Mixture of 1-Butanol + Methyl Alcohol

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (4)
3. c_sound,fluid - Speed of Sound, m/s (2)
4. P [kPa] x T [K] x x1[mol/mol] (2)
5. Vapor Liquid Equilibrium at Constant Pressure (3)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0006
293.15	0.0997	0.0007
293.15	0.1994	0.0008
293.15	0.3068	0.0010
293.15	0.3991	0.0011
293.15	0.5082	0.0014
293.15	0.6040	0.0016
293.15	0.6992	0.0018
293.15	0.7994	0.0021
293.15	0.9038	0.0023
293.15	1.0000	0.0026
303.15	0.0000	0.0005
303.15	0.0997	0.0006
303.15	0.1994	0.0008
303.15	0.3068	0.0009
303.15	0.3991	0.0010
303.15	0.5082	0.0012
303.15	0.6040	0.0014
303.15	0.6992	0.0016
303.15	0.7994	0.0018
303.15	0.9038	0.0021
303.15	1.0000	0.0023
308.15	0.0000	0.0005
308.15	0.0997	0.0006
308.15	0.1994	0.0007
308.15	0.3068	0.0008
308.15	0.3991	0.0010
308.15	0.5082	0.0011
308.15	0.6040	0.0013
308.15	0.6992	0.0014
308.15	0.7994	0.0016
308.15	0.9038	0.0019
308.15	1.0000	0.0021
313.15	0.0000	0.0004
313.15	0.0997	0.0006
313.15	0.1994	0.0007
313.15	0.3068	0.0008
313.15	0.3991	0.0009
313.15	0.5082	0.0010
313.15	0.6040	0.0012
313.15	0.6992	0.0013
313.15	0.7994	0.0015
313.15	0.9038	0.0017
313.15	1.0000	0.0019
318.15	0.0000	0.0004
318.15	0.0997	0.0005
318.15	0.1994	0.0006
318.15	0.3068	0.0007
318.15	0.3991	0.0008
318.15	0.5082	0.0009
318.15	0.6040	0.0010
318.15	0.6992	0.0012
318.15	0.7994	0.0013
318.15	0.9038	0.0015
318.15	1.0000	0.0017
323.15	0.0000	0.0004
323.15	0.0997	0.0005
323.15	0.1994	0.0006
323.15	0.3068	0.0007
323.15	0.3991	0.0008
323.15	0.5082	0.0009
323.15	0.6040	0.0010
323.15	0.6992	0.0011
323.15	0.7994	0.0012
323.15	0.9038	0.0014
323.15	1.0000	0.0015

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0006
293.15	0.0997	0.0007
293.15	0.1994	0.0008
293.15	0.3068	0.0010
293.15	0.3991	0.0011
293.15	0.5082	0.0014
293.15	0.6040	0.0016
293.15	0.6992	0.0018
293.15	0.7994	0.0021
293.15	0.9038	0.0023
293.15	1.0000	0.0026
303.15	0.0000	0.0005
303.15	0.0997	0.0006
303.15	0.1994	0.0008
303.15	0.3068	0.0009
303.15	0.3991	0.0010
303.15	0.5082	0.0012
303.15	0.6040	0.0014
303.15	0.6992	0.0016
303.15	0.7994	0.0018
303.15	0.9038	0.0021
303.15	1.0000	0.0023
308.15	0.0000	0.0005
308.15	0.0997	0.0006
308.15	0.1994	0.0007
308.15	0.3068	0.0008
308.15	0.3991	0.0010
308.15	0.5082	0.0011
308.15	0.6040	0.0013
308.15	0.6992	0.0014
308.15	0.7994	0.0016
308.15	0.9038	0.0019
308.15	1.0000	0.0021
313.15	0.0000	0.0004
313.15	0.0997	0.0006
313.15	0.1994	0.0007
313.15	0.3068	0.0008
313.15	0.3991	0.0009
313.15	0.5082	0.0010
313.15	0.6040	0.0012
313.15	0.6992	0.0013
313.15	0.7994	0.0015
313.15	0.9038	0.0017
313.15	1.0000	0.0019
318.15	0.0000	0.0004
318.15	0.0997	0.0005
318.15	0.1994	0.0006
318.15	0.3068	0.0007
318.15	0.3991	0.0008
318.15	0.5082	0.0009
318.15	0.6040	0.0010
318.15	0.6992	0.0012
318.15	0.7994	0.0013
318.15	0.9038	0.0015
318.15	1.0000	0.0017
323.15	0.0000	0.0004
323.15	0.0997	0.0005
323.15	0.1994	0.0006
323.15	0.3068	0.0007
323.15	0.3991	0.0008
323.15	0.5082	0.0009
323.15	0.6040	0.0010
323.15	0.6992	0.0011
323.15	0.7994	0.0012
323.15	0.9038	0.0014
323.15	1.0000	0.0015

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	786.884
298.15	0.0997	791.339
298.15	0.1994	794.665
298.15	0.3068	797.503
298.15	0.3991	799.477
298.15	0.5082	801.494
298.15	0.6040	802.958
298.15	0.6992	804.13
298.15	0.7994	805.057
298.15	0.9038	805.689
298.15	1.0000	806.27
303.15	0.0000	782.158
303.15	0.0997	786.81
303.15	0.1994	790.266
303.15	0.3068	793.243
303.15	0.3991	795.305
303.15	0.5082	797.42
303.15	0.6040	798.956
303.15	0.6992	800.184
303.15	0.7994	801.155
303.15	0.9038	801.817
303.15	1.0000	802.42
308.15	0.0000	777.414
308.15	0.0997	782.263
308.15	0.1994	785.837
308.15	0.3068	788.95
308.15	0.3991	791.101
308.15	0.5082	793.315
308.15	0.6040	794.922
308.15	0.6992	796.169
308.15	0.7994	797.222
308.15	0.9038	797.914
308.15	1.0000	798.536
313.15	0.0000	772.64
313.15	0.0997	777.683
313.15	0.1994	781.397
313.15	0.3068	784.606
313.15	0.3991	786.863
313.15	0.5082	789.167
313.15	0.6040	790.889
313.15	0.6992	792.224
313.15	0.7994	793.273
313.15	0.9038	793.979
313.15	1.0000	794.617
318.15	0.0000	767.844
318.15	0.0997	773.076
318.15	0.1994	776.932
318.15	0.3068	780.263
318.15	0.3991	782.592
318.15	0.5082	784.996
318.15	0.6040	786.847
318.15	0.6992	788.248
318.15	0.7994	789.325
318.15	0.9038	789.993
318.15	1.0000	790.655
323.15	0.0000	763.028
323.15	0.0997	768.447
323.15	0.1994	772.448
323.15	0.3068	775.921
323.15	0.3991	778.306
323.15	0.5082	780.936
323.15	0.6040	782.762
323.15	0.6992	784.201
323.15	0.7994	785.373
323.15	0.9038	785.98
323.15	1.0000	786.645

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Fixed		Measured
Mole fraction of 1-Butanol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	791.34
0.0500	293.15	793.0
0.1000	293.15	794.55
0.1500	293.15	795.82
0.2000	293.15	797.09
0.2500	293.15	798.29
0.3000	293.15	799.4
0.4000	293.15	801.48
0.5000	293.15	803.28
0.6000	293.15	804.87
0.7000	293.15	806.38
0.8000	293.15	807.62
0.9000	293.15	808.83
1.0000	293.15	809.84
0.0000	298.15	786.68
0.0500	298.15	788.48
0.1000	298.15	790.15
0.1500	298.15	791.52
0.2000	298.15	792.81
0.2500	298.15	794.06
0.3000	298.15	795.23
0.4000	298.15	797.4
0.5000	298.15	799.27
0.6000	298.15	800.94
0.7000	298.15	802.48
0.8000	298.15	803.77
0.9000	298.15	804.99
1.0000	298.15	806.03
0.0000	303.15	781.96
0.0500	303.15	783.92
0.1000	303.15	785.69
0.1500	303.15	787.15
0.2000	303.15	788.52
0.2500	303.15	789.82
0.3000	303.15	791.01
0.4000	303.15	793.26
0.5000	303.15	795.21
0.6000	303.15	796.94
0.7000	303.15	798.57
0.8000	303.15	799.91
0.9000	303.15	801.12
1.0000	303.15	802.19
0.0000	308.15	777.21
0.0500	308.15	779.32
0.1000	308.15	781.19
0.1500	308.15	782.74
0.2000	308.15	784.19
0.2500	308.15	785.52
0.3000	308.15	786.78
0.4000	308.15	789.13
0.5000	308.15	791.18
0.6000	308.15	792.99
0.7000	308.15	794.64
0.8000	308.15	796.04
0.9000	308.15	797.29
1.0000	308.15	798.38

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	786.884
298.15	0.0997	791.339
298.15	0.1994	794.665
298.15	0.3068	797.503
298.15	0.3991	799.477
298.15	0.5082	801.494
298.15	0.6040	802.958
298.15	0.6992	804.13
298.15	0.7994	805.057
298.15	0.9038	805.689
298.15	1.0000	806.27
303.15	0.0000	782.158
303.15	0.0997	786.81
303.15	0.1994	790.266
303.15	0.3068	793.243
303.15	0.3991	795.305
303.15	0.5082	797.42
303.15	0.6040	798.956
303.15	0.6992	800.184
303.15	0.7994	801.155
303.15	0.9038	801.817
303.15	1.0000	802.42
308.15	0.0000	777.414
308.15	0.0997	782.263
308.15	0.1994	785.837
308.15	0.3068	788.95
308.15	0.3991	791.101
308.15	0.5082	793.315
308.15	0.6040	794.922
308.15	0.6992	796.169
308.15	0.7994	797.222
308.15	0.9038	797.914
308.15	1.0000	798.536
313.15	0.0000	772.64
313.15	0.0997	777.683
313.15	0.1994	781.397
313.15	0.3068	784.606
313.15	0.3991	786.863
313.15	0.5082	789.167
313.15	0.6040	790.889
313.15	0.6992	792.224
313.15	0.7994	793.273
313.15	0.9038	793.979
313.15	1.0000	794.617
318.15	0.0000	767.844
318.15	0.0997	773.076
318.15	0.1994	776.932
318.15	0.3068	780.263
318.15	0.3991	782.592
318.15	0.5082	784.996
318.15	0.6040	786.847
318.15	0.6992	788.248
318.15	0.7994	789.325
318.15	0.9038	789.993
318.15	1.0000	790.655
323.15	0.0000	763.028
323.15	0.0997	768.447
323.15	0.1994	772.448
323.15	0.3068	775.921
323.15	0.3991	778.306
323.15	0.5082	780.936
323.15	0.6040	782.762
323.15	0.6992	784.201
323.15	0.7994	785.373
323.15	0.9038	785.98
323.15	1.0000	786.645

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 102 (Liquid)

Fixed		Measured
Mole fraction of 1-Butanol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	791.34
0.0500	293.15	793.0
0.1000	293.15	794.55
0.1500	293.15	795.82
0.2000	293.15	797.09
0.2500	293.15	798.29
0.3000	293.15	799.4
0.4000	293.15	801.48
0.5000	293.15	803.28
0.6000	293.15	804.87
0.7000	293.15	806.38
0.8000	293.15	807.62
0.9000	293.15	808.83
1.0000	293.15	809.84
0.0000	298.15	786.68
0.0500	298.15	788.48
0.1000	298.15	790.15
0.1500	298.15	791.52
0.2000	298.15	792.81
0.2500	298.15	794.06
0.3000	298.15	795.23
0.4000	298.15	797.4
0.5000	298.15	799.27
0.6000	298.15	800.94
0.7000	298.15	802.48
0.8000	298.15	803.77
0.9000	298.15	804.99
1.0000	298.15	806.03
0.0000	303.15	781.96
0.0500	303.15	783.92
0.1000	303.15	785.69
0.1500	303.15	787.15
0.2000	303.15	788.52
0.2500	303.15	789.82
0.3000	303.15	791.01
0.4000	303.15	793.26
0.5000	303.15	795.21
0.6000	303.15	796.94
0.7000	303.15	798.57
0.8000	303.15	799.91
0.9000	303.15	801.12
1.0000	303.15	802.19
0.0000	308.15	777.21
0.0500	308.15	779.32
0.1000	308.15	781.19
0.1500	308.15	782.74
0.2000	308.15	784.19
0.2500	308.15	785.52
0.3000	308.15	786.78
0.4000	308.15	789.13
0.5000	308.15	791.18
0.6000	308.15	792.99
0.7000	308.15	794.64
0.8000	308.15	796.04
0.9000	308.15	797.29
1.0000	308.15	798.38

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1103.34
298.15	0.0997	1130.58
298.15	0.1994	1149.99
298.15	0.3068	1169.23
298.15	0.3991	1183.46
298.15	0.5082	1196.97
298.15	0.6040	1210.29
298.15	0.6992	1218.04
298.15	0.7994	1228.8
298.15	0.9038	1235.85
298.15	1.0000	1241.13
303.15	0.0000	1086.89
303.15	0.0997	1114.2
303.15	0.1994	1133.58
303.15	0.3068	1152.44
303.15	0.3991	1166.7
303.15	0.5082	1180.42
303.15	0.6040	1193.7
303.15	0.6992	1201.36
303.15	0.7994	1212.09
303.15	0.9038	1219.07
303.15	1.0000	1224.3
308.15	0.0000	1070.63
308.15	0.0997	1097.94
308.15	0.1994	1117.27
308.15	0.3068	1136.4
308.15	0.3991	1150.56
308.15	0.5082	1163.94
308.15	0.6040	1177.18
308.15	0.6992	1184.78
308.15	0.7994	1195.45
308.15	0.9038	1202.36
308.15	1.0000	1207.54
313.15	0.0000	1054.47
313.15	0.0997	1081.77
313.15	0.1994	1101.05
313.15	0.3068	1119.8
313.15	0.3991	1134.24
313.15	0.5082	1147.55
313.15	0.6040	1160.74
313.15	0.6992	1168.28
313.15	0.7994	1178.89
313.15	0.9038	1185.74
313.15	1.0000	1190.87
318.15	0.0000	1038.52
318.15	0.0997	1065.72
318.15	0.1994	1084.94
318.15	0.3068	1103.61
318.15	0.3991	1117.99
318.15	0.5082	1131.25
318.15	0.6040	1144.36
318.15	0.6992	1151.85
318.15	0.7994	1162.39
318.15	0.9038	1169.18
318.15	1.0000	1174.24
323.15	0.0000	1022.52
323.15	0.0997	1049.71
323.15	0.1994	1068.86
323.15	0.3068	1087.47
323.15	0.3991	1101.79
323.15	0.5082	1115.0
323.15	0.6040	1128.01
323.15	0.6992	1135.42
323.15	0.7994	1145.89
323.15	0.9038	1152.6
323.15	1.0000	1157.6

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1103.34
298.15	0.0997	1130.58
298.15	0.1994	1149.99
298.15	0.3068	1169.23
298.15	0.3991	1183.46
298.15	0.5082	1196.97
298.15	0.6040	1210.29
298.15	0.6992	1218.04
298.15	0.7994	1228.8
298.15	0.9038	1235.85
298.15	1.0000	1241.13
303.15	0.0000	1086.89
303.15	0.0997	1114.2
303.15	0.1994	1133.58
303.15	0.3068	1152.44
303.15	0.3991	1166.7
303.15	0.5082	1180.42
303.15	0.6040	1193.7
303.15	0.6992	1201.36
303.15	0.7994	1212.09
303.15	0.9038	1219.07
303.15	1.0000	1224.3
308.15	0.0000	1070.63
308.15	0.0997	1097.94
308.15	0.1994	1117.27
308.15	0.3068	1136.4
308.15	0.3991	1150.56
308.15	0.5082	1163.94
308.15	0.6040	1177.18
308.15	0.6992	1184.78
308.15	0.7994	1195.45
308.15	0.9038	1202.36
308.15	1.0000	1207.54
313.15	0.0000	1054.47
313.15	0.0997	1081.77
313.15	0.1994	1101.05
313.15	0.3068	1119.8
313.15	0.3991	1134.24
313.15	0.5082	1147.55
313.15	0.6040	1160.74
313.15	0.6992	1168.28
313.15	0.7994	1178.89
313.15	0.9038	1185.74
313.15	1.0000	1190.87
318.15	0.0000	1038.52
318.15	0.0997	1065.72
318.15	0.1994	1084.94
318.15	0.3068	1103.61
318.15	0.3991	1117.99
318.15	0.5082	1131.25
318.15	0.6040	1144.36
318.15	0.6992	1151.85
318.15	0.7994	1162.39
318.15	0.9038	1169.18
318.15	1.0000	1174.24
323.15	0.0000	1022.52
323.15	0.0997	1049.71
323.15	0.1994	1068.86
323.15	0.3068	1087.47
323.15	0.3991	1101.79
323.15	0.5082	1115.0
323.15	0.6040	1128.01
323.15	0.6992	1135.42
323.15	0.7994	1145.89
323.15	0.9038	1152.6
323.15	1.0000	1157.6

P [kPa] x T [K] x x1[mol/mol] [ref]

Fixed	Measured
P [kPa] - VLE	T [K] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid
773.591	463.15	1.0000
957.681	473.15	1.0000
1173.487	483.15	1.0000
1424.456	493.15	1.0000
1710.593	503.15	1.0000
2036.713	513.15	1.0000
2406.269	523.15	1.0000
2821.328	533.15	1.0000
3292.249	543.15	1.0000
3753.505	553.15	1.0000
4415.397	562.89	1.0000

P [kPa] x T [K] x x1[mol/mol] [ref]

Fixed	Measured
P [kPa] - VLE	T [K] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid
837.712	403.15	0.0000
1087.992	413.15	0.0000
1392.046	423.15	0.0000
1758.162	433.15	0.0000
2194.593	443.15	0.0000
2711.017	453.15	0.0000
3319.14	463.15	0.0000
4025.162	473.15	0.0000
4844.948	483.15	0.0000
5797.11	493.15	0.0000
6897.513	503.15	0.0000
8097.201	512.58	0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 1378.95 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
491.45	0.0000	0.0000
488.15	0.0270	0.0690
483.15	0.0690	0.1720
473.15	0.1570	0.3610
463.15	0.2570	0.5220
453.15	0.3800	0.6570
443.15	0.5360	0.7790
433.15	0.7360	0.8910
422.75	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 2757.91 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
531.75	0.0000	0.0000
528.15	0.0270	0.0580
523.15	0.0660	0.1380
513.15	0.1480	0.2920
503.15	0.2420	0.4400
493.15	0.3520	0.5770
483.15	0.4750	0.7000
473.15	0.6200	0.8120
463.15	0.8000	0.9120
453.95	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 4136.85 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
558.55	0.0000	0.0000
553.15	0.0420	0.0720
543.15	0.1260	0.2070
533.15	0.2110	0.3380
523.15	0.3050	0.4650
513.15	0.4090	0.5880
503.15	0.5260	0.7040
493.15	0.6670	0.8160
483.15	0.8360	0.9180
474.55	1.0000	1.0000

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Effect of composition and temperature variations on thermophysical properties of binary and ternary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate with 1-butanol and /or methanol
• Density and Excess Molar Volumes of 1-Butanol + Methanol + Electrolyte Systems in the Temperature Range (293.15 308.15) K