Mixture of n-Hexane + 1-Butanol

Datasets

1. η - Viscosity, Pa*s (2)
2. Excess molar enthalpy (molar enthalpy (4)
3. P_c - Critical pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (4)
5. c_sound,fluid - Speed of Sound, m/s (4)
6. γ - Surface tension liquid-gas, N/m (2)
7. T_c - Critical temperature, K (2)
8. Vapor Liquid Equilibrium at Constant Pressure (2)
9. Vapor Liquid Equilibrium at Constant Temperature
10. Excess molar volume, m3/mol (4)

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0003
0.0507	0.0003
0.1010	0.0003
0.1524	0.0004
0.2574	0.0004
0.3790	0.0005
0.4125	0.0005
0.4502	0.0006
0.5121	0.0007
0.6005	0.0009
0.7004	0.0011
0.8202	0.0015
0.8523	0.0017
0.8957	0.0019
0.9476	0.0022
1.0000	0.0026

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0003
0.0507	0.0003
0.1010	0.0003
0.1524	0.0004
0.2574	0.0004
0.3790	0.0005
0.4125	0.0005
0.4502	0.0006
0.5121	0.0007
0.6005	0.0009
0.7004	0.0011
0.8202	0.0015
0.8523	0.0017
0.8957	0.0019
0.9476	0.0022
1.0000	0.0026

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0199	0.2206
0.0399	0.2866
0.0500	0.3089
0.0600	0.3277
0.0799	0.3639
0.0999	0.3946
0.1499	0.4592
0.2000	0.5130
0.2500	0.5418
0.2999	0.5566
0.3500	0.5595
0.4001	0.5475
0.4501	0.5286
0.5000	0.5012
0.5500	0.4667
0.6001	0.4252
0.6501	0.3805
0.7000	0.3299
0.7501	0.2783
0.7999	0.2238
0.8500	0.1668
0.8999	0.1092
0.9500	0.0461

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2065	0.5366
0.2516	0.5394
0.4050	0.5546
0.5028	0.5031
0.6056	0.4397
0.7505	0.2754
0.8055	0.2181

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0199	0.2206
0.0399	0.2866
0.0500	0.3089
0.0600	0.3277
0.0799	0.3639
0.0999	0.3946
0.1499	0.4592
0.2000	0.5130
0.2500	0.5418
0.2999	0.5566
0.3500	0.5595
0.4001	0.5475
0.4501	0.5286
0.5000	0.5012
0.5500	0.4667
0.6001	0.4252
0.6501	0.3805
0.7000	0.3299
0.7501	0.2783
0.7999	0.2238
0.8500	0.1668
0.8999	0.1092
0.9500	0.0461

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.2065	0.5366
0.2516	0.5394
0.4050	0.5546
0.5028	0.5031
0.6056	0.4397
0.7505	0.2754
0.8055	0.2181

Critical pressure, kPa [ref]

Mass fraction of 1-Butanol (2) - Liquid	Critical pressure, kPa - Liquid
0.1000	3145.00
0.2000	3262.00
0.3000	3396.00
0.4000	3534.00
0.5000	3719.00
0.6000	3887.00
0.7000	4003.00
0.8000	4146.00
0.9000	4291.00

Critical pressure, kPa [ref]

Mass fraction of 1-Butanol (2) - Liquid	Critical pressure, kPa - Liquid
0.1000	3145.00
0.2000	3262.00
0.3000	3396.00
0.4000	3534.00
0.5000	3719.00
0.6000	3887.00
0.7000	4003.00
0.8000	4146.00
0.9000	4291.00

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0031	659.9
0.0476	664.4
0.1026	670.3
0.1225	672.4
0.1509	675.6
0.2261	684.4
0.2979	693.4
0.4965	720.9
0.6128	738.8
0.6817	750.1
0.7658	764.5
0.8937	788.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	655.072
298.15	0.0507	660.196
298.15	0.1010	665.602
298.15	0.1524	671.434
298.15	0.2574	684.29
298.15	0.3790	700.46
298.15	0.4125	705.163
298.15	0.4502	710.564
298.15	0.5121	719.663
298.15	0.6005	733.301
298.15	0.7004	749.66
298.15	0.8202	770.812
298.15	0.8523	776.78
298.15	0.8957	785.079
298.15	0.9476	795.298
298.15	1.0000	805.907
303.15	0.0000	650.369
303.15	0.0507	655.432
303.15	0.1010	660.733
303.15	0.1524	666.54
303.15	0.2574	679.54
303.15	0.3790	696.019
303.15	0.4125	700.869
303.15	0.4502	706.47
303.15	0.5121	715.869
303.15	0.6005	730.025
303.15	0.7004	746.763
303.15	0.8202	767.985
303.15	0.8523	773.953
303.15	0.8957	782.252
303.15	0.9476	792.462
303.15	1.0000	803.155
308.15	0.0000	645.767
308.15	0.0507	650.791
308.15	0.1010	656.143
308.15	0.1524	661.908
308.15	0.2574	674.857
308.15	0.3790	691.525
308.15	0.4125	696.345
308.15	0.4502	701.99
308.15	0.5121	711.606
308.15	0.6005	725.938
308.15	0.7004	742.943
308.15	0.8202	764.319
308.15	0.8523	770.292
308.15	0.8957	778.547
308.15	0.9476	788.743
308.15	1.0000	799.249

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0031	659.9
0.0476	664.4
0.1026	670.3
0.1225	672.4
0.1509	675.6
0.2261	684.4
0.2979	693.4
0.4965	720.9
0.6128	738.8
0.6817	750.1
0.7658	764.5
0.8937	788.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	655.072
298.15	0.0507	660.196
298.15	0.1010	665.602
298.15	0.1524	671.434
298.15	0.2574	684.29
298.15	0.3790	700.46
298.15	0.4125	705.163
298.15	0.4502	710.564
298.15	0.5121	719.663
298.15	0.6005	733.301
298.15	0.7004	749.66
298.15	0.8202	770.812
298.15	0.8523	776.78
298.15	0.8957	785.079
298.15	0.9476	795.298
298.15	1.0000	805.907
303.15	0.0000	650.369
303.15	0.0507	655.432
303.15	0.1010	660.733
303.15	0.1524	666.54
303.15	0.2574	679.54
303.15	0.3790	696.019
303.15	0.4125	700.869
303.15	0.4502	706.47
303.15	0.5121	715.869
303.15	0.6005	730.025
303.15	0.7004	746.763
303.15	0.8202	767.985
303.15	0.8523	773.953
303.15	0.8957	782.252
303.15	0.9476	792.462
303.15	1.0000	803.155
308.15	0.0000	645.767
308.15	0.0507	650.791
308.15	0.1010	656.143
308.15	0.1524	661.908
308.15	0.2574	674.857
308.15	0.3790	691.525
308.15	0.4125	696.345
308.15	0.4502	701.99
308.15	0.5121	711.606
308.15	0.6005	725.938
308.15	0.7004	742.943
308.15	0.8202	764.319
308.15	0.8523	770.292
308.15	0.8957	778.547
308.15	0.9476	788.743
308.15	1.0000	799.249

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
0.0031	1099.0
0.0476	1099.2
0.1026	1099.8
0.1225	1100.5
0.1509	1101.6
0.2261	1105.9
0.2979	1112.1
0.4965	1140.0
0.6128	1160.2
0.6817	1174.0
0.7658	1192.1
0.8937	1224.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1077.8
298.15	0.0507	1077.6
298.15	0.1010	1079.4
298.15	0.1524	1082.5
298.15	0.2574	1091.7
298.15	0.3790	1106.3
298.15	0.4125	1111.1
298.15	0.4502	1116.7
298.15	0.5121	1126.5
298.15	0.6005	1141.9
298.15	0.7004	1162.2
298.15	0.8202	1190.9
298.15	0.8523	1199.0
298.15	0.8957	1210.5
298.15	0.9476	1225.1
298.15	1.0000	1240.5
303.15	0.0000	1055.2
303.15	0.0507	1054.9
303.15	0.1010	1056.8
303.15	0.1524	1059.9
303.15	0.2574	1069.1
303.15	0.3790	1083.7
303.15	0.4125	1088.5
303.15	0.4502	1094.1
303.15	0.5121	1103.9
303.15	0.6005	1120.8
303.15	0.7004	1141.1
303.15	0.8202	1171.5
303.15	0.8523	1179.9
303.15	0.8957	1192.1
303.15	0.9476	1207.9
303.15	1.0000	1226.5
308.15	0.0000	1032.9
308.15	0.0507	1032.7
308.15	0.1010	1034.5
308.15	0.1524	1037.6
308.15	0.2574	1046.8
308.15	0.3790	1062.0
308.15	0.4125	1066.7
308.15	0.4502	1072.3
308.15	0.5121	1082.5
308.15	0.6005	1099.2
308.15	0.7004	1120.6
308.15	0.8202	1151.5
308.15	0.8523	1160.3
308.15	0.8957	1172.9
308.15	0.9476	1189.6
308.15	1.0000	1209.8

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
0.0031	1099.0
0.0476	1099.2
0.1026	1099.8
0.1225	1100.5
0.1509	1101.6
0.2261	1105.9
0.2979	1112.1
0.4965	1140.0
0.6128	1160.2
0.6817	1174.0
0.7658	1192.1
0.8937	1224.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0000	1077.8
298.15	0.0507	1077.6
298.15	0.1010	1079.4
298.15	0.1524	1082.5
298.15	0.2574	1091.7
298.15	0.3790	1106.3
298.15	0.4125	1111.1
298.15	0.4502	1116.7
298.15	0.5121	1126.5
298.15	0.6005	1141.9
298.15	0.7004	1162.2
298.15	0.8202	1190.9
298.15	0.8523	1199.0
298.15	0.8957	1210.5
298.15	0.9476	1225.1
298.15	1.0000	1240.5
303.15	0.0000	1055.2
303.15	0.0507	1054.9
303.15	0.1010	1056.8
303.15	0.1524	1059.9
303.15	0.2574	1069.1
303.15	0.3790	1083.7
303.15	0.4125	1088.5
303.15	0.4502	1094.1
303.15	0.5121	1103.9
303.15	0.6005	1120.8
303.15	0.7004	1141.1
303.15	0.8202	1171.5
303.15	0.8523	1179.9
303.15	0.8957	1192.1
303.15	0.9476	1207.9
303.15	1.0000	1226.5
308.15	0.0000	1032.9
308.15	0.0507	1032.7
308.15	0.1010	1034.5
308.15	0.1524	1037.6
308.15	0.2574	1046.8
308.15	0.3790	1062.0
308.15	0.4125	1066.7
308.15	0.4502	1072.3
308.15	0.5121	1082.5
308.15	0.6005	1099.2
308.15	0.7004	1120.6
308.15	0.8202	1151.5
308.15	0.8523	1160.3
308.15	0.8957	1172.9
308.15	0.9476	1189.6
308.15	1.0000	1209.8

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0519	0.0198
283.15	0.0875	0.0199
283.15	0.1959	0.0202
283.15	0.2999	0.0204
283.15	0.3990	0.0207
283.15	0.4914	0.0209
283.15	0.5974	0.0214
283.15	0.7044	0.0221
283.15	0.8027	0.0231
283.15	0.9088	0.0244
283.15	0.9530	0.0249
288.15	0.0519	0.0192
288.15	0.0875	0.0193
288.15	0.1959	0.0196
288.15	0.2999	0.0199
288.15	0.3990	0.0201
288.15	0.4914	0.0204
288.15	0.5974	0.0209
288.15	0.7044	0.0216
288.15	0.8027	0.0225
288.15	0.9088	0.0238
288.15	0.9530	0.0245
293.15	0.0519	0.0186
293.15	0.0875	0.0187
293.15	0.1959	0.0190
293.15	0.2999	0.0193
293.15	0.3990	0.0197
293.15	0.4914	0.0200
293.15	0.5974	0.0204
293.15	0.7044	0.0212
293.15	0.8027	0.0221
293.15	0.9088	0.0234
293.15	0.9530	0.0241
298.15	0.0519	0.0181
298.15	0.0875	0.0182
298.15	0.1959	0.0185
298.15	0.2999	0.0188
298.15	0.3990	0.0191
298.15	0.4914	0.0194
298.15	0.5974	0.0199
298.15	0.7044	0.0206
298.15	0.8027	0.0215
298.15	0.9088	0.0229
298.15	0.9530	0.0235
303.15	0.0519	0.0175
303.15	0.0875	0.0176
303.15	0.1959	0.0179
303.15	0.2999	0.0183
303.15	0.3990	0.0186
303.15	0.4914	0.0189
303.15	0.5974	0.0194
303.15	0.7044	0.0202
303.15	0.8027	0.0211
303.15	0.9088	0.0225
303.15	0.9530	0.0232
308.15	0.0519	0.0168
308.15	0.0875	0.0168
308.15	0.1959	0.0171
308.15	0.2999	0.0175
308.15	0.3990	0.0179
308.15	0.4914	0.0183
308.15	0.5974	0.0188
308.15	0.7044	0.0196
308.15	0.8027	0.0206
308.15	0.9088	0.0221
308.15	0.9530	0.0228
313.15	0.0519	0.0164
313.15	0.0875	0.0164
313.15	0.1959	0.0167
313.15	0.2999	0.0171
313.15	0.3990	0.0175
313.15	0.4914	0.0178
313.15	0.5974	0.0184
313.15	0.7044	0.0191
313.15	0.8027	0.0202
313.15	0.9088	0.0216
313.15	0.9530	0.0224

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0519	0.0198
283.15	0.0875	0.0199
283.15	0.1959	0.0202
283.15	0.2999	0.0204
283.15	0.3990	0.0207
283.15	0.4914	0.0209
283.15	0.5974	0.0214
283.15	0.7044	0.0221
283.15	0.8027	0.0231
283.15	0.9088	0.0244
283.15	0.9530	0.0249
288.15	0.0519	0.0192
288.15	0.0875	0.0193
288.15	0.1959	0.0196
288.15	0.2999	0.0199
288.15	0.3990	0.0201
288.15	0.4914	0.0204
288.15	0.5974	0.0209
288.15	0.7044	0.0216
288.15	0.8027	0.0225
288.15	0.9088	0.0238
288.15	0.9530	0.0245
293.15	0.0519	0.0186
293.15	0.0875	0.0187
293.15	0.1959	0.0190
293.15	0.2999	0.0193
293.15	0.3990	0.0197
293.15	0.4914	0.0200
293.15	0.5974	0.0204
293.15	0.7044	0.0212
293.15	0.8027	0.0221
293.15	0.9088	0.0234
293.15	0.9530	0.0241
298.15	0.0519	0.0181
298.15	0.0875	0.0182
298.15	0.1959	0.0185
298.15	0.2999	0.0188
298.15	0.3990	0.0191
298.15	0.4914	0.0194
298.15	0.5974	0.0199
298.15	0.7044	0.0206
298.15	0.8027	0.0215
298.15	0.9088	0.0229
298.15	0.9530	0.0235
303.15	0.0519	0.0175
303.15	0.0875	0.0176
303.15	0.1959	0.0179
303.15	0.2999	0.0183
303.15	0.3990	0.0186
303.15	0.4914	0.0189
303.15	0.5974	0.0194
303.15	0.7044	0.0202
303.15	0.8027	0.0211
303.15	0.9088	0.0225
303.15	0.9530	0.0232
308.15	0.0519	0.0168
308.15	0.0875	0.0168
308.15	0.1959	0.0171
308.15	0.2999	0.0175
308.15	0.3990	0.0179
308.15	0.4914	0.0183
308.15	0.5974	0.0188
308.15	0.7044	0.0196
308.15	0.8027	0.0206
308.15	0.9088	0.0221
308.15	0.9530	0.0228
313.15	0.0519	0.0164
313.15	0.0875	0.0164
313.15	0.1959	0.0167
313.15	0.2999	0.0171
313.15	0.3990	0.0175
313.15	0.4914	0.0178
313.15	0.5974	0.0184
313.15	0.7044	0.0191
313.15	0.8027	0.0202
313.15	0.9088	0.0216
313.15	0.9530	0.0224

Critical temperature, K [ref]

Mass fraction of 1-Butanol (2) - Liquid	Critical temperature, K - Liquid
0.1000	509.60
0.2000	511.50
0.3000	515.00
0.4000	521.20
0.5000	528.30
0.6000	534.40
0.7000	542.10
0.8000	548.50
0.9000	558.10

Critical temperature, K [ref]

Mass fraction of 1-Butanol (2) - Liquid	Critical temperature, K - Liquid
0.1000	509.60
0.2000	511.50
0.3000	515.00
0.4000	521.20
0.5000	528.30
0.6000	534.40
0.7000	542.10
0.8000	548.50
0.9000	558.10

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of n-Hexane (1) - Liquid	y1[mol/mol] of n-Hexane (1) - Vapour
380.55	0.0450	0.3350
373.65	0.0825	0.5200
369.55	0.1030	0.6070
366.05	0.1300	0.6530
361.15	0.1670	0.7320
355.95	0.2240	0.8000
353.85	0.2550	0.8250
352.5	0.2900	0.8350
348.95	0.3530	0.8750
346.35	0.4420	0.8975
345.25	0.5100	0.9025
344.05	0.5860	0.9125
343.55	0.6730	0.9220
342.2	0.8000	0.9300
342.15	0.8250	0.9310
342.05	0.8480	0.9340
341.75	0.8850	0.9400
341.65	0.9225	0.9475
341.45	0.9650	0.9680
341.45	0.9750	0.9730
341.65	0.9900	0.9870

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

T [K] - VLE	x1[mol/mol] of n-Hexane (1) - Liquid
373.05	0.0730
356.85	0.1920
350.75	0.2740
346.05	0.3740
343.95	0.4860
343.05	0.5470
342.15	0.6700
341.95	0.7680
341.75	0.8340
341.65	0.9010

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of n-Hexane (1) - Liquid	y1[mol/mol] of n-Hexane (1) - Vapour
8.306	0.0820	0.9010
12.879	0.1710	0.9390
15.385	0.2760	0.9500
18.145	0.4880	0.9640
19.025	0.6810	0.9690
19.305	0.7150	0.9720
19.545	0.7650	0.9760
19.945	0.8670	0.9840
19.972	0.8940	0.9870

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0155	5.7000e-08
0.0369	8.5000e-08
0.0511	9.7000e-08
0.0766	1.1300e-07
0.0993	1.2200e-07
0.1065	1.2800e-07
0.1499	1.3800e-07
0.1976	1.4200e-07
0.1981	1.4100e-07
0.1997	1.3700e-07
0.2497	1.3600e-07
0.2997	1.2700e-07
0.3437	1.1200e-07
0.3999	8.9000e-08
0.4016	8.8000e-08
0.4538	6.3000e-08
0.4995	4.1000e-08
0.5545	1.5000e-08
0.5960	-0.0000
0.5987	-0.0000
0.6008	-1.4000e-08
0.6575	-2.5000e-08
0.7003	-3.7000e-08
0.7525	-4.7000e-08
0.7994	-4.9000e-08
0.8006	-5.3000e-08
0.8007	-5.8000e-08
0.8481	-4.9000e-08
0.8998	-3.9000e-08
0.9025	-4.1000e-08
0.9496	-2.4000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.2007	1.4100e-07
0.2058	1.4000e-07
0.4008	8.8000e-08
0.4069	8.4000e-08
0.6008	-0.0000
0.6124	-1.0000e-08
0.7993	-5.1000e-08
0.8013	-5.3000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0155	5.7000e-08
0.0369	8.5000e-08
0.0511	9.7000e-08
0.0766	1.1300e-07
0.0993	1.2200e-07
0.1065	1.2800e-07
0.1499	1.3800e-07
0.1976	1.4200e-07
0.1981	1.4100e-07
0.1997	1.3700e-07
0.2497	1.3600e-07
0.2997	1.2700e-07
0.3437	1.1200e-07
0.3999	8.9000e-08
0.4016	8.8000e-08
0.4538	6.3000e-08
0.4995	4.1000e-08
0.5545	1.5000e-08
0.5960	-0.0000
0.5987	-0.0000
0.6008	-1.4000e-08
0.6575	-2.5000e-08
0.7003	-3.7000e-08
0.7525	-4.7000e-08
0.7994	-4.9000e-08
0.8006	-5.3000e-08
0.8007	-5.8000e-08
0.8481	-4.9000e-08
0.8998	-3.9000e-08
0.9025	-4.1000e-08
0.9496	-2.4000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.2007	1.4100e-07
0.2058	1.4000e-07
0.4008	8.8000e-08
0.4069	8.4000e-08
0.6008	-0.0000
0.6124	-1.0000e-08
0.7993	-5.1000e-08
0.8013	-5.3000e-08

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of 1-butanol, a tertiary amine (tri-n-butylamine or tri-n-octylamine) and n-hexane: Experimental results and ERAS-model calculations
• Study of densities, viscosities, and speeds of sound of binary liquid mixtures of butan-1-ol with n-alkanes (C6, C8, and C10) at T = (298.15, 303.15, and 308.15) K
• Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
• Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures