
0.8170	293.15	3.3143e-06
0.8170	298.15	2.9584e-06
0.8170	303.15	2.6408e-06
0.8170	308.15	2.3675e-06
0.8170	313.15	2.1269e-06
0.8170	318.15	1.9171e-06
0.8170	323.15	1.7215e-06
0.8844	293.15	3.7958e-06
0.8844	298.15	3.3721e-06
0.8844	303.15	2.9915e-06
0.8844	308.15	2.6601e-06
0.8844	313.15	2.3802e-06
0.8844	318.15	2.1336e-06
0.8844	323.15	1.9041e-06
0.9451	293.15	4.3509e-06
0.9451	298.15	3.8414e-06
0.9451	303.15	3.3834e-06
0.9451	308.15	2.9814e-06
0.9451	313.15	2.6556e-06
0.9451	318.15	2.3629e-06
0.9451	323.15	2.0943e-06
1.0000	293.15	5.0041e-06
1.0000	298.15	4.3550e-06
1.0000	303.15	3.8147e-06
1.0000	308.15	3.3305e-06
1.0000	313.15	2.9366e-06
1.0000	318.15	2.5896e-06
1.0000	323.15	2.2863e-06

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Butanol, 3-methyl- (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	790.5
0.0268	298.15	786.2
0.0268	303.15	781.8
0.0268	308.15	777.5
0.0268	313.15	773.2
0.0268	318.15	769.0
0.0268	323.15	764.6
0.0549	293.15	791.3
0.0549	298.15	787.0
0.0549	303.15	782.7
0.0549	308.15	778.4
0.0549	313.15	774.2
0.0549	318.15	770.0
0.0549	323.15	765.7
0.0845	293.15	792.1
0.0845	298.15	787.9
0.0845	303.15	783.7
0.0845	308.15	779.4
0.0845	313.15	775.2
0.0845	318.15	771.0
0.0845	323.15	766.7
0.1156	293.15	792.9
0.1156	298.15	788.8
0.1156	303.15	784.6
0.1156	308.15	780.4
0.1156	313.15	776.2
0.1156	318.15	772.0
0.1156	323.15	767.8
0.1484	293.15	793.8
0.1484	298.15	789.7
0.1484	303.15	785.5
0.1484	308.15	781.4
0.1484	313.15	777.2
0.1484	318.15	773.1
0.1484	323.15	768.9
0.1830	293.15	794.7
0.1830	298.15	790.6
0.1830	303.15	786.5
0.1830	308.15	782.4
0.1830	313.15	778.2
0.1830	318.15	774.1
0.1830	323.15	769.9
0.2584	293.15	796.6
0.2584	298.15	792.5
0.2584	303.15	788.5
0.2584	308.15	784.4
0.2584	313.15	780.3
0.2584	318.15	776.3
0.2584	323.15	772.1
0.3433	293.15	798.5
0.3433	298.15	794.5
0.3433	303.15	790.5
0.3433	308.15	786.5
0.3433	313.15	782.4
0.3433	318.15	778.4
0.3433	323.15	774.3
0.4395	293.15	800.4
0.4395	298.15	796.5
0.4395	303.15	792.5
0.4395	308.15	788.6
0.4395	313.15	784.6
0.4395	318.15	780.6
0.4395	323.15	776.6
0.5495	293.15	802.4
0.5495	298.15	798.5
0.5495	303.15	794.6
0.5495	308.15	790.7
0.5495	313.15	786.7
0.5495	318.15	782.8
0.5495	323.15	778.9
0.6765	293.15	804.3
0.6765	298.15	800.5
0.6765	303.15	796.7
0.6765	308.15	792.9
0.6765	313.15	788.9
0.6765	318.15	785.1
0.6765	323.15	781.2
0.8247	293.15	806.3
0.8247	298.15	802.6
0.8247	303.15	798.7
0.8247	308.15	795.0
0.8247	313.15	791.0
0.8247	318.15	787.3
0.8247	323.15	783.4
1.0000	293.15	808.3
1.0000	298.15	804.6
1.0000	303.15	800.8
1.0000	308.15	797.1
1.0000	313.15	793.2
1.0000	318.15	789.5
1.0000	323.15	785.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1-Butanol, 3-methyl- (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	790.5
0.0268	298.15	786.2
0.0268	303.15	781.8
0.0268	308.15	777.5
0.0268	313.15	773.2
0.0268	318.15	769.0
0.0268	323.15	764.6
0.0549	293.15	791.3
0.0549	298.15	787.0
0.0549	303.15	782.7
0.0549	308.15	778.4
0.0549	313.15	774.2
0.0549	318.15	770.0
0.0549	323.15	765.7
0.0845	293.15	792.1
0.0845	298.15	787.9
0.0845	303.15	783.7
0.0845	308.15	779.4
0.0845	313.15	775.2
0.0845	318.15	771.0
0.0845	323.15	766.7
0.1156	293.15	792.9
0.1156	298.15	788.8
0.1156	303.15	784.6
0.1156	308.15	780.4
0.1156	313.15	776.2
0.1156	318.15	772.0
0.1156	323.15	767.8
0.1484	293.15	793.8
0.1484	298.15	789.7
0.1484	303.15	785.5
0.1484	308.15	781.4
0.1484	313.15	777.2
0.1484	318.15	773.1
0.1484	323.15	768.9
0.1830	293.15	794.7
0.1830	298.15	790.6
0.1830	303.15	786.5
0.1830	308.15	782.4
0.1830	313.15	778.2
0.1830	318.15	774.1
0.1830	323.15	769.9
0.2584	293.15	796.6
0.2584	298.15	792.5
0.2584	303.15	788.5
0.2584	308.15	784.4
0.2584	313.15	780.3
0.2584	318.15	776.3
0.2584	323.15	772.1
0.3433	293.15	798.5
0.3433	298.15	794.5
0.3433	303.15	790.5
0.3433	308.15	786.5
0.3433	313.15	782.4
0.3433	318.15	778.4
0.3433	323.15	774.3
0.4395	293.15	800.4
0.4395	298.15	796.5
0.4395	303.15	792.5
0.4395	308.15	788.6
0.4395	313.15	784.6
0.4395	318.15	780.6
0.4395	323.15	776.6
0.5495	293.15	802.4
0.5495	298.15	798.5
0.5495	303.15	794.6
0.5495	308.15	790.7
0.5495	313.15	786.7
0.5495	318.15	782.8
0.5495	323.15	778.9
0.6765	293.15	804.3
0.6765	298.15	800.5
0.6765	303.15	796.7
0.6765	308.15	792.9
0.6765	313.15	788.9
0.6765	318.15	785.1
0.6765	323.15	781.2
0.8247	293.15	806.3
0.8247	298.15	802.6
0.8247	303.15	798.7
0.8247	308.15	795.0
0.8247	313.15	791.0
0.8247	318.15	787.3
0.8247	323.15	783.4
1.0000	293.15	808.3
1.0000	298.15	804.6
1.0000	303.15	800.8
1.0000	308.15	797.1
1.0000	313.15	793.2
1.0000	318.15	789.5
1.0000	323.15	785.7

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol, 3-methyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.15	0.0000	0.0223
293.15	0.0268	0.0226
293.15	0.0549	0.0228
293.15	0.0845	0.0230
293.15	0.1156	0.0232
293.15	0.1484	0.0233
293.15	0.1830	0.0235
293.15	0.2584	0.0238
293.15	0.3433	0.0240
293.15	0.4395	0.0241
293.15	0.5495	0.0243
293.15	0.6765	0.0243
293.15	0.8247	0.0244
293.15	1.0000	0.0245
298.15	0.0000	0.0218
298.15	0.0268	0.0221
298.15	0.0549	0.0223
298.15	0.0845	0.0225
298.15	0.1156	0.0227
298.15	0.1484	0.0229
298.15	0.1830	0.0231
298.15	0.2584	0.0233
298.15	0.3433	0.0235
298.15	0.4395	0.0237
298.15	0.5495	0.0238
298.15	0.6765	0.0240
298.15	0.8247	0.0240
298.15	1.0000	0.0242
303.15	0.0000	0.0214
303.15	0.0268	0.0217
303.15	0.0549	0.0219
303.15	0.0845	0.0222
303.15	0.1156	0.0224
303.15	0.1484	0.0225
303.15	0.1830	0.0227
303.15	0.2584	0.0230
303.15	0.3433	0.0232
303.15	0.4395	0.0234
303.15	0.5495	0.0235
303.15	0.6765	0.0236
303.15	0.8247	0.0237
303.15	1.0000	0.0238
308.15	0.0000	0.0210
308.15	0.0268	0.0214
308.15	0.0549	0.0216
308.15	0.0845	0.0218
308.15	0.1156	0.0220
308.15	0.1484	0.0222
308.15	0.1830	0.0223
308.15	0.2584	0.0226
308.15	0.3433	0.0228
308.15	0.4395	0.0230
308.15	0.5495	0.0231
308.15	0.6765	0.0232
308.15	0.8247	0.0233
308.15	1.0000	0.0234
313.15	0.0000	0.0206
313.15	0.0268	0.0209
313.15	0.0549	0.0212
313.15	0.0845	0.0214
313.15	0.1156	0.0216
313.15	0.1484	0.0218
313.15	0.1830	0.0219
313.15	0.2584	0.0222
313.15	0.3433	0.0224
313.15	0.4395	0.0226
313.15	0.5495	0.0227
313.15	0.6765	0.0228
313.15	0.8247	0.0229
313.15	1.0000	0.0230
318.15	0.0000	0.0202
318.15	0.0268	0.0206
318.15	0.0549	0.0208
318.15	0.0845	0.0210
318.15	0.1156	0.0212
318.15	0.1484	0.0214
318.15	0.1830	0.0215
318.15	0.2584	0.0218
318.15	0.3433	0.0220
318.15	0.4395	0.0222
318.15	0.5495	0.0223
318.15	0.6765	0.0224
318.15	0.8247	0.0225
318.15	1.0000	0.0226
323.15	0.0000	0.0198
323.15	0.0268	0.0202
323.15	0.0549	0.0204
323.15	0.0845	0.0207
323.15	0.1156	0.0209
323.15	0.1484	0.0210
323.15	0.1830	0.0212
323.15	0.2584	0.0214
323.15	0.3433	0.0216
323.15	0.4395	0.0218
323.15	0.5495	0.0220
323.15	0.6765	0.0221
323.15	0.8247	0.0221
323.15	1.0000	0.0222

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol, 3-methyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.15	0.0000	0.0223
293.15	0.0268	0.0226
293.15	0.0549	0.0228
293.15	0.0845	0.0230
293.15	0.1156	0.0232
293.15	0.1484	0.0233
293.15	0.1830	0.0235
293.15	0.2584	0.0238
293.15	0.3433	0.0240
293.15	0.4395	0.0241
293.15	0.5495	0.0243
293.15	0.6765	0.0243
293.15	0.8247	0.0244
293.15	1.0000	0.0245
298.15	0.0000	0.0218
298.15	0.0268	0.0221
298.15	0.0549	0.0223
298.15	0.0845	0.0225
298.15	0.1156	0.0227
298.15	0.1484	0.0229
298.15	0.1830	0.0231
298.15	0.2584	0.0233
298.15	0.3433	0.0235
298.15	0.4395	0.0237
298.15	0.5495	0.0238
298.15	0.6765	0.0240
298.15	0.8247	0.0240
298.15	1.0000	0.0242
303.15	0.0000	0.0214
303.15	0.0268	0.0217
303.15	0.0549	0.0219
303.15	0.0845	0.0222
303.15	0.1156	0.0224
303.15	0.1484	0.0225
303.15	0.1830	0.0227
303.15	0.2584	0.0230
303.15	0.3433	0.0232
303.15	0.4395	0.0234
303.15	0.5495	0.0235
303.15	0.6765	0.0236
303.15	0.8247	0.0237
303.15	1.0000	0.0238
308.15	0.0000	0.0210
308.15	0.0268	0.0214
308.15	0.0549	0.0216
308.15	0.0845	0.0218
308.15	0.1156	0.0220
308.15	0.1484	0.0222
308.15	0.1830	0.0223
308.15	0.2584	0.0226
308.15	0.3433	0.0228
308.15	0.4395	0.0230
308.15	0.5495	0.0231
308.15	0.6765	0.0232
308.15	0.8247	0.0233
308.15	1.0000	0.0234
313.15	0.0000	0.0206
313.15	0.0268	0.0209
313.15	0.0549	0.0212
313.15	0.0845	0.0214
313.15	0.1156	0.0216
313.15	0.1484	0.0218
313.15	0.1830	0.0219
313.15	0.2584	0.0222
313.15	0.3433	0.0224
313.15	0.4395	0.0226
313.15	0.5495	0.0227
313.15	0.6765	0.0228
313.15	0.8247	0.0229
313.15	1.0000	0.0230
318.15	0.0000	0.0202
318.15	0.0268	0.0206
318.15	0.0549	0.0208
318.15	0.0845	0.0210
318.15	0.1156	0.0212
318.15	0.1484	0.0214
318.15	0.1830	0.0215
318.15	0.2584	0.0218
318.15	0.3433	0.0220
318.15	0.4395	0.0222
318.15	0.5495	0.0223
318.15	0.6765	0.0224
318.15	0.8247	0.0225
318.15	1.0000	0.0226
323.15	0.0000	0.0198
323.15	0.0268	0.0202
323.15	0.0549	0.0204
323.15	0.0845	0.0207
323.15	0.1156	0.0209
323.15	0.1484	0.0210
323.15	0.1830	0.0212
323.15	0.2584	0.0214
323.15	0.3433	0.0216
323.15	0.4395	0.0218
323.15	0.5495	0.0220
323.15	0.6765	0.0221
323.15	0.8247	0.0221
323.15	1.0000	0.0222

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
0.0697	50.66	374.70
0.2336	50.66	360.32
0.2951	50.66	356.55
0.4911	50.66	348.21
0.7153	50.66	340.95
0.8182	50.66	338.27
0.0740	101.33	392.88
0.1372	101.33	386.12
0.3643	101.33	371.55
0.4133	101.33	369.21
0.4940	101.33	366.06
0.6053	101.33	362.05
0.6730	101.33	359.81
0.8825	101.33	353.82
0.1887	151.99	394.42
0.3729	151.99	382.29
0.4265	151.99	379.83
0.6166	151.99	372.50
0.6578	151.99	371.19
0.7068	151.99	369.33
0.9940	151.99	361.72

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
0.0697	50.66	374.70
0.2336	50.66	360.32
0.2951	50.66	356.55
0.4911	50.66	348.21
0.7153	50.66	340.95
0.8182	50.66	338.27
0.0740	101.33	392.88
0.1372	101.33	386.12
0.3643	101.33	371.55
0.4133	101.33	369.21
0.4940	101.33	366.06
0.6053	101.33	362.05
0.6730	101.33	359.81
0.8825	101.33	353.82
0.1887	151.99	394.42
0.3729	151.99	382.29
0.4265	151.99	379.83
0.6166	151.99	372.50
0.6578	151.99	371.19
0.7068	151.99	369.33
0.9940	151.99	361.72

Sources

• Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
• Vapor liquid equilibrium of the ethanol + 3-methyl-1-butanol system at 50.66, 101.33 and 151.99 kPa
• 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