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

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (4)
4. P_vap - Vapor or sublimation pressure, kPa (2)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (8)
7. γ - Surface tension liquid-gas, N/m (2)

Mole fraction of 1-Propanol (1) [ref]

Operational condition: Temperature, K = 303.15 (Gas)

Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of 1-Propanol (1) - Gas
0.0223	0.1552
0.0394	0.1771
0.0590	0.1943
0.0794	0.2084
0.1188	0.2292
0.1702	0.2452
0.2292	0.2558
0.2896	0.2617
0.3515	0.2723
0.4095	0.2746
0.4702	0.2845
0.5297	0.2925
0.5894	0.2967
0.6497	0.3073
0.7106	0.3226
0.7707	0.3444
0.8298	0.3776
0.8804	0.4284
0.9200	0.5031
0.9404	0.5579
0.9604	0.6394
0.9797	0.7595

Mole fraction of 1-Propanol (1) [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of 1-Propanol (1) - Gas
0.0475	0.1888
0.0539	0.1948
0.0759	0.2467
0.1262	0.2719
0.1265	0.2742
0.1507	0.2903
0.1514	0.2906
0.1966	0.3083
0.2416	0.3186
0.2751	0.3206
0.2784	0.3294
0.3925	0.3317
0.3997	0.3371
0.4225	0.3534
0.4294	0.3596
0.5060	0.3491
0.5673	0.3679
0.6061	0.3707
0.6248	0.3634
0.6810	0.3897
0.7875	0.4062
0.9182	0.5673

Mole fraction of 1-Propanol (1) [ref]

Operational condition: Temperature, K = 303.15 (Gas)

Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of 1-Propanol (1) - Gas
0.0223	0.1552
0.0394	0.1771
0.0590	0.1943
0.0794	0.2084
0.1188	0.2292
0.1702	0.2452
0.2292	0.2558
0.2896	0.2617
0.3515	0.2723
0.4095	0.2746
0.4702	0.2845
0.5297	0.2925
0.5894	0.2967
0.6497	0.3073
0.7106	0.3226
0.7707	0.3444
0.8298	0.3776
0.8804	0.4284
0.9200	0.5031
0.9404	0.5579
0.9604	0.6394
0.9797	0.7595

Mole fraction of 1-Propanol (1) [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Mole fraction of 1-Propanol (1) - Gas
0.0475	0.1888
0.0539	0.1948
0.0759	0.2467
0.1262	0.2719
0.1265	0.2742
0.1507	0.2903
0.1514	0.2906
0.1966	0.3083
0.2416	0.3186
0.2751	0.3206
0.2784	0.3294
0.3925	0.3317
0.3997	0.3371
0.4225	0.3534
0.4294	0.3596
0.5060	0.3491
0.5673	0.3679
0.6061	0.3707
0.6248	0.3634
0.6810	0.3897
0.7875	0.4062
0.9182	0.5673

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0020
298.15	0.1000	0.0015
298.15	0.2000	0.0012
298.15	0.3000	0.0010
298.15	0.4000	0.0008
298.15	0.4999	0.0007
298.15	0.5996	0.0006
298.15	0.6998	0.0006
298.15	0.7995	0.0005
298.15	0.9000	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0017
303.15	0.1000	0.0014
303.15	0.2000	0.0011
303.15	0.3000	0.0009
303.15	0.4000	0.0008
303.15	0.4999	0.0007
303.15	0.5996	0.0006
303.15	0.6998	0.0005
303.15	0.7995	0.0005
303.15	0.9000	0.0005
303.15	1.0000	0.0005
308.15	0.0000	0.0015
308.15	0.1000	0.0012
308.15	0.2000	0.0010
308.15	0.3000	0.0008
308.15	0.4000	0.0007
308.15	0.4999	0.0006
308.15	0.5996	0.0005
308.15	0.6998	0.0005
308.15	0.7995	0.0005
308.15	0.9000	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0014
313.15	0.1000	0.0011
313.15	0.2000	0.0009
313.15	0.3000	0.0008
313.15	0.4000	0.0006
313.15	0.4999	0.0006
313.15	0.5996	0.0005
313.15	0.6998	0.0005
313.15	0.7995	0.0004
313.15	0.9000	0.0004
313.15	1.0000	0.0004
318.15	0.0000	0.0012
318.15	0.1000	0.0010
318.15	0.2000	0.0008
318.15	0.3000	0.0007
318.15	0.4000	0.0006
318.15	0.4999	0.0005
318.15	0.5996	0.0005
318.15	0.6998	0.0004
318.15	0.7995	0.0004
318.15	0.9000	0.0004
318.15	1.0000	0.0004
323.15	0.0000	0.0011
323.15	0.1000	0.0009
323.15	0.2000	0.0008
323.15	0.3000	0.0006
323.15	0.4000	0.0006
323.15	0.4999	0.0005
323.15	0.5996	0.0004
323.15	0.6998	0.0004
323.15	0.7995	0.0004
323.15	0.9000	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- (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0020
298.15	0.1000	0.0015
298.15	0.2000	0.0012
298.15	0.3000	0.0010
298.15	0.4000	0.0008
298.15	0.4999	0.0007
298.15	0.5996	0.0006
298.15	0.6998	0.0006
298.15	0.7995	0.0005
298.15	0.9000	0.0005
298.15	1.0000	0.0005
303.15	0.0000	0.0017
303.15	0.1000	0.0014
303.15	0.2000	0.0011
303.15	0.3000	0.0009
303.15	0.4000	0.0008
303.15	0.4999	0.0007
303.15	0.5996	0.0006
303.15	0.6998	0.0005
303.15	0.7995	0.0005
303.15	0.9000	0.0005
303.15	1.0000	0.0005
308.15	0.0000	0.0015
308.15	0.1000	0.0012
308.15	0.2000	0.0010
308.15	0.3000	0.0008
308.15	0.4000	0.0007
308.15	0.4999	0.0006
308.15	0.5996	0.0005
308.15	0.6998	0.0005
308.15	0.7995	0.0005
308.15	0.9000	0.0004
308.15	1.0000	0.0004
313.15	0.0000	0.0014
313.15	0.1000	0.0011
313.15	0.2000	0.0009
313.15	0.3000	0.0008
313.15	0.4000	0.0006
313.15	0.4999	0.0006
313.15	0.5996	0.0005
313.15	0.6998	0.0005
313.15	0.7995	0.0004
313.15	0.9000	0.0004
313.15	1.0000	0.0004
318.15	0.0000	0.0012
318.15	0.1000	0.0010
318.15	0.2000	0.0008
318.15	0.3000	0.0007
318.15	0.4000	0.0006
318.15	0.4999	0.0005
318.15	0.5996	0.0005
318.15	0.6998	0.0004
318.15	0.7995	0.0004
318.15	0.9000	0.0004
318.15	1.0000	0.0004
323.15	0.0000	0.0011
323.15	0.1000	0.0009
323.15	0.2000	0.0008
323.15	0.3000	0.0006
323.15	0.4000	0.0006
323.15	0.4999	0.0005
323.15	0.5996	0.0004
323.15	0.6998	0.0004
323.15	0.7995	0.0004
323.15	0.9000	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-Propanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0516	0.4077
0.1000	0.5250
0.1500	0.5598
0.2001	0.6094
0.3001	0.6544
0.4001	0.6533
0.5002	0.6025
0.6001	0.5251
0.7048	0.4056
0.8000	0.2967
0.8500	0.2348
0.8998	0.1622
0.9499	0.0854

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0500	0.0870
298.15	0.1001	0.1670
298.15	0.1505	0.2410
298.15	0.2003	0.3080
298.15	0.2501	0.3690
298.15	0.2999	0.4270
298.15	0.3499	0.4790
298.15	0.4006	0.5260
298.15	0.4503	0.5670
298.15	0.4997	0.6020
298.15	0.5504	0.6300
298.15	0.5998	0.6480
298.15	0.6500	0.6560
298.15	0.7008	0.6550
298.15	0.7502	0.6400
298.15	0.7994	0.6110
298.15	0.8499	0.5660
298.15	0.8998	0.5020
298.15	0.9506	0.3920
313.15	0.0500	0.1180
313.15	0.1000	0.2270
313.15	0.1504	0.3280
313.15	0.2002	0.4190
313.15	0.2500	0.5040
313.15	0.2997	0.5810
313.15	0.3498	0.6530
313.15	0.4004	0.7180
313.15	0.4502	0.7720
313.15	0.4995	0.8170
313.15	0.5503	0.8510
313.15	0.5997	0.8750
313.15	0.6498	0.8830
313.15	0.7007	0.8810
313.15	0.7501	0.8620
313.15	0.7993	0.8260
313.15	0.8499	0.7690
313.15	0.8998	0.6840
313.15	0.9506	0.5180

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-Propanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0516	0.4077
0.1000	0.5250
0.1500	0.5598
0.2001	0.6094
0.3001	0.6544
0.4001	0.6533
0.5002	0.6025
0.6001	0.5251
0.7048	0.4056
0.8000	0.2967
0.8500	0.2348
0.8998	0.1622
0.9499	0.0854

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

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0500	0.0870
298.15	0.1001	0.1670
298.15	0.1505	0.2410
298.15	0.2003	0.3080
298.15	0.2501	0.3690
298.15	0.2999	0.4270
298.15	0.3499	0.4790
298.15	0.4006	0.5260
298.15	0.4503	0.5670
298.15	0.4997	0.6020
298.15	0.5504	0.6300
298.15	0.5998	0.6480
298.15	0.6500	0.6560
298.15	0.7008	0.6550
298.15	0.7502	0.6400
298.15	0.7994	0.6110
298.15	0.8499	0.5660
298.15	0.8998	0.5020
298.15	0.9506	0.3920
313.15	0.0500	0.1180
313.15	0.1000	0.2270
313.15	0.1504	0.3280
313.15	0.2002	0.4190
313.15	0.2500	0.5040
313.15	0.2997	0.5810
313.15	0.3498	0.6530
313.15	0.4004	0.7180
313.15	0.4502	0.7720
313.15	0.4995	0.8170
313.15	0.5503	0.8510
313.15	0.5997	0.8750
313.15	0.6498	0.8830
313.15	0.7007	0.8810
313.15	0.7501	0.8620
313.15	0.7993	0.8260
313.15	0.8499	0.7690
313.15	0.8998	0.6840
313.15	0.9506	0.5180

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0475	9.00
0.0539	19.13
0.0759	19.93
0.1262	20.53
0.1265	20.53
0.1507	20.66
0.1514	20.66
0.1966	20.93
0.2416	21.06
0.2751	21.06
0.2784	20.93
0.3925	21.13
0.3997	21.06
0.4225	21.00
0.4294	21.00
0.5060	20.93
0.5673	20.66
0.6061	20.66
0.6248	20.33
0.6810	20.27
0.7875	19.47
0.9182	15.47

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0475	9.00
0.0539	19.13
0.0759	19.93
0.1262	20.53
0.1265	20.53
0.1507	20.66
0.1514	20.66
0.1966	20.93
0.2416	21.06
0.2751	21.06
0.2784	20.93
0.3925	21.13
0.3997	21.06
0.4225	21.00
0.4294	21.00
0.5060	20.93
0.5673	20.66
0.6061	20.66
0.6248	20.33
0.6810	20.27
0.7875	19.47
0.9182	15.47

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0502	1.3885
0.1002	1.3882
0.1504	1.3879
0.1999	1.3876
0.3000	1.3871
0.3999	1.3867
0.5000	1.3863
0.6001	1.3858
0.7000	1.3853
0.7999	1.3846
0.8500	1.3843
0.9000	1.3839
0.9501	1.3835

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0502	1.3885
0.1002	1.3882
0.1504	1.3879
0.1999	1.3876
0.3000	1.3871
0.3999	1.3867
0.5000	1.3863
0.6001	1.3858
0.7000	1.3853
0.7999	1.3846
0.8500	1.3843
0.9000	1.3839
0.9501	1.3835

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0531	690.2
0.0980	692.4
0.1986	698.3
0.2981	705.1
0.3987	713.1
0.4987	722.3
0.5987	732.9
0.6994	745.8
0.8007	761.0
0.9000	779.2
0.9499	789.6

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0502	689.82
0.1002	692.19
0.1504	694.9
0.1999	697.87
0.3000	704.65
0.3999	712.46
0.5000	721.44
0.6001	731.85
0.7000	744.14
0.7999	758.95
0.8500	767.56
0.9000	777.1
0.9501	787.71

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	800.03
298.15	0.0200	795.39
298.15	0.0400	790.82
298.15	0.0600	786.22
298.15	0.1000	777.82
298.15	0.2000	759.71
298.15	0.3000	744.88
298.15	0.4000	732.42
298.15	0.4999	721.93
298.15	0.5996	712.88
298.15	0.6998	704.9
298.15	0.7995	698.16
298.15	0.9000	692.36
298.15	1.0000	687.82
303.15	0.0000	796.01
303.15	0.0200	791.36
303.15	0.0400	786.77
303.15	0.0600	782.15
303.15	0.1000	773.72
303.15	0.2000	755.54
303.15	0.3000	740.67
303.15	0.4000	728.17
303.15	0.4999	717.66
303.15	0.5996	708.61
303.15	0.6998	700.62
303.15	0.7995	693.9
303.15	0.9000	688.13
303.15	1.0000	683.68
308.15	0.0000	791.92
308.15	0.0200	787.26
308.15	0.0400	782.66
308.15	0.0600	778.03
308.15	0.1000	769.57
308.15	0.2000	751.33
308.15	0.3000	736.41
308.15	0.4000	723.88
308.15	0.4999	713.35
308.15	0.5996	704.28
308.15	0.6998	696.31
308.15	0.7995	689.61
308.15	0.9000	683.86
308.15	1.0000	679.52
313.15	0.0000	787.79
313.15	0.0200	783.12
313.15	0.0400	778.51
313.15	0.0600	773.86
313.15	0.1000	765.38
313.15	0.2000	747.08
313.15	0.3000	732.1
313.15	0.4000	719.54
313.15	0.4999	708.99
313.15	0.5996	699.91
313.15	0.6998	691.95
313.15	0.7995	685.26
313.15	0.9000	679.55
313.15	1.0000	675.32
318.15	0.0000	783.65
318.15	0.0200	778.94
318.15	0.0400	774.31
318.15	0.0600	769.64
318.15	0.1000	761.14
318.15	0.2000	742.76
318.15	0.3000	727.73
318.15	0.4000	715.13
318.15	0.4999	704.58
318.15	0.5996	695.48
318.15	0.6998	687.53
318.15	0.7995	680.87
318.15	0.9000	675.2
318.15	1.0000	671.1
323.15	0.0000	779.43
323.15	0.0200	774.7
323.15	0.0400	770.05
323.15	0.0600	765.36
323.15	0.1000	756.84
323.15	0.2000	738.39
323.15	0.3000	723.3
323.15	0.4000	710.67
323.15	0.4999	700.11
323.15	0.5996	691.0
323.15	0.6998	683.07
323.15	0.7995	676.44
323.15	0.9000	670.81
323.15	1.0000	666.85

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	683.74
0.0484	685.75
0.0993	688.26
0.2038	694.24
0.2983	700.64
0.4000	708.63
0.5007	717.82
0.5989	728.33
0.6995	741.12
0.7998	756.21
0.8984	774.29
0.9502	785.01
1.0000	796.55

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0531	690.2
0.0980	692.4
0.1986	698.3
0.2981	705.1
0.3987	713.1
0.4987	722.3
0.5987	732.9
0.6994	745.8
0.8007	761.0
0.9000	779.2
0.9499	789.6

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0502	689.82
0.1002	692.19
0.1504	694.9
0.1999	697.87
0.3000	704.65
0.3999	712.46
0.5000	721.44
0.6001	731.85
0.7000	744.14
0.7999	758.95
0.8500	767.56
0.9000	777.1
0.9501	787.71

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	800.03
298.15	0.0200	795.39
298.15	0.0400	790.82
298.15	0.0600	786.22
298.15	0.1000	777.82
298.15	0.2000	759.71
298.15	0.3000	744.88
298.15	0.4000	732.42
298.15	0.4999	721.93
298.15	0.5996	712.88
298.15	0.6998	704.9
298.15	0.7995	698.16
298.15	0.9000	692.36
298.15	1.0000	687.82
303.15	0.0000	796.01
303.15	0.0200	791.36
303.15	0.0400	786.77
303.15	0.0600	782.15
303.15	0.1000	773.72
303.15	0.2000	755.54
303.15	0.3000	740.67
303.15	0.4000	728.17
303.15	0.4999	717.66
303.15	0.5996	708.61
303.15	0.6998	700.62
303.15	0.7995	693.9
303.15	0.9000	688.13
303.15	1.0000	683.68
308.15	0.0000	791.92
308.15	0.0200	787.26
308.15	0.0400	782.66
308.15	0.0600	778.03
308.15	0.1000	769.57
308.15	0.2000	751.33
308.15	0.3000	736.41
308.15	0.4000	723.88
308.15	0.4999	713.35
308.15	0.5996	704.28
308.15	0.6998	696.31
308.15	0.7995	689.61
308.15	0.9000	683.86
308.15	1.0000	679.52
313.15	0.0000	787.79
313.15	0.0200	783.12
313.15	0.0400	778.51
313.15	0.0600	773.86
313.15	0.1000	765.38
313.15	0.2000	747.08
313.15	0.3000	732.1
313.15	0.4000	719.54
313.15	0.4999	708.99
313.15	0.5996	699.91
313.15	0.6998	691.95
313.15	0.7995	685.26
313.15	0.9000	679.55
313.15	1.0000	675.32
318.15	0.0000	783.65
318.15	0.0200	778.94
318.15	0.0400	774.31
318.15	0.0600	769.64
318.15	0.1000	761.14
318.15	0.2000	742.76
318.15	0.3000	727.73
318.15	0.4000	715.13
318.15	0.4999	704.58
318.15	0.5996	695.48
318.15	0.6998	687.53
318.15	0.7995	680.87
318.15	0.9000	675.2
318.15	1.0000	671.1
323.15	0.0000	779.43
323.15	0.0200	774.7
323.15	0.0400	770.05
323.15	0.0600	765.36
323.15	0.1000	756.84
323.15	0.2000	738.39
323.15	0.3000	723.3
323.15	0.4000	710.67
323.15	0.4999	700.11
323.15	0.5996	691.0
323.15	0.6998	683.07
323.15	0.7995	676.44
323.15	0.9000	670.81
323.15	1.0000	666.85

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of 1-Propanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	683.74
0.0484	685.75
0.0993	688.26
0.2038	694.24
0.2983	700.64
0.4000	708.63
0.5007	717.82
0.5989	728.33
0.6995	741.12
0.7998	756.21
0.8984	774.29
0.9502	785.01
1.0000	796.55

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0233
298.15	0.1000	0.0221
298.15	0.2000	0.0212
298.15	0.3000	0.0206
298.15	0.4000	0.0200
298.15	0.4999	0.0196
298.15	0.5996	0.0192
298.15	0.6998	0.0190
298.15	0.7995	0.0187
298.15	0.9000	0.0185
298.15	1.0000	0.0183
303.15	0.0000	0.0229
303.15	0.1000	0.0216
303.15	0.2000	0.0207
303.15	0.3000	0.0201
303.15	0.4000	0.0196
303.15	0.4999	0.0191
303.15	0.5996	0.0188
303.15	0.6998	0.0185
303.15	0.7995	0.0183
303.15	0.9000	0.0181
303.15	1.0000	0.0179
308.15	0.0000	0.0225
308.15	0.1000	0.0212
308.15	0.2000	0.0203
308.15	0.3000	0.0197
308.15	0.4000	0.0191
308.15	0.4999	0.0186
308.15	0.5996	0.0183
308.15	0.6998	0.0181
308.15	0.7995	0.0178
308.15	0.9000	0.0176
308.15	1.0000	0.0174
313.15	0.0000	0.0221
313.15	0.1000	0.0208
313.15	0.2000	0.0198
313.15	0.3000	0.0192
313.15	0.4000	0.0187
313.15	0.4999	0.0182
313.15	0.5996	0.0179
313.15	0.6998	0.0176
313.15	0.7995	0.0174
313.15	0.9000	0.0173
313.15	1.0000	0.0171
318.15	0.0000	0.0217
318.15	0.1000	0.0203
318.15	0.2000	0.0193
318.15	0.3000	0.0187
318.15	0.4000	0.0181
318.15	0.4999	0.0176
318.15	0.5996	0.0173
318.15	0.6998	0.0171
318.15	0.7995	0.0169
318.15	0.9000	0.0167
318.15	1.0000	0.0166
323.15	0.0000	0.0213
323.15	0.1000	0.0198
323.15	0.2000	0.0188
323.15	0.3000	0.0182
323.15	0.4000	0.0176
323.15	0.4999	0.0172
323.15	0.5996	0.0168
323.15	0.6998	0.0167
323.15	0.7995	0.0164
323.15	0.9000	0.0163
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- (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
298.15	0.0000	0.0233
298.15	0.1000	0.0221
298.15	0.2000	0.0212
298.15	0.3000	0.0206
298.15	0.4000	0.0200
298.15	0.4999	0.0196
298.15	0.5996	0.0192
298.15	0.6998	0.0190
298.15	0.7995	0.0187
298.15	0.9000	0.0185
298.15	1.0000	0.0183
303.15	0.0000	0.0229
303.15	0.1000	0.0216
303.15	0.2000	0.0207
303.15	0.3000	0.0201
303.15	0.4000	0.0196
303.15	0.4999	0.0191
303.15	0.5996	0.0188
303.15	0.6998	0.0185
303.15	0.7995	0.0183
303.15	0.9000	0.0181
303.15	1.0000	0.0179
308.15	0.0000	0.0225
308.15	0.1000	0.0212
308.15	0.2000	0.0203
308.15	0.3000	0.0197
308.15	0.4000	0.0191
308.15	0.4999	0.0186
308.15	0.5996	0.0183
308.15	0.6998	0.0181
308.15	0.7995	0.0178
308.15	0.9000	0.0176
308.15	1.0000	0.0174
313.15	0.0000	0.0221
313.15	0.1000	0.0208
313.15	0.2000	0.0198
313.15	0.3000	0.0192
313.15	0.4000	0.0187
313.15	0.4999	0.0182
313.15	0.5996	0.0179
313.15	0.6998	0.0176
313.15	0.7995	0.0174
313.15	0.9000	0.0173
313.15	1.0000	0.0171
318.15	0.0000	0.0217
318.15	0.1000	0.0203
318.15	0.2000	0.0193
318.15	0.3000	0.0187
318.15	0.4000	0.0181
318.15	0.4999	0.0176
318.15	0.5996	0.0173
318.15	0.6998	0.0171
318.15	0.7995	0.0169
318.15	0.9000	0.0167
318.15	1.0000	0.0166
323.15	0.0000	0.0213
323.15	0.1000	0.0198
323.15	0.2000	0.0188
323.15	0.3000	0.0182
323.15	0.4000	0.0176
323.15	0.4999	0.0172
323.15	0.5996	0.0168
323.15	0.6998	0.0167
323.15	0.7995	0.0164
323.15	0.9000	0.0163
323.15	1.0000	0.0162

Sources

• Isothermal vapor liquid equilibrium at 303.15K and excess molar volumes at 298.15 K for the ternary system of propyl vinyl ether + 1-propanol + 2,2,4-trimethyl-pentane and its binary sub-systems
• 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
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Isothermal Vapor Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K
• Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K
• 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
• Isothermal VLE and VE at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether (DIPE) + 1-Propanol + 2,2,4-Trimethylpentane