Mixture of 1-Hexanamine + 1-Butanol

Datasets

1. ρ_l - Mass density, kg/m3 (2)
2. Excess molar volume, m3/mol (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	768.637
288.15	0.0503	771.284
288.15	0.1108	774.579
288.15	0.1615	777.172
288.15	0.2004	779.327
288.15	0.2455	781.707
288.15	0.3004	784.53
288.15	0.4000	789.735
288.15	0.4802	793.847
288.15	0.6294	800.788
288.15	0.6999	803.655
288.15	0.7500	805.487
288.15	0.7997	807.332
288.15	0.8495	808.927
288.15	0.8994	810.567
288.15	0.9504	812.092
288.15	1.0000	813.373
293.15	0.0000	764.385
293.15	0.0503	767.06
293.15	0.1108	770.381
293.15	0.1615	772.994
293.15	0.2004	775.161
293.15	0.2455	777.556
293.15	0.3004	780.391
293.15	0.4000	785.619
293.15	0.4802	789.75
293.15	0.6294	796.75
293.15	0.6999	799.656
293.15	0.7500	801.517
293.15	0.7997	803.397
293.15	0.8495	805.024
293.15	0.8994	806.697
293.15	0.9504	808.261
293.15	1.0000	809.573
298.15	0.0000	760.128
298.15	0.0503	762.826
298.15	0.1108	766.172
298.15	0.1615	768.799
298.15	0.2004	770.98
298.15	0.2455	773.386
298.15	0.3004	776.235
298.15	0.4000	781.483
298.15	0.4802	785.637
298.15	0.6294	792.692
298.15	0.6999	795.637
298.15	0.7500	797.53
298.15	0.7997	799.441
298.15	0.8495	801.1
298.15	0.8994	802.808
298.15	0.9504	804.406
298.15	1.0000	805.762
303.15	0.0000	755.856
303.15	0.0503	758.576
303.15	0.1108	761.947
303.15	0.1615	764.593
303.15	0.2004	766.783
303.15	0.2455	769.201
303.15	0.3004	772.062
303.15	0.4000	777.33
303.15	0.4802	781.501
303.15	0.6294	788.612
303.15	0.6999	791.594
303.15	0.7500	793.517
303.15	0.7997	795.46
303.15	0.8495	797.154
303.15	0.8994	798.893
303.15	0.9504	800.528
303.15	1.0000	801.923
308.15	0.0000	751.573
308.15	0.0503	754.314
308.15	0.1108	757.705
308.15	0.1615	760.366
308.15	0.2004	762.567
308.15	0.2455	764.996
308.15	0.3004	767.867
308.15	0.4000	773.155
308.15	0.4802	777.345
308.15	0.6294	784.508
308.15	0.6999	787.526
308.15	0.7500	789.481
308.15	0.7997	791.45
308.15	0.8495	793.178
308.15	0.8994	794.95
308.15	0.9504	796.618
308.15	1.0000	798.053
313.15	0.0000	747.276
313.15	0.0503	750.035
313.15	0.1108	753.444
313.15	0.1615	756.118
313.15	0.2004	758.331
313.15	0.2455	760.77
313.15	0.3004	763.651
313.15	0.4000	768.956
313.15	0.4802	773.162
313.15	0.6294	780.377
313.15	0.6999	783.429
313.15	0.7500	785.41
313.15	0.7997	787.411
313.15	0.8495	789.169
313.15	0.8994	790.973
313.15	0.9504	792.674
313.15	1.0000	794.147
318.15	0.0000	742.962
318.15	0.0503	745.737
318.15	0.1108	749.165
318.15	0.1615	751.85
318.15	0.2004	754.072
318.15	0.2455	756.52
318.15	0.3004	759.41
318.15	0.4000	764.732
318.15	0.4802	768.953
318.15	0.6294	776.215
318.15	0.6999	779.299
318.15	0.7500	781.306
318.15	0.7997	783.336
318.15	0.8495	785.123
318.15	0.8994	786.956
318.15	0.9504	788.687
318.15	1.0000	790.231
323.15	0.0000	738.636
323.15	0.0503	741.427
323.15	0.1108	744.868
323.15	0.1615	747.565
323.15	0.2004	749.795
323.15	0.2455	752.247
323.15	0.3004	755.147
323.15	0.4000	760.481
323.15	0.4802	764.717
323.15	0.6294	772.02
323.15	0.6999	775.138
323.15	0.7500	777.172
323.15	0.7997	779.228
323.15	0.8495	781.043
323.15	0.8994	782.9
323.15	0.9504	784.663
323.15	1.0000	786.238

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	768.637
288.15	0.0503	771.284
288.15	0.1108	774.579
288.15	0.1615	777.172
288.15	0.2004	779.327
288.15	0.2455	781.707
288.15	0.3004	784.53
288.15	0.4000	789.735
288.15	0.4802	793.847
288.15	0.6294	800.788
288.15	0.6999	803.655
288.15	0.7500	805.487
288.15	0.7997	807.332
288.15	0.8495	808.927
288.15	0.8994	810.567
288.15	0.9504	812.092
288.15	1.0000	813.373
293.15	0.0000	764.385
293.15	0.0503	767.06
293.15	0.1108	770.381
293.15	0.1615	772.994
293.15	0.2004	775.161
293.15	0.2455	777.556
293.15	0.3004	780.391
293.15	0.4000	785.619
293.15	0.4802	789.75
293.15	0.6294	796.75
293.15	0.6999	799.656
293.15	0.7500	801.517
293.15	0.7997	803.397
293.15	0.8495	805.024
293.15	0.8994	806.697
293.15	0.9504	808.261
293.15	1.0000	809.573
298.15	0.0000	760.128
298.15	0.0503	762.826
298.15	0.1108	766.172
298.15	0.1615	768.799
298.15	0.2004	770.98
298.15	0.2455	773.386
298.15	0.3004	776.235
298.15	0.4000	781.483
298.15	0.4802	785.637
298.15	0.6294	792.692
298.15	0.6999	795.637
298.15	0.7500	797.53
298.15	0.7997	799.441
298.15	0.8495	801.1
298.15	0.8994	802.808
298.15	0.9504	804.406
298.15	1.0000	805.762
303.15	0.0000	755.856
303.15	0.0503	758.576
303.15	0.1108	761.947
303.15	0.1615	764.593
303.15	0.2004	766.783
303.15	0.2455	769.201
303.15	0.3004	772.062
303.15	0.4000	777.33
303.15	0.4802	781.501
303.15	0.6294	788.612
303.15	0.6999	791.594
303.15	0.7500	793.517
303.15	0.7997	795.46
303.15	0.8495	797.154
303.15	0.8994	798.893
303.15	0.9504	800.528
303.15	1.0000	801.923
308.15	0.0000	751.573
308.15	0.0503	754.314
308.15	0.1108	757.705
308.15	0.1615	760.366
308.15	0.2004	762.567
308.15	0.2455	764.996
308.15	0.3004	767.867
308.15	0.4000	773.155
308.15	0.4802	777.345
308.15	0.6294	784.508
308.15	0.6999	787.526
308.15	0.7500	789.481
308.15	0.7997	791.45
308.15	0.8495	793.178
308.15	0.8994	794.95
308.15	0.9504	796.618
308.15	1.0000	798.053
313.15	0.0000	747.276
313.15	0.0503	750.035
313.15	0.1108	753.444
313.15	0.1615	756.118
313.15	0.2004	758.331
313.15	0.2455	760.77
313.15	0.3004	763.651
313.15	0.4000	768.956
313.15	0.4802	773.162
313.15	0.6294	780.377
313.15	0.6999	783.429
313.15	0.7500	785.41
313.15	0.7997	787.411
313.15	0.8495	789.169
313.15	0.8994	790.973
313.15	0.9504	792.674
313.15	1.0000	794.147
318.15	0.0000	742.962
318.15	0.0503	745.737
318.15	0.1108	749.165
318.15	0.1615	751.85
318.15	0.2004	754.072
318.15	0.2455	756.52
318.15	0.3004	759.41
318.15	0.4000	764.732
318.15	0.4802	768.953
318.15	0.6294	776.215
318.15	0.6999	779.299
318.15	0.7500	781.306
318.15	0.7997	783.336
318.15	0.8495	785.123
318.15	0.8994	786.956
318.15	0.9504	788.687
318.15	1.0000	790.231
323.15	0.0000	738.636
323.15	0.0503	741.427
323.15	0.1108	744.868
323.15	0.1615	747.565
323.15	0.2004	749.795
323.15	0.2455	752.247
323.15	0.3004	755.147
323.15	0.4000	760.481
323.15	0.4802	764.717
323.15	0.6294	772.02
323.15	0.6999	775.138
323.15	0.7500	777.172
323.15	0.7997	779.228
323.15	0.8495	781.043
323.15	0.8994	782.9
323.15	0.9504	784.663
323.15	1.0000	786.238

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
288.15	0.0000	0.0000
288.15	0.0503	-1.7890e-07
288.15	0.1108	-3.9230e-07
288.15	0.1615	-5.2670e-07
288.15	0.2004	-6.4610e-07
288.15	0.2455	-7.5450e-07
288.15	0.3004	-8.5930e-07
288.15	0.4000	-1.0190e-06
288.15	0.4802	-1.0970e-06
288.15	0.6294	-1.0570e-06
288.15	0.6999	-9.5020e-07
288.15	0.7500	-8.3650e-07
288.15	0.7997	-7.1850e-07
288.15	0.8495	-5.6130e-07
288.15	0.8994	-4.0140e-07
288.15	0.9504	-2.1280e-07
288.15	1.0000	0.0000
293.15	0.0000	0.0000
293.15	0.0503	-1.8320e-07
293.15	0.1108	-4.0010e-07
293.15	0.1615	-5.3650e-07
293.15	0.2004	-6.5700e-07
293.15	0.2455	-7.6630e-07
293.15	0.3004	-8.7100e-07
293.15	0.4000	-1.0300e-06
293.15	0.4802	-1.1070e-06
293.15	0.6294	-1.0650e-06
293.15	0.6999	-9.5760e-07
293.15	0.7500	-8.4300e-07
293.15	0.7997	-7.2470e-07
293.15	0.8495	-5.6630e-07
293.15	0.8994	-4.0490e-07
293.15	0.9504	-2.1520e-07
293.15	1.0000	0.0000
298.15	0.0000	0.0000
298.15	0.0503	-1.8670e-07
298.15	0.1108	-4.0710e-07
298.15	0.1615	-5.4470e-07
298.15	0.2004	-6.6660e-07
298.15	0.2455	-7.7640e-07
298.15	0.3004	-8.8130e-07
298.15	0.4000	-1.0400e-06
298.15	0.4802	-1.1150e-06
298.15	0.6294	-1.0720e-06
298.15	0.6999	-9.6360e-07
298.15	0.7500	-8.4860e-07
298.15	0.7997	-7.2960e-07
298.15	0.8495	-5.6990e-07
298.15	0.8994	-4.0750e-07
298.15	0.9504	-2.1610e-07
298.15	1.0000	0.0000
303.15	0.0000	0.0000
303.15	0.0503	-1.9020e-07
303.15	0.1108	-4.1430e-07
303.15	0.1615	-5.5390e-07
303.15	0.2004	-6.7660e-07
303.15	0.2455	-7.8710e-07
303.15	0.3004	-8.9200e-07
303.15	0.4000	-1.0490e-06
303.15	0.4802	-1.1240e-06
303.15	0.6294	-1.0790e-06
303.15	0.6999	-9.6970e-07
303.15	0.7500	-8.5410e-07
303.15	0.7997	-7.3450e-07
303.15	0.8495	-5.7410e-07
303.15	0.8994	-4.1020e-07
303.15	0.9504	-2.1750e-07
303.15	1.0000	0.0000
308.15	0.0000	0.0000
308.15	0.0503	-1.9370e-07
308.15	0.1108	-4.2090e-07
308.15	0.1615	-5.6210e-07
308.15	0.2004	-6.8590e-07
308.15	0.2455	-7.9710e-07
308.15	0.3004	-9.0190e-07
308.15	0.4000	-1.0590e-06
308.15	0.4802	-1.1320e-06
308.15	0.6294	-1.0850e-06
308.15	0.6999	-9.7560e-07
308.15	0.7500	-8.5990e-07
308.15	0.7997	-7.3910e-07
308.15	0.8495	-5.7790e-07
308.15	0.8994	-4.1300e-07
308.15	0.9504	-2.1860e-07
308.15	1.0000	0.0000
313.15	0.0000	0.0000
313.15	0.0503	-1.9690e-07
313.15	0.1108	-4.2700e-07
313.15	0.1615	-5.6960e-07
313.15	0.2004	-6.9500e-07
313.15	0.2455	-8.0690e-07
313.15	0.3004	-9.1170e-07
313.15	0.4000	-1.0680e-06
313.15	0.4802	-1.1400e-06
313.15	0.6294	-1.0920e-06
313.15	0.6999	-9.8160e-07
313.15	0.7500	-8.6490e-07
313.15	0.7997	-7.4400e-07
313.15	0.8495	-5.8170e-07
313.15	0.8994	-4.1570e-07
313.15	0.9504	-2.1980e-07
313.15	1.0000	0.0000
318.15	0.0000	0.0000
318.15	0.0503	-1.9980e-07
318.15	0.1108	-4.3310e-07
318.15	0.1615	-5.7670e-07
318.15	0.2004	-7.0320e-07
318.15	0.2455	-8.1550e-07
318.15	0.3004	-9.2020e-07
318.15	0.4000	-1.0750e-06
318.15	0.4802	-1.1470e-06
318.15	0.6294	-1.0960e-06
318.15	0.6999	-9.8490e-07
318.15	0.7500	-8.6740e-07
318.15	0.7997	-7.4580e-07
318.15	0.8495	-5.8230e-07
318.15	0.8994	-4.1490e-07
318.15	0.9504	-2.1710e-07
318.15	1.0000	0.0000
323.15	0.0000	0.0000
323.15	0.0503	-2.0320e-07
323.15	0.1108	-4.3900e-07
323.15	0.1615	-5.8440e-07
323.15	0.2004	-7.1200e-07
323.15	0.2455	-8.2440e-07
323.15	0.3004	-9.2950e-07
323.15	0.4000	-1.0840e-06
323.15	0.4802	-1.1550e-06
323.15	0.6294	-1.1030e-06
323.15	0.6999	-9.9110e-07
323.15	0.7500	-8.7340e-07
323.15	0.7997	-7.5120e-07
323.15	0.8495	-5.8680e-07
323.15	0.8994	-4.1770e-07
323.15	0.9504	-2.1870e-07
323.15	1.0000	0.0000

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
288.15	0.0000	0.0000
288.15	0.0503	-1.7890e-07
288.15	0.1108	-3.9230e-07
288.15	0.1615	-5.2670e-07
288.15	0.2004	-6.4610e-07
288.15	0.2455	-7.5450e-07
288.15	0.3004	-8.5930e-07
288.15	0.4000	-1.0190e-06
288.15	0.4802	-1.0970e-06
288.15	0.6294	-1.0570e-06
288.15	0.6999	-9.5020e-07
288.15	0.7500	-8.3650e-07
288.15	0.7997	-7.1850e-07
288.15	0.8495	-5.6130e-07
288.15	0.8994	-4.0140e-07
288.15	0.9504	-2.1280e-07
288.15	1.0000	0.0000
293.15	0.0000	0.0000
293.15	0.0503	-1.8320e-07
293.15	0.1108	-4.0010e-07
293.15	0.1615	-5.3650e-07
293.15	0.2004	-6.5700e-07
293.15	0.2455	-7.6630e-07
293.15	0.3004	-8.7100e-07
293.15	0.4000	-1.0300e-06
293.15	0.4802	-1.1070e-06
293.15	0.6294	-1.0650e-06
293.15	0.6999	-9.5760e-07
293.15	0.7500	-8.4300e-07
293.15	0.7997	-7.2470e-07
293.15	0.8495	-5.6630e-07
293.15	0.8994	-4.0490e-07
293.15	0.9504	-2.1520e-07
293.15	1.0000	0.0000
298.15	0.0000	0.0000
298.15	0.0503	-1.8670e-07
298.15	0.1108	-4.0710e-07
298.15	0.1615	-5.4470e-07
298.15	0.2004	-6.6660e-07
298.15	0.2455	-7.7640e-07
298.15	0.3004	-8.8130e-07
298.15	0.4000	-1.0400e-06
298.15	0.4802	-1.1150e-06
298.15	0.6294	-1.0720e-06
298.15	0.6999	-9.6360e-07
298.15	0.7500	-8.4860e-07
298.15	0.7997	-7.2960e-07
298.15	0.8495	-5.6990e-07
298.15	0.8994	-4.0750e-07
298.15	0.9504	-2.1610e-07
298.15	1.0000	0.0000
303.15	0.0000	0.0000
303.15	0.0503	-1.9020e-07
303.15	0.1108	-4.1430e-07
303.15	0.1615	-5.5390e-07
303.15	0.2004	-6.7660e-07
303.15	0.2455	-7.8710e-07
303.15	0.3004	-8.9200e-07
303.15	0.4000	-1.0490e-06
303.15	0.4802	-1.1240e-06
303.15	0.6294	-1.0790e-06
303.15	0.6999	-9.6970e-07
303.15	0.7500	-8.5410e-07
303.15	0.7997	-7.3450e-07
303.15	0.8495	-5.7410e-07
303.15	0.8994	-4.1020e-07
303.15	0.9504	-2.1750e-07
303.15	1.0000	0.0000
308.15	0.0000	0.0000
308.15	0.0503	-1.9370e-07
308.15	0.1108	-4.2090e-07
308.15	0.1615	-5.6210e-07
308.15	0.2004	-6.8590e-07
308.15	0.2455	-7.9710e-07
308.15	0.3004	-9.0190e-07
308.15	0.4000	-1.0590e-06
308.15	0.4802	-1.1320e-06
308.15	0.6294	-1.0850e-06
308.15	0.6999	-9.7560e-07
308.15	0.7500	-8.5990e-07
308.15	0.7997	-7.3910e-07
308.15	0.8495	-5.7790e-07
308.15	0.8994	-4.1300e-07
308.15	0.9504	-2.1860e-07
308.15	1.0000	0.0000
313.15	0.0000	0.0000
313.15	0.0503	-1.9690e-07
313.15	0.1108	-4.2700e-07
313.15	0.1615	-5.6960e-07
313.15	0.2004	-6.9500e-07
313.15	0.2455	-8.0690e-07
313.15	0.3004	-9.1170e-07
313.15	0.4000	-1.0680e-06
313.15	0.4802	-1.1400e-06
313.15	0.6294	-1.0920e-06
313.15	0.6999	-9.8160e-07
313.15	0.7500	-8.6490e-07
313.15	0.7997	-7.4400e-07
313.15	0.8495	-5.8170e-07
313.15	0.8994	-4.1570e-07
313.15	0.9504	-2.1980e-07
313.15	1.0000	0.0000
318.15	0.0000	0.0000
318.15	0.0503	-1.9980e-07
318.15	0.1108	-4.3310e-07
318.15	0.1615	-5.7670e-07
318.15	0.2004	-7.0320e-07
318.15	0.2455	-8.1550e-07
318.15	0.3004	-9.2020e-07
318.15	0.4000	-1.0750e-06
318.15	0.4802	-1.1470e-06
318.15	0.6294	-1.0960e-06
318.15	0.6999	-9.8490e-07
318.15	0.7500	-8.6740e-07
318.15	0.7997	-7.4580e-07
318.15	0.8495	-5.8230e-07
318.15	0.8994	-4.1490e-07
318.15	0.9504	-2.1710e-07
318.15	1.0000	0.0000
323.15	0.0000	0.0000
323.15	0.0503	-2.0320e-07
323.15	0.1108	-4.3900e-07
323.15	0.1615	-5.8440e-07
323.15	0.2004	-7.1200e-07
323.15	0.2455	-8.2440e-07
323.15	0.3004	-9.2950e-07
323.15	0.4000	-1.0840e-06
323.15	0.4802	-1.1550e-06
323.15	0.6294	-1.1030e-06
323.15	0.6999	-9.9110e-07
323.15	0.7500	-8.7340e-07
323.15	0.7997	-7.5120e-07
323.15	0.8495	-5.8680e-07
323.15	0.8994	-4.1770e-07
323.15	0.9504	-2.1870e-07
323.15	1.0000	0.0000

Sources

• 1-Butanol + hexylamine + n-heptane at temperature range (288.15 323.15 K): Experimental density data, excess molar volumes determination and modeling with cubic EOS