Mixture of Pentane, 2,2,4-trimethyl- + 1-Pentanol

Datasets

1. Mole fraction (6)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (4)
4. P_vap - Vapor or sublimation pressure, kPa (4)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (4)
7. γ - Surface tension liquid-gas, N/m (2)

Mole fraction of 1-Pentanol (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Mole fraction of 1-Pentanol (2) - Gas
0.0000	0.0000
0.0492	0.0294
0.0997	0.0356
0.1482	0.0382
0.1990	0.0406
0.2483	0.0432
0.2997	0.0459
0.3495	0.0485
0.3999	0.0511
0.4006	0.0511
0.4500	0.0536
0.4508	0.0536
0.5003	0.0563
0.5011	0.0563
0.5504	0.0593
0.5509	0.0594
0.6002	0.0631
0.6012	0.0631
0.6515	0.0680
0.7011	0.0742
0.7511	0.0829
0.8007	0.0954
0.8472	0.1140
0.9007	0.1553
0.9507	0.2598
1.0000	1.0000

Mole fraction of Pentane, 2,2,4-trimethyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid
350.20	8.00	0.0000
350.20	18.00	0.0610
350.20	25.00	0.1210
350.20	33.00	0.2130
350.20	38.00	0.2840
350.20	46.00	0.5250
350.20	50.00	0.8140
350.20	51.00	0.8990
350.20	51.40	0.9490
350.20	51.60	0.9690
350.20	51.60	0.9900
350.20	51.60	1.0000
360.20	13.30	0.0000
360.20	37.80	0.1320
360.20	45.00	0.1920
360.20	51.50	0.2630
360.20	59.00	0.3930
360.20	67.10	0.6640
360.20	68.60	0.7370
360.20	69.40	0.7960
360.20	70.10	0.8390
360.20	70.90	0.8690
360.20	71.10	0.9310
360.20	71.10	0.9700
360.20	70.70	1.0000
370.20	21.00	0.0000
370.20	25.30	0.0100
370.20	30.90	0.0300
370.20	38.40	0.0610
370.20	47.10	0.1000
370.20	59.20	0.1720
370.20	68.30	0.2400
370.20	75.20	0.3130
370.20	87.80	0.5360
370.20	90.40	0.6160
370.20	93.70	0.7480
370.20	96.50	0.9390
370.20	96.50	0.9490
370.20	95.80	0.9890
370.20	95.00	1.0000

Mole fraction of Pentane, 2,2,4-trimethyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Gas
350.20	8.00	0.0000
350.20	18.00	0.5420
350.20	25.00	0.6900
350.20	33.00	0.7800
350.20	38.00	0.8160
350.20	46.00	0.8710
350.20	50.00	0.9140
350.20	51.00	0.9300
350.20	51.40	0.9550
350.20	51.60	0.9700
350.20	51.60	0.9880
350.20	51.60	1.0000
360.20	13.30	0.0000
360.20	37.80	0.6620
360.20	45.00	0.7280
360.20	51.50	0.7760
360.20	59.00	0.8210
360.20	67.10	0.8720
360.20	68.60	0.8770
360.20	69.40	0.8920
360.20	70.10	0.9020
360.20	70.90	0.9170
360.20	71.10	0.9380
360.20	71.10	0.9660
360.20	70.70	1.0000
370.20	21.00	0.0000
370.20	25.30	0.1220
370.20	30.90	0.2920
370.20	38.40	0.4460
370.20	47.10	0.5620
370.20	59.20	0.6660
370.20	68.30	0.7290
370.20	75.20	0.7660
370.20	87.80	0.8290
370.20	90.40	0.8430
370.20	93.70	0.8680
370.20	96.50	0.9380
370.20	96.50	0.9450
370.20	95.80	0.9860
370.20	95.00	1.0000

Mole fraction of 1-Pentanol (2) [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Mole fraction of 1-Pentanol (2) - Gas
0.0000	0.0000
0.0492	0.0294
0.0997	0.0356
0.1482	0.0382
0.1990	0.0406
0.2483	0.0432
0.2997	0.0459
0.3495	0.0485
0.3999	0.0511
0.4006	0.0511
0.4500	0.0536
0.4508	0.0536
0.5003	0.0563
0.5011	0.0563
0.5504	0.0593
0.5509	0.0594
0.6002	0.0631
0.6012	0.0631
0.6515	0.0680
0.7011	0.0742
0.7511	0.0829
0.8007	0.0954
0.8472	0.1140
0.9007	0.1553
0.9507	0.2598
1.0000	1.0000

Mole fraction of Pentane, 2,2,4-trimethyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid
350.20	8.00	0.0000
350.20	18.00	0.0610
350.20	25.00	0.1210
350.20	33.00	0.2130
350.20	38.00	0.2840
350.20	46.00	0.5250
350.20	50.00	0.8140
350.20	51.00	0.8990
350.20	51.40	0.9490
350.20	51.60	0.9690
350.20	51.60	0.9900
350.20	51.60	1.0000
360.20	13.30	0.0000
360.20	37.80	0.1320
360.20	45.00	0.1920
360.20	51.50	0.2630
360.20	59.00	0.3930
360.20	67.10	0.6640
360.20	68.60	0.7370
360.20	69.40	0.7960
360.20	70.10	0.8390
360.20	70.90	0.8690
360.20	71.10	0.9310
360.20	71.10	0.9700
360.20	70.70	1.0000
370.20	21.00	0.0000
370.20	25.30	0.0100
370.20	30.90	0.0300
370.20	38.40	0.0610
370.20	47.10	0.1000
370.20	59.20	0.1720
370.20	68.30	0.2400
370.20	75.20	0.3130
370.20	87.80	0.5360
370.20	90.40	0.6160
370.20	93.70	0.7480
370.20	96.50	0.9390
370.20	96.50	0.9490
370.20	95.80	0.9890
370.20	95.00	1.0000

Mole fraction of Pentane, 2,2,4-trimethyl- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Gas
350.20	8.00	0.0000
350.20	18.00	0.5420
350.20	25.00	0.6900
350.20	33.00	0.7800
350.20	38.00	0.8160
350.20	46.00	0.8710
350.20	50.00	0.9140
350.20	51.00	0.9300
350.20	51.40	0.9550
350.20	51.60	0.9700
350.20	51.60	0.9880
350.20	51.60	1.0000
360.20	13.30	0.0000
360.20	37.80	0.6620
360.20	45.00	0.7280
360.20	51.50	0.7760
360.20	59.00	0.8210
360.20	67.10	0.8720
360.20	68.60	0.8770
360.20	69.40	0.8920
360.20	70.10	0.9020
360.20	70.90	0.9170
360.20	71.10	0.9380
360.20	71.10	0.9660
360.20	70.70	1.0000
370.20	21.00	0.0000
370.20	25.30	0.1220
370.20	30.90	0.2920
370.20	38.40	0.4460
370.20	47.10	0.5620
370.20	59.20	0.6660
370.20	68.30	0.7290
370.20	75.20	0.7660
370.20	87.80	0.8290
370.20	90.40	0.8430
370.20	93.70	0.8680
370.20	96.50	0.9380
370.20	96.50	0.9450
370.20	95.80	0.9860
370.20	95.00	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0035
298.15	0.1004	0.0026
298.15	0.2003	0.0020
298.15	0.3000	0.0015
298.15	0.4000	0.0012
298.15	0.5000	0.0009
298.15	0.5999	0.0008
298.15	0.6998	0.0007
298.15	0.7999	0.0006
298.15	0.8996	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0030
303.15	0.1004	0.0023
303.15	0.2003	0.0018
303.15	0.3000	0.0014
303.15	0.4000	0.0011
303.15	0.5000	0.0009
303.15	0.5999	0.0007
303.15	0.6998	0.0006
303.15	0.7999	0.0006
303.15	0.8996	0.0005
303.15	1.0000	0.0005
308.15	0.0000	0.0026
308.15	0.1004	0.0020
308.15	0.2003	0.0016
308.15	0.3000	0.0012
308.15	0.4000	0.0010
308.15	0.5000	0.0008
308.15	0.5999	0.0007
308.15	0.6998	0.0006
308.15	0.7999	0.0005
308.15	0.8996	0.0005
308.15	1.0000	0.0004
313.15	0.0000	0.0023
313.15	0.1004	0.0018
313.15	0.2003	0.0014
313.15	0.3000	0.0011
313.15	0.4000	0.0009
313.15	0.5000	0.0007
313.15	0.5999	0.0006
313.15	0.6998	0.0005
313.15	0.7999	0.0005
313.15	0.8996	0.0004
313.15	1.0000	0.0004
318.15	0.0000	0.0020
318.15	0.1004	0.0016
318.15	0.2003	0.0013
318.15	0.3000	0.0010
318.15	0.4000	0.0008
318.15	0.5000	0.0007
318.15	0.5999	0.0006
318.15	0.6998	0.0005
318.15	0.7999	0.0005
318.15	0.8996	0.0004
318.15	1.0000	0.0004
323.15	0.0000	0.0018
323.15	0.1004	0.0014
323.15	0.2003	0.0011
323.15	0.3000	0.0009
323.15	0.4000	0.0007
323.15	0.5000	0.0006
323.15	0.5999	0.0005
323.15	0.6998	0.0005
323.15	0.7999	0.0004
323.15	0.8996	0.0004
323.15	1.0000	0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0035
298.15	0.1004	0.0026
298.15	0.2003	0.0020
298.15	0.3000	0.0015
298.15	0.4000	0.0012
298.15	0.5000	0.0009
298.15	0.5999	0.0008
298.15	0.6998	0.0007
298.15	0.7999	0.0006
298.15	0.8996	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0030
303.15	0.1004	0.0023
303.15	0.2003	0.0018
303.15	0.3000	0.0014
303.15	0.4000	0.0011
303.15	0.5000	0.0009
303.15	0.5999	0.0007
303.15	0.6998	0.0006
303.15	0.7999	0.0006
303.15	0.8996	0.0005
303.15	1.0000	0.0005
308.15	0.0000	0.0026
308.15	0.1004	0.0020
308.15	0.2003	0.0016
308.15	0.3000	0.0012
308.15	0.4000	0.0010
308.15	0.5000	0.0008
308.15	0.5999	0.0007
308.15	0.6998	0.0006
308.15	0.7999	0.0005
308.15	0.8996	0.0005
308.15	1.0000	0.0004
313.15	0.0000	0.0023
313.15	0.1004	0.0018
313.15	0.2003	0.0014
313.15	0.3000	0.0011
313.15	0.4000	0.0009
313.15	0.5000	0.0007
313.15	0.5999	0.0006
313.15	0.6998	0.0005
313.15	0.7999	0.0005
313.15	0.8996	0.0004
313.15	1.0000	0.0004
318.15	0.0000	0.0020
318.15	0.1004	0.0016
318.15	0.2003	0.0013
318.15	0.3000	0.0010
318.15	0.4000	0.0008
318.15	0.5000	0.0007
318.15	0.5999	0.0006
318.15	0.6998	0.0005
318.15	0.7999	0.0005
318.15	0.8996	0.0004
318.15	1.0000	0.0004
323.15	0.0000	0.0018
323.15	0.1004	0.0014
323.15	0.2003	0.0011
323.15	0.3000	0.0009
323.15	0.4000	0.0007
323.15	0.5000	0.0006
323.15	0.5999	0.0005
323.15	0.6998	0.0005
323.15	0.7999	0.0004
323.15	0.8996	0.0004
323.15	1.0000	0.0004

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-Pentanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.3764
0.0998	0.4747
0.1500	0.5313
0.1996	0.5546
0.2997	0.6019
0.3999	0.5912
0.4998	0.5511
0.5999	0.4561
0.7000	0.3806
0.8000	0.2636
0.8500	0.1974
0.9000	0.1342
0.9500	0.0627

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0000	0.0000
298.15	0.0508	0.3763
298.15	0.0999	0.4696
298.15	0.1501	0.5278
298.15	0.2008	0.5721
298.15	0.2500	0.5989
298.15	0.2999	0.6185
298.15	0.3516	0.6178
298.15	0.4025	0.6150
298.15	0.4514	0.6059
298.15	0.5025	0.5822
298.15	0.5516	0.5493
298.15	0.6025	0.5066
298.15	0.6513	0.4566
298.15	0.7015	0.3979
298.15	0.7512	0.3354
298.15	0.8003	0.2679
298.15	0.8503	0.2009
298.15	0.9008	0.1302
298.15	0.9503	0.0616
298.15	1.0000	0.0000
313.15	0.0000	0.0000
313.15	0.0510	0.5181
313.15	0.1003	0.6479
313.15	0.1506	0.7292
313.15	0.2019	0.7806
313.15	0.2512	0.8136
313.15	0.3012	0.8322
313.15	0.3517	0.8385
313.15	0.4026	0.8321
313.15	0.4514	0.8132
313.15	0.5026	0.7835
313.15	0.5517	0.7385
313.15	0.6026	0.6851
313.15	0.6513	0.6194
313.15	0.7016	0.5458
313.15	0.7513	0.4619
313.15	0.8003	0.3681
313.15	0.8503	0.2736
313.15	0.9008	0.1769
313.15	0.9503	0.0859
313.15	1.0000	0.0000

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-Pentanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.3764
0.0998	0.4747
0.1500	0.5313
0.1996	0.5546
0.2997	0.6019
0.3999	0.5912
0.4998	0.5511
0.5999	0.4561
0.7000	0.3806
0.8000	0.2636
0.8500	0.1974
0.9000	0.1342
0.9500	0.0627

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Pentanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0000	0.0000
298.15	0.0508	0.3763
298.15	0.0999	0.4696
298.15	0.1501	0.5278
298.15	0.2008	0.5721
298.15	0.2500	0.5989
298.15	0.2999	0.6185
298.15	0.3516	0.6178
298.15	0.4025	0.6150
298.15	0.4514	0.6059
298.15	0.5025	0.5822
298.15	0.5516	0.5493
298.15	0.6025	0.5066
298.15	0.6513	0.4566
298.15	0.7015	0.3979
298.15	0.7512	0.3354
298.15	0.8003	0.2679
298.15	0.8503	0.2009
298.15	0.9008	0.1302
298.15	0.9503	0.0616
298.15	1.0000	0.0000
313.15	0.0000	0.0000
313.15	0.0510	0.5181
313.15	0.1003	0.6479
313.15	0.1506	0.7292
313.15	0.2019	0.7806
313.15	0.2512	0.8136
313.15	0.3012	0.8322
313.15	0.3517	0.8385
313.15	0.4026	0.8321
313.15	0.4514	0.8132
313.15	0.5026	0.7835
313.15	0.5517	0.7385
313.15	0.6026	0.6851
313.15	0.6513	0.6194
313.15	0.7016	0.5458
313.15	0.7513	0.4619
313.15	0.8003	0.3681
313.15	0.8503	0.2736
313.15	0.9008	0.1769
313.15	0.9503	0.0859
313.15	1.0000	0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	12.95
0.0492	12.99
0.0997	12.88
0.1482	12.76
0.1990	12.62
0.2483	12.52
0.2997	12.31
0.3495	12.13
0.3999	11.93
0.4006	11.90
0.4500	11.71
0.4508	11.67
0.5003	11.45
0.5011	11.41
0.5504	11.14
0.5509	11.11
0.6002	10.78
0.6012	10.73
0.6515	10.28
0.7011	9.71
0.7511	8.98
0.8007	8.07
0.8472	6.98
0.9007	5.32
0.9507	3.35
1.0000	0.89

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.7012	9.79
0.2993	12.31

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	12.95
0.0492	12.99
0.0997	12.88
0.1482	12.76
0.1990	12.62
0.2483	12.52
0.2997	12.31
0.3495	12.13
0.3999	11.93
0.4006	11.90
0.4500	11.71
0.4508	11.67
0.5003	11.45
0.5011	11.41
0.5504	11.14
0.5509	11.11
0.6002	10.78
0.6012	10.73
0.6515	10.28
0.7011	9.71
0.7511	8.98
0.8007	8.07
0.8472	6.98
0.9007	5.32
0.9507	3.35
1.0000	0.89

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Pentanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.7012	9.79
0.2993	12.31

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Pentanol (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0501	1.3894
0.1000	1.3899
0.1499	1.3906
0.2017	1.3914
0.3001	1.393
0.4000	1.3948
0.5001	1.3967
0.6001	1.3987
0.7000	1.4008
0.7999	1.4029
0.8500	1.4041
0.9000	1.4053
0.9500	1.4065

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Pentanol (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0501	1.3894
0.1000	1.3899
0.1499	1.3906
0.2017	1.3914
0.3001	1.393
0.4000	1.3948
0.5001	1.3967
0.6001	1.3987
0.7000	1.4008
0.7999	1.4029
0.8500	1.4041
0.9000	1.4053
0.9500	1.4065

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Pentanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0501	691.14
0.1000	695.2
0.1499	699.5
0.2017	704.19
0.3001	713.84
0.4000	724.6
0.5001	736.36
0.6001	749.12
0.7000	762.91
0.7999	777.72
0.8500	785.54
0.9000	793.63
0.9500	801.98

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	810.59
298.15	0.1004	794.33
298.15	0.2003	778.35
298.15	0.3000	763.77
298.15	0.4000	749.96
298.15	0.5000	737.18
298.15	0.5999	725.64
298.15	0.6998	714.97
298.15	0.7999	705.08
298.15	0.8996	696.03
298.15	1.0000	687.82
303.15	0.0000	807.89
303.15	0.1004	790.55
303.15	0.2003	774.49
303.15	0.3000	759.83
303.15	0.4000	745.97
303.15	0.5000	733.13
303.15	0.5999	721.55
303.15	0.6998	710.84
303.15	0.7999	700.93
303.15	0.8996	691.85
303.15	1.0000	683.68
308.15	0.0000	804.16
308.15	0.1004	786.73
308.15	0.2003	770.6
308.15	0.3000	755.86
308.15	0.4000	741.94
308.15	0.5000	729.05
308.15	0.5999	717.43
308.15	0.6998	706.68
308.15	0.7999	696.74
308.15	0.8996	687.64
308.15	1.0000	679.52
313.15	0.0000	800.4
313.15	0.1004	782.88
313.15	0.2003	766.66
313.15	0.3000	751.85
313.15	0.4000	737.87
313.15	0.5000	724.94
313.15	0.5999	713.27
313.15	0.6998	702.49
313.15	0.7999	692.51
313.15	0.8996	683.4
313.15	1.0000	675.32
318.15	0.0000	796.59
318.15	0.1004	778.99
318.15	0.2003	762.69
318.15	0.3000	747.8
318.15	0.4000	733.76
318.15	0.5000	720.78
318.15	0.5999	709.06
318.15	0.6998	698.25
318.15	0.7999	688.24
318.15	0.8996	679.11
318.15	1.0000	671.1
323.15	0.0000	792.75
323.15	0.1004	775.05
323.15	0.2003	758.67
323.15	0.3000	743.71
323.15	0.4000	729.61
323.15	0.5000	716.58
323.15	0.5999	704.82
323.15	0.6998	693.98
323.15	0.7999	683.93
323.15	0.8996	674.79
323.15	1.0000	666.85

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Pentanol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0501	691.14
0.1000	695.2
0.1499	699.5
0.2017	704.19
0.3001	713.84
0.4000	724.6
0.5001	736.36
0.6001	749.12
0.7000	762.91
0.7999	777.72
0.8500	785.54
0.9000	793.63
0.9500	801.98

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	810.59
298.15	0.1004	794.33
298.15	0.2003	778.35
298.15	0.3000	763.77
298.15	0.4000	749.96
298.15	0.5000	737.18
298.15	0.5999	725.64
298.15	0.6998	714.97
298.15	0.7999	705.08
298.15	0.8996	696.03
298.15	1.0000	687.82
303.15	0.0000	807.89
303.15	0.1004	790.55
303.15	0.2003	774.49
303.15	0.3000	759.83
303.15	0.4000	745.97
303.15	0.5000	733.13
303.15	0.5999	721.55
303.15	0.6998	710.84
303.15	0.7999	700.93
303.15	0.8996	691.85
303.15	1.0000	683.68
308.15	0.0000	804.16
308.15	0.1004	786.73
308.15	0.2003	770.6
308.15	0.3000	755.86
308.15	0.4000	741.94
308.15	0.5000	729.05
308.15	0.5999	717.43
308.15	0.6998	706.68
308.15	0.7999	696.74
308.15	0.8996	687.64
308.15	1.0000	679.52
313.15	0.0000	800.4
313.15	0.1004	782.88
313.15	0.2003	766.66
313.15	0.3000	751.85
313.15	0.4000	737.87
313.15	0.5000	724.94
313.15	0.5999	713.27
313.15	0.6998	702.49
313.15	0.7999	692.51
313.15	0.8996	683.4
313.15	1.0000	675.32
318.15	0.0000	796.59
318.15	0.1004	778.99
318.15	0.2003	762.69
318.15	0.3000	747.8
318.15	0.4000	733.76
318.15	0.5000	720.78
318.15	0.5999	709.06
318.15	0.6998	698.25
318.15	0.7999	688.24
318.15	0.8996	679.11
318.15	1.0000	671.1
323.15	0.0000	792.75
323.15	0.1004	775.05
323.15	0.2003	758.67
323.15	0.3000	743.71
323.15	0.4000	729.61
323.15	0.5000	716.58
323.15	0.5999	704.82
323.15	0.6998	693.98
323.15	0.7999	683.93
323.15	0.8996	674.79
323.15	1.0000	666.85

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0253
298.15	0.1004	0.0238
298.15	0.2003	0.0225
298.15	0.3000	0.0217
298.15	0.4000	0.0210
298.15	0.5000	0.0203
298.15	0.5999	0.0198
298.15	0.6998	0.0194
298.15	0.7999	0.0189
298.15	0.8996	0.0186
298.15	1.0000	0.0183
303.15	0.0000	0.0249
303.15	0.1004	0.0233
303.15	0.2003	0.0221
303.15	0.3000	0.0212
303.15	0.4000	0.0205
303.15	0.5000	0.0198
303.15	0.5999	0.0193
303.15	0.6998	0.0189
303.15	0.7999	0.0185
303.15	0.8996	0.0182
303.15	1.0000	0.0179
308.15	0.0000	0.0245
308.15	0.1004	0.0228
308.15	0.2003	0.0216
308.15	0.3000	0.0207
308.15	0.4000	0.0200
308.15	0.5000	0.0193
308.15	0.5999	0.0188
308.15	0.6998	0.0184
308.15	0.7999	0.0180
308.15	0.8996	0.0177
308.15	1.0000	0.0174
313.15	0.0000	0.0240
313.15	0.1004	0.0224
313.15	0.2003	0.0211
313.15	0.3000	0.0202
313.15	0.4000	0.0195
313.15	0.5000	0.0188
313.15	0.5999	0.0183
313.15	0.6998	0.0180
313.15	0.7999	0.0176
313.15	0.8996	0.0174
313.15	1.0000	0.0171
318.15	0.0000	0.0237
318.15	0.1004	0.0220
318.15	0.2003	0.0206
318.15	0.3000	0.0197
318.15	0.4000	0.0190
318.15	0.5000	0.0183
318.15	0.5999	0.0178
318.15	0.6998	0.0175
318.15	0.7999	0.0171
318.15	0.8996	0.0169
318.15	1.0000	0.0166
323.15	0.0000	0.0232
323.15	0.1004	0.0215
323.15	0.2003	0.0201
323.15	0.3000	0.0193
323.15	0.4000	0.0185
323.15	0.5000	0.0178
323.15	0.5999	0.0173
323.15	0.6998	0.0170
323.15	0.7999	0.0167
323.15	0.8996	0.0164
323.15	1.0000	0.0162

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0253
298.15	0.1004	0.0238
298.15	0.2003	0.0225
298.15	0.3000	0.0217
298.15	0.4000	0.0210
298.15	0.5000	0.0203
298.15	0.5999	0.0198
298.15	0.6998	0.0194
298.15	0.7999	0.0189
298.15	0.8996	0.0186
298.15	1.0000	0.0183
303.15	0.0000	0.0249
303.15	0.1004	0.0233
303.15	0.2003	0.0221
303.15	0.3000	0.0212
303.15	0.4000	0.0205
303.15	0.5000	0.0198
303.15	0.5999	0.0193
303.15	0.6998	0.0189
303.15	0.7999	0.0185
303.15	0.8996	0.0182
303.15	1.0000	0.0179
308.15	0.0000	0.0245
308.15	0.1004	0.0228
308.15	0.2003	0.0216
308.15	0.3000	0.0207
308.15	0.4000	0.0200
308.15	0.5000	0.0193
308.15	0.5999	0.0188
308.15	0.6998	0.0184
308.15	0.7999	0.0180
308.15	0.8996	0.0177
308.15	1.0000	0.0174
313.15	0.0000	0.0240
313.15	0.1004	0.0224
313.15	0.2003	0.0211
313.15	0.3000	0.0202
313.15	0.4000	0.0195
313.15	0.5000	0.0188
313.15	0.5999	0.0183
313.15	0.6998	0.0180
313.15	0.7999	0.0176
313.15	0.8996	0.0174
313.15	1.0000	0.0171
318.15	0.0000	0.0237
318.15	0.1004	0.0220
318.15	0.2003	0.0206
318.15	0.3000	0.0197
318.15	0.4000	0.0190
318.15	0.5000	0.0183
318.15	0.5999	0.0178
318.15	0.6998	0.0175
318.15	0.7999	0.0171
318.15	0.8996	0.0169
318.15	1.0000	0.0166
323.15	0.0000	0.0232
323.15	0.1004	0.0215
323.15	0.2003	0.0201
323.15	0.3000	0.0193
323.15	0.4000	0.0185
323.15	0.5000	0.0178
323.15	0.5999	0.0173
323.15	0.6998	0.0170
323.15	0.7999	0.0167
323.15	0.8996	0.0164
323.15	1.0000	0.0162

Sources

• Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
• Vapour liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
• Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
• Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K