Datasets
-
η - Viscosity, Pa*s (4)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (4)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0012 |
293.15 |
0.1044 |
0.0011 |
293.15 |
0.2078 |
0.0011 |
293.15 |
0.3105 |
0.0010 |
293.15 |
0.4008 |
0.0010 |
293.15 |
0.5171 |
0.0010 |
293.15 |
0.5908 |
0.0009 |
293.15 |
0.7133 |
0.0009 |
293.15 |
0.8046 |
0.0009 |
293.15 |
0.9051 |
0.0008 |
293.15 |
1.0000 |
0.0008 |
303.15 |
0.0000 |
0.0010 |
303.15 |
0.1044 |
0.0009 |
303.15 |
0.2078 |
0.0009 |
303.15 |
0.3105 |
0.0009 |
303.15 |
0.4008 |
0.0009 |
303.15 |
0.5171 |
0.0008 |
303.15 |
0.5908 |
0.0008 |
303.15 |
0.7133 |
0.0008 |
303.15 |
0.8046 |
0.0007 |
303.15 |
0.9051 |
0.0007 |
303.15 |
1.0000 |
0.0007 |
313.15 |
0.0000 |
0.0008 |
313.15 |
0.1044 |
0.0008 |
313.15 |
0.2078 |
0.0008 |
313.15 |
0.3105 |
0.0007 |
313.15 |
0.4008 |
0.0007 |
313.15 |
0.5171 |
0.0007 |
313.15 |
0.5908 |
0.0007 |
313.15 |
0.7133 |
0.0007 |
313.15 |
0.8046 |
0.0006 |
313.15 |
0.9051 |
0.0006 |
313.15 |
1.0000 |
0.0006 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Viscosity, Pa*s - Liquid |
288.15 |
0.0000 |
0.0013 |
288.15 |
0.0500 |
0.0012 |
288.15 |
0.1000 |
0.0012 |
288.15 |
0.1500 |
0.0011 |
288.15 |
0.2000 |
0.0011 |
288.15 |
0.2500 |
0.0011 |
288.15 |
0.3000 |
0.0011 |
288.15 |
0.3500 |
0.0011 |
288.15 |
0.4000 |
0.0010 |
288.15 |
0.4500 |
0.0010 |
288.15 |
0.5000 |
0.0010 |
288.15 |
0.5500 |
0.0010 |
288.15 |
0.6000 |
0.0010 |
288.15 |
0.6500 |
0.0010 |
288.15 |
0.7000 |
0.0010 |
288.15 |
0.7500 |
0.0011 |
288.15 |
0.8000 |
0.0011 |
288.15 |
0.8500 |
0.0011 |
288.15 |
0.9000 |
0.0011 |
288.15 |
0.9500 |
0.0011 |
288.15 |
1.0000 |
0.0011 |
298.15 |
0.0000 |
0.0011 |
298.15 |
0.0500 |
0.0010 |
298.15 |
0.1000 |
0.0010 |
298.15 |
0.1500 |
0.0009 |
298.15 |
0.2000 |
0.0009 |
298.15 |
0.2500 |
0.0009 |
298.15 |
0.3000 |
0.0009 |
298.15 |
0.3500 |
0.0009 |
298.15 |
0.4000 |
0.0009 |
298.15 |
0.4500 |
0.0009 |
298.15 |
0.5000 |
0.0009 |
298.15 |
0.5500 |
0.0009 |
298.15 |
0.6000 |
0.0009 |
298.15 |
0.6500 |
0.0009 |
298.15 |
0.7000 |
0.0009 |
298.15 |
0.7500 |
0.0009 |
298.15 |
0.8000 |
0.0009 |
298.15 |
0.8500 |
0.0009 |
298.15 |
0.9000 |
0.0009 |
298.15 |
0.9500 |
0.0009 |
298.15 |
1.0000 |
0.0009 |
308.15 |
0.0000 |
0.0009 |
308.15 |
0.0500 |
0.0009 |
308.15 |
0.1000 |
0.0008 |
308.15 |
0.1500 |
0.0008 |
308.15 |
0.2000 |
0.0008 |
308.15 |
0.2500 |
0.0008 |
308.15 |
0.3000 |
0.0008 |
308.15 |
0.3500 |
0.0008 |
308.15 |
0.4000 |
0.0008 |
308.15 |
0.4500 |
0.0008 |
308.15 |
0.5000 |
0.0008 |
308.15 |
0.5500 |
0.0008 |
308.15 |
0.6000 |
0.0008 |
308.15 |
0.6500 |
0.0008 |
308.15 |
0.7000 |
0.0008 |
308.15 |
0.7500 |
0.0008 |
308.15 |
0.8000 |
0.0008 |
308.15 |
0.8500 |
0.0008 |
308.15 |
0.9000 |
0.0008 |
308.15 |
0.9500 |
0.0008 |
308.15 |
1.0000 |
0.0008 |
318.15 |
0.0000 |
0.0008 |
318.15 |
0.0500 |
0.0007 |
318.15 |
0.1000 |
0.0007 |
318.15 |
0.1500 |
0.0007 |
318.15 |
0.2000 |
0.0007 |
318.15 |
0.2500 |
0.0007 |
318.15 |
0.3000 |
0.0007 |
318.15 |
0.3500 |
0.0007 |
318.15 |
0.4000 |
0.0007 |
318.15 |
0.4500 |
0.0007 |
318.15 |
0.5000 |
0.0007 |
318.15 |
0.5500 |
0.0007 |
318.15 |
0.6000 |
0.0007 |
318.15 |
0.6500 |
0.0007 |
318.15 |
0.7000 |
0.0007 |
318.15 |
0.7500 |
0.0007 |
318.15 |
0.8000 |
0.0007 |
318.15 |
0.8500 |
0.0007 |
318.15 |
0.9000 |
0.0007 |
318.15 |
0.9500 |
0.0007 |
318.15 |
1.0000 |
0.0007 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0012 |
293.15 |
0.1044 |
0.0011 |
293.15 |
0.2078 |
0.0011 |
293.15 |
0.3105 |
0.0010 |
293.15 |
0.4008 |
0.0010 |
293.15 |
0.5171 |
0.0010 |
293.15 |
0.5908 |
0.0009 |
293.15 |
0.7133 |
0.0009 |
293.15 |
0.8046 |
0.0009 |
293.15 |
0.9051 |
0.0008 |
293.15 |
1.0000 |
0.0008 |
303.15 |
0.0000 |
0.0010 |
303.15 |
0.1044 |
0.0009 |
303.15 |
0.2078 |
0.0009 |
303.15 |
0.3105 |
0.0009 |
303.15 |
0.4008 |
0.0009 |
303.15 |
0.5171 |
0.0008 |
303.15 |
0.5908 |
0.0008 |
303.15 |
0.7133 |
0.0008 |
303.15 |
0.8046 |
0.0007 |
303.15 |
0.9051 |
0.0007 |
303.15 |
1.0000 |
0.0007 |
313.15 |
0.0000 |
0.0008 |
313.15 |
0.1044 |
0.0008 |
313.15 |
0.2078 |
0.0008 |
313.15 |
0.3105 |
0.0007 |
313.15 |
0.4008 |
0.0007 |
313.15 |
0.5171 |
0.0007 |
313.15 |
0.5908 |
0.0007 |
313.15 |
0.7133 |
0.0007 |
313.15 |
0.8046 |
0.0006 |
313.15 |
0.9051 |
0.0006 |
313.15 |
1.0000 |
0.0006 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Viscosity, Pa*s - Liquid |
288.15 |
0.0000 |
0.0013 |
288.15 |
0.0500 |
0.0012 |
288.15 |
0.1000 |
0.0012 |
288.15 |
0.1500 |
0.0011 |
288.15 |
0.2000 |
0.0011 |
288.15 |
0.2500 |
0.0011 |
288.15 |
0.3000 |
0.0011 |
288.15 |
0.3500 |
0.0011 |
288.15 |
0.4000 |
0.0010 |
288.15 |
0.4500 |
0.0010 |
288.15 |
0.5000 |
0.0010 |
288.15 |
0.5500 |
0.0010 |
288.15 |
0.6000 |
0.0010 |
288.15 |
0.6500 |
0.0010 |
288.15 |
0.7000 |
0.0010 |
288.15 |
0.7500 |
0.0011 |
288.15 |
0.8000 |
0.0011 |
288.15 |
0.8500 |
0.0011 |
288.15 |
0.9000 |
0.0011 |
288.15 |
0.9500 |
0.0011 |
288.15 |
1.0000 |
0.0011 |
298.15 |
0.0000 |
0.0011 |
298.15 |
0.0500 |
0.0010 |
298.15 |
0.1000 |
0.0010 |
298.15 |
0.1500 |
0.0009 |
298.15 |
0.2000 |
0.0009 |
298.15 |
0.2500 |
0.0009 |
298.15 |
0.3000 |
0.0009 |
298.15 |
0.3500 |
0.0009 |
298.15 |
0.4000 |
0.0009 |
298.15 |
0.4500 |
0.0009 |
298.15 |
0.5000 |
0.0009 |
298.15 |
0.5500 |
0.0009 |
298.15 |
0.6000 |
0.0009 |
298.15 |
0.6500 |
0.0009 |
298.15 |
0.7000 |
0.0009 |
298.15 |
0.7500 |
0.0009 |
298.15 |
0.8000 |
0.0009 |
298.15 |
0.8500 |
0.0009 |
298.15 |
0.9000 |
0.0009 |
298.15 |
0.9500 |
0.0009 |
298.15 |
1.0000 |
0.0009 |
308.15 |
0.0000 |
0.0009 |
308.15 |
0.0500 |
0.0009 |
308.15 |
0.1000 |
0.0008 |
308.15 |
0.1500 |
0.0008 |
308.15 |
0.2000 |
0.0008 |
308.15 |
0.2500 |
0.0008 |
308.15 |
0.3000 |
0.0008 |
308.15 |
0.3500 |
0.0008 |
308.15 |
0.4000 |
0.0008 |
308.15 |
0.4500 |
0.0008 |
308.15 |
0.5000 |
0.0008 |
308.15 |
0.5500 |
0.0008 |
308.15 |
0.6000 |
0.0008 |
308.15 |
0.6500 |
0.0008 |
308.15 |
0.7000 |
0.0008 |
308.15 |
0.7500 |
0.0008 |
308.15 |
0.8000 |
0.0008 |
308.15 |
0.8500 |
0.0008 |
308.15 |
0.9000 |
0.0008 |
308.15 |
0.9500 |
0.0008 |
308.15 |
1.0000 |
0.0008 |
318.15 |
0.0000 |
0.0008 |
318.15 |
0.0500 |
0.0007 |
318.15 |
0.1000 |
0.0007 |
318.15 |
0.1500 |
0.0007 |
318.15 |
0.2000 |
0.0007 |
318.15 |
0.2500 |
0.0007 |
318.15 |
0.3000 |
0.0007 |
318.15 |
0.3500 |
0.0007 |
318.15 |
0.4000 |
0.0007 |
318.15 |
0.4500 |
0.0007 |
318.15 |
0.5000 |
0.0007 |
318.15 |
0.5500 |
0.0007 |
318.15 |
0.6000 |
0.0007 |
318.15 |
0.6500 |
0.0007 |
318.15 |
0.7000 |
0.0007 |
318.15 |
0.7500 |
0.0007 |
318.15 |
0.8000 |
0.0007 |
318.15 |
0.8500 |
0.0007 |
318.15 |
0.9000 |
0.0007 |
318.15 |
0.9500 |
0.0007 |
318.15 |
1.0000 |
0.0007 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3633 |
288.15 |
0.0500 |
1.3694 |
288.15 |
0.1000 |
1.3745 |
288.15 |
0.1500 |
1.3788 |
288.15 |
0.2000 |
1.3825 |
288.15 |
0.2500 |
1.3858 |
288.15 |
0.3000 |
1.3886 |
288.15 |
0.3500 |
1.3912 |
288.15 |
0.4000 |
1.3935 |
288.15 |
0.4500 |
1.3955 |
288.15 |
0.5000 |
1.3974 |
288.15 |
0.5500 |
1.3991 |
288.15 |
0.6000 |
1.4007 |
288.15 |
0.6500 |
1.4021 |
288.15 |
0.7000 |
1.4034 |
288.15 |
0.7500 |
1.4047 |
288.15 |
0.8000 |
1.4058 |
288.15 |
0.8500 |
1.4068 |
288.15 |
0.9000 |
1.4078 |
288.15 |
0.9500 |
1.4087 |
288.15 |
1.0000 |
1.4095 |
298.15 |
0.0000 |
1.3594 |
298.15 |
0.0500 |
1.3654 |
298.15 |
0.1000 |
1.3703 |
298.15 |
0.1500 |
1.3746 |
298.15 |
0.2000 |
1.3783 |
298.15 |
0.2500 |
1.3815 |
298.15 |
0.3000 |
1.3843 |
298.15 |
0.3500 |
1.3868 |
298.15 |
0.4000 |
1.3891 |
298.15 |
0.4500 |
1.3911 |
298.15 |
0.5000 |
1.393 |
298.15 |
0.5500 |
1.3946 |
298.15 |
0.6000 |
1.3962 |
298.15 |
0.6500 |
1.3976 |
298.15 |
0.7000 |
1.3989 |
298.15 |
0.7500 |
1.4002 |
298.15 |
0.8000 |
1.4013 |
298.15 |
0.8500 |
1.4024 |
298.15 |
0.9000 |
1.4033 |
298.15 |
0.9500 |
1.4042 |
298.15 |
1.0000 |
1.405 |
308.15 |
0.0000 |
1.3553 |
308.15 |
0.0500 |
1.3611 |
308.15 |
0.1000 |
1.366 |
308.15 |
0.1500 |
1.3702 |
308.15 |
0.2000 |
1.3739 |
308.15 |
0.2500 |
1.3771 |
308.15 |
0.3000 |
1.3799 |
308.15 |
0.3500 |
1.3824 |
308.15 |
0.4000 |
1.3846 |
308.15 |
0.4500 |
1.3866 |
308.15 |
0.5000 |
1.3885 |
308.15 |
0.5500 |
1.3902 |
308.15 |
0.6000 |
1.3917 |
308.15 |
0.6500 |
1.3931 |
308.15 |
0.7000 |
1.3944 |
308.15 |
0.7500 |
1.3957 |
308.15 |
0.8000 |
1.3968 |
308.15 |
0.8500 |
1.3979 |
308.15 |
0.9000 |
1.3988 |
308.15 |
0.9500 |
1.3997 |
308.15 |
1.0000 |
1.4005 |
318.15 |
0.0000 |
1.3515 |
318.15 |
0.0500 |
1.357 |
318.15 |
0.1000 |
1.3619 |
318.15 |
0.1500 |
1.366 |
318.15 |
0.2000 |
1.3696 |
318.15 |
0.2500 |
1.3727 |
318.15 |
0.3000 |
1.3755 |
318.15 |
0.3500 |
1.378 |
318.15 |
0.4000 |
1.3802 |
318.15 |
0.4500 |
1.3822 |
318.15 |
0.5000 |
1.384 |
318.15 |
0.5500 |
1.3856 |
318.15 |
0.6000 |
1.3872 |
318.15 |
0.6500 |
1.3886 |
318.15 |
0.7000 |
1.3899 |
318.15 |
0.7500 |
1.3911 |
318.15 |
0.8000 |
1.3922 |
318.15 |
0.8500 |
1.3933 |
318.15 |
0.9000 |
1.3943 |
318.15 |
0.9500 |
1.3951 |
318.15 |
1.0000 |
1.396 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100.5 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3633 |
288.15 |
0.0500 |
1.3694 |
288.15 |
0.1000 |
1.3745 |
288.15 |
0.1500 |
1.3788 |
288.15 |
0.2000 |
1.3825 |
288.15 |
0.2500 |
1.3858 |
288.15 |
0.3000 |
1.3886 |
288.15 |
0.3500 |
1.3912 |
288.15 |
0.4000 |
1.3935 |
288.15 |
0.4500 |
1.3955 |
288.15 |
0.5000 |
1.3974 |
288.15 |
0.5500 |
1.3991 |
288.15 |
0.6000 |
1.4007 |
288.15 |
0.6500 |
1.4021 |
288.15 |
0.7000 |
1.4034 |
288.15 |
0.7500 |
1.4047 |
288.15 |
0.8000 |
1.4058 |
288.15 |
0.8500 |
1.4068 |
288.15 |
0.9000 |
1.4078 |
288.15 |
0.9500 |
1.4087 |
288.15 |
1.0000 |
1.4095 |
298.15 |
0.0000 |
1.3594 |
298.15 |
0.0500 |
1.3654 |
298.15 |
0.1000 |
1.3703 |
298.15 |
0.1500 |
1.3746 |
298.15 |
0.2000 |
1.3783 |
298.15 |
0.2500 |
1.3815 |
298.15 |
0.3000 |
1.3843 |
298.15 |
0.3500 |
1.3868 |
298.15 |
0.4000 |
1.3891 |
298.15 |
0.4500 |
1.3911 |
298.15 |
0.5000 |
1.393 |
298.15 |
0.5500 |
1.3946 |
298.15 |
0.6000 |
1.3962 |
298.15 |
0.6500 |
1.3976 |
298.15 |
0.7000 |
1.3989 |
298.15 |
0.7500 |
1.4002 |
298.15 |
0.8000 |
1.4013 |
298.15 |
0.8500 |
1.4024 |
298.15 |
0.9000 |
1.4033 |
298.15 |
0.9500 |
1.4042 |
298.15 |
1.0000 |
1.405 |
308.15 |
0.0000 |
1.3553 |
308.15 |
0.0500 |
1.3611 |
308.15 |
0.1000 |
1.366 |
308.15 |
0.1500 |
1.3702 |
308.15 |
0.2000 |
1.3739 |
308.15 |
0.2500 |
1.3771 |
308.15 |
0.3000 |
1.3799 |
308.15 |
0.3500 |
1.3824 |
308.15 |
0.4000 |
1.3846 |
308.15 |
0.4500 |
1.3866 |
308.15 |
0.5000 |
1.3885 |
308.15 |
0.5500 |
1.3902 |
308.15 |
0.6000 |
1.3917 |
308.15 |
0.6500 |
1.3931 |
308.15 |
0.7000 |
1.3944 |
308.15 |
0.7500 |
1.3957 |
308.15 |
0.8000 |
1.3968 |
308.15 |
0.8500 |
1.3979 |
308.15 |
0.9000 |
1.3988 |
308.15 |
0.9500 |
1.3997 |
308.15 |
1.0000 |
1.4005 |
318.15 |
0.0000 |
1.3515 |
318.15 |
0.0500 |
1.357 |
318.15 |
0.1000 |
1.3619 |
318.15 |
0.1500 |
1.366 |
318.15 |
0.2000 |
1.3696 |
318.15 |
0.2500 |
1.3727 |
318.15 |
0.3000 |
1.3755 |
318.15 |
0.3500 |
1.378 |
318.15 |
0.4000 |
1.3802 |
318.15 |
0.4500 |
1.3822 |
318.15 |
0.5000 |
1.384 |
318.15 |
0.5500 |
1.3856 |
318.15 |
0.6000 |
1.3872 |
318.15 |
0.6500 |
1.3886 |
318.15 |
0.7000 |
1.3899 |
318.15 |
0.7500 |
1.3911 |
318.15 |
0.8000 |
1.3922 |
318.15 |
0.8500 |
1.3933 |
318.15 |
0.9000 |
1.3943 |
318.15 |
0.9500 |
1.3951 |
318.15 |
1.0000 |
1.396 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
788.24 |
293.15 |
0.1044 |
797.72 |
293.15 |
0.2078 |
807.1 |
293.15 |
0.3105 |
816.42 |
293.15 |
0.4008 |
824.62 |
293.15 |
0.5171 |
835.18 |
293.15 |
0.5908 |
841.87 |
293.15 |
0.7133 |
852.99 |
293.15 |
0.8046 |
861.27 |
293.15 |
0.9051 |
870.4 |
293.15 |
1.0000 |
879.01 |
303.15 |
0.0000 |
780.73 |
303.15 |
0.1044 |
789.98 |
303.15 |
0.2078 |
799.14 |
303.15 |
0.3105 |
808.23 |
303.15 |
0.4008 |
816.23 |
303.15 |
0.5171 |
826.53 |
303.15 |
0.5908 |
833.06 |
303.15 |
0.7133 |
843.91 |
303.15 |
0.8046 |
852.0 |
303.15 |
0.9051 |
860.9 |
303.15 |
1.0000 |
869.31 |
313.15 |
0.0000 |
771.98 |
313.15 |
0.1044 |
781.51 |
313.15 |
0.2078 |
790.95 |
313.15 |
0.3105 |
800.33 |
313.15 |
0.4008 |
808.57 |
313.15 |
0.5171 |
819.19 |
313.15 |
0.5908 |
825.92 |
313.15 |
0.7133 |
837.1 |
313.15 |
0.8046 |
845.44 |
313.15 |
0.9051 |
854.62 |
313.15 |
1.0000 |
863.28 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
793.6 |
288.15 |
0.0500 |
804.18 |
288.15 |
0.1000 |
812.99 |
288.15 |
0.1500 |
820.54 |
288.15 |
0.2000 |
827.14 |
288.15 |
0.2500 |
832.89 |
288.15 |
0.3000 |
837.94 |
288.15 |
0.3500 |
842.47 |
288.15 |
0.4000 |
846.5 |
288.15 |
0.4500 |
850.15 |
288.15 |
0.5000 |
853.47 |
288.15 |
0.5500 |
856.51 |
288.15 |
0.6000 |
859.28 |
288.15 |
0.6500 |
861.84 |
288.15 |
0.7000 |
864.22 |
288.15 |
0.7500 |
866.43 |
288.15 |
0.8000 |
868.48 |
288.15 |
0.8500 |
870.41 |
288.15 |
0.9000 |
872.22 |
288.15 |
0.9500 |
873.99 |
288.15 |
1.0000 |
875.64 |
298.15 |
0.0000 |
785.0 |
298.15 |
0.0500 |
795.44 |
298.15 |
0.1000 |
804.11 |
298.15 |
0.1500 |
811.53 |
298.15 |
0.2000 |
818.05 |
298.15 |
0.2500 |
823.72 |
298.15 |
0.3000 |
828.72 |
298.15 |
0.3500 |
833.2 |
298.15 |
0.4000 |
837.18 |
298.15 |
0.4500 |
840.82 |
298.15 |
0.5000 |
844.11 |
298.15 |
0.5500 |
847.12 |
298.15 |
0.6000 |
849.88 |
298.15 |
0.6500 |
852.43 |
298.15 |
0.7000 |
854.82 |
298.15 |
0.7500 |
857.02 |
298.15 |
0.8000 |
859.09 |
298.15 |
0.8500 |
861.04 |
298.15 |
0.9000 |
862.86 |
298.15 |
0.9500 |
864.66 |
298.15 |
1.0000 |
866.29 |
308.15 |
0.0000 |
776.31 |
308.15 |
0.0500 |
786.59 |
308.15 |
0.1000 |
795.12 |
308.15 |
0.1500 |
802.42 |
308.15 |
0.2000 |
808.85 |
308.15 |
0.2500 |
814.44 |
308.15 |
0.3000 |
819.38 |
308.15 |
0.3500 |
823.82 |
308.15 |
0.4000 |
827.76 |
308.15 |
0.4500 |
831.37 |
308.15 |
0.5000 |
834.63 |
308.15 |
0.5500 |
837.64 |
308.15 |
0.6000 |
840.39 |
308.15 |
0.6500 |
842.94 |
308.15 |
0.7000 |
845.33 |
308.15 |
0.7500 |
847.54 |
308.15 |
0.8000 |
849.63 |
308.15 |
0.8500 |
851.59 |
308.15 |
0.9000 |
853.45 |
308.15 |
0.9500 |
855.27 |
308.15 |
1.0000 |
856.91 |
318.15 |
0.0000 |
767.44 |
318.15 |
0.0500 |
777.58 |
318.15 |
0.1000 |
785.96 |
318.15 |
0.1500 |
793.14 |
318.15 |
0.2000 |
799.48 |
318.15 |
0.2500 |
805.01 |
318.15 |
0.3000 |
809.89 |
318.15 |
0.3500 |
814.29 |
318.15 |
0.4000 |
818.2 |
318.15 |
0.4500 |
821.8 |
318.15 |
0.5000 |
825.05 |
318.15 |
0.5500 |
828.05 |
318.15 |
0.6000 |
830.79 |
318.15 |
0.6500 |
833.34 |
318.15 |
0.7000 |
835.75 |
318.15 |
0.7500 |
837.97 |
318.15 |
0.8000 |
840.08 |
318.15 |
0.8500 |
842.07 |
318.15 |
0.9000 |
843.97 |
318.15 |
0.9500 |
845.83 |
318.15 |
1.0000 |
847.5 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
788.24 |
293.15 |
0.1044 |
797.72 |
293.15 |
0.2078 |
807.1 |
293.15 |
0.3105 |
816.42 |
293.15 |
0.4008 |
824.62 |
293.15 |
0.5171 |
835.18 |
293.15 |
0.5908 |
841.87 |
293.15 |
0.7133 |
852.99 |
293.15 |
0.8046 |
861.27 |
293.15 |
0.9051 |
870.4 |
293.15 |
1.0000 |
879.01 |
303.15 |
0.0000 |
780.73 |
303.15 |
0.1044 |
789.98 |
303.15 |
0.2078 |
799.14 |
303.15 |
0.3105 |
808.23 |
303.15 |
0.4008 |
816.23 |
303.15 |
0.5171 |
826.53 |
303.15 |
0.5908 |
833.06 |
303.15 |
0.7133 |
843.91 |
303.15 |
0.8046 |
852.0 |
303.15 |
0.9051 |
860.9 |
303.15 |
1.0000 |
869.31 |
313.15 |
0.0000 |
771.98 |
313.15 |
0.1044 |
781.51 |
313.15 |
0.2078 |
790.95 |
313.15 |
0.3105 |
800.33 |
313.15 |
0.4008 |
808.57 |
313.15 |
0.5171 |
819.19 |
313.15 |
0.5908 |
825.92 |
313.15 |
0.7133 |
837.1 |
313.15 |
0.8046 |
845.44 |
313.15 |
0.9051 |
854.62 |
313.15 |
1.0000 |
863.28 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
793.6 |
288.15 |
0.0500 |
804.18 |
288.15 |
0.1000 |
812.99 |
288.15 |
0.1500 |
820.54 |
288.15 |
0.2000 |
827.14 |
288.15 |
0.2500 |
832.89 |
288.15 |
0.3000 |
837.94 |
288.15 |
0.3500 |
842.47 |
288.15 |
0.4000 |
846.5 |
288.15 |
0.4500 |
850.15 |
288.15 |
0.5000 |
853.47 |
288.15 |
0.5500 |
856.51 |
288.15 |
0.6000 |
859.28 |
288.15 |
0.6500 |
861.84 |
288.15 |
0.7000 |
864.22 |
288.15 |
0.7500 |
866.43 |
288.15 |
0.8000 |
868.48 |
288.15 |
0.8500 |
870.41 |
288.15 |
0.9000 |
872.22 |
288.15 |
0.9500 |
873.99 |
288.15 |
1.0000 |
875.64 |
298.15 |
0.0000 |
785.0 |
298.15 |
0.0500 |
795.44 |
298.15 |
0.1000 |
804.11 |
298.15 |
0.1500 |
811.53 |
298.15 |
0.2000 |
818.05 |
298.15 |
0.2500 |
823.72 |
298.15 |
0.3000 |
828.72 |
298.15 |
0.3500 |
833.2 |
298.15 |
0.4000 |
837.18 |
298.15 |
0.4500 |
840.82 |
298.15 |
0.5000 |
844.11 |
298.15 |
0.5500 |
847.12 |
298.15 |
0.6000 |
849.88 |
298.15 |
0.6500 |
852.43 |
298.15 |
0.7000 |
854.82 |
298.15 |
0.7500 |
857.02 |
298.15 |
0.8000 |
859.09 |
298.15 |
0.8500 |
861.04 |
298.15 |
0.9000 |
862.86 |
298.15 |
0.9500 |
864.66 |
298.15 |
1.0000 |
866.29 |
308.15 |
0.0000 |
776.31 |
308.15 |
0.0500 |
786.59 |
308.15 |
0.1000 |
795.12 |
308.15 |
0.1500 |
802.42 |
308.15 |
0.2000 |
808.85 |
308.15 |
0.2500 |
814.44 |
308.15 |
0.3000 |
819.38 |
308.15 |
0.3500 |
823.82 |
308.15 |
0.4000 |
827.76 |
308.15 |
0.4500 |
831.37 |
308.15 |
0.5000 |
834.63 |
308.15 |
0.5500 |
837.64 |
308.15 |
0.6000 |
840.39 |
308.15 |
0.6500 |
842.94 |
308.15 |
0.7000 |
845.33 |
308.15 |
0.7500 |
847.54 |
308.15 |
0.8000 |
849.63 |
308.15 |
0.8500 |
851.59 |
308.15 |
0.9000 |
853.45 |
308.15 |
0.9500 |
855.27 |
308.15 |
1.0000 |
856.91 |
318.15 |
0.0000 |
767.44 |
318.15 |
0.0500 |
777.58 |
318.15 |
0.1000 |
785.96 |
318.15 |
0.1500 |
793.14 |
318.15 |
0.2000 |
799.48 |
318.15 |
0.2500 |
805.01 |
318.15 |
0.3000 |
809.89 |
318.15 |
0.3500 |
814.29 |
318.15 |
0.4000 |
818.2 |
318.15 |
0.4500 |
821.8 |
318.15 |
0.5000 |
825.05 |
318.15 |
0.5500 |
828.05 |
318.15 |
0.6000 |
830.79 |
318.15 |
0.6500 |
833.34 |
318.15 |
0.7000 |
835.75 |
318.15 |
0.7500 |
837.97 |
318.15 |
0.8000 |
840.08 |
318.15 |
0.8500 |
842.07 |
318.15 |
0.9000 |
843.97 |
318.15 |
0.9500 |
845.83 |
318.15 |
1.0000 |
847.5 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
288.15 |
0.0000 |
0.0230 |
288.15 |
0.0500 |
0.0234 |
288.15 |
0.1000 |
0.0238 |
288.15 |
0.1500 |
0.0241 |
288.15 |
0.2000 |
0.0243 |
288.15 |
0.2500 |
0.0245 |
288.15 |
0.3000 |
0.0247 |
288.15 |
0.3500 |
0.0249 |
288.15 |
0.4000 |
0.0251 |
288.15 |
0.4500 |
0.0252 |
288.15 |
0.5000 |
0.0254 |
288.15 |
0.5500 |
0.0255 |
288.15 |
0.6000 |
0.0256 |
288.15 |
0.6500 |
0.0257 |
288.15 |
0.7000 |
0.0258 |
288.15 |
0.7500 |
0.0259 |
288.15 |
0.8000 |
0.0260 |
288.15 |
0.8500 |
0.0261 |
288.15 |
0.9000 |
0.0262 |
288.15 |
0.9500 |
0.0263 |
288.15 |
1.0000 |
0.0264 |
298.15 |
0.0000 |
0.0223 |
298.15 |
0.0500 |
0.0227 |
298.15 |
0.1000 |
0.0230 |
298.15 |
0.1500 |
0.0232 |
298.15 |
0.2000 |
0.0235 |
298.15 |
0.2500 |
0.0237 |
298.15 |
0.3000 |
0.0239 |
298.15 |
0.3500 |
0.0240 |
298.15 |
0.4000 |
0.0242 |
298.15 |
0.4500 |
0.0243 |
298.15 |
0.5000 |
0.0244 |
298.15 |
0.5500 |
0.0245 |
298.15 |
0.6000 |
0.0246 |
298.15 |
0.6500 |
0.0247 |
298.15 |
0.7000 |
0.0249 |
298.15 |
0.7500 |
0.0250 |
298.15 |
0.8000 |
0.0251 |
298.15 |
0.8500 |
0.0251 |
298.15 |
0.9000 |
0.0252 |
298.15 |
0.9500 |
0.0253 |
298.15 |
1.0000 |
0.0254 |
308.15 |
0.0000 |
0.0215 |
308.15 |
0.0500 |
0.0218 |
308.15 |
0.1000 |
0.0221 |
308.15 |
0.1500 |
0.0224 |
308.15 |
0.2000 |
0.0226 |
308.15 |
0.2500 |
0.0228 |
308.15 |
0.3000 |
0.0230 |
308.15 |
0.3500 |
0.0231 |
308.15 |
0.4000 |
0.0233 |
308.15 |
0.4500 |
0.0234 |
308.15 |
0.5000 |
0.0235 |
308.15 |
0.5500 |
0.0236 |
308.15 |
0.6000 |
0.0237 |
308.15 |
0.6500 |
0.0238 |
308.15 |
0.7000 |
0.0239 |
308.15 |
0.7500 |
0.0240 |
308.15 |
0.8000 |
0.0241 |
308.15 |
0.8500 |
0.0242 |
308.15 |
0.9000 |
0.0243 |
308.15 |
0.9500 |
0.0244 |
308.15 |
1.0000 |
0.0245 |
318.15 |
0.0000 |
0.0206 |
318.15 |
0.0500 |
0.0209 |
318.15 |
0.1000 |
0.0212 |
318.15 |
0.1500 |
0.0215 |
318.15 |
0.2000 |
0.0217 |
318.15 |
0.2500 |
0.0219 |
318.15 |
0.3000 |
0.0220 |
318.15 |
0.3500 |
0.0222 |
318.15 |
0.4000 |
0.0223 |
318.15 |
0.4500 |
0.0225 |
318.15 |
0.5000 |
0.0226 |
318.15 |
0.5500 |
0.0227 |
318.15 |
0.6000 |
0.0228 |
318.15 |
0.6500 |
0.0229 |
318.15 |
0.7000 |
0.0230 |
318.15 |
0.7500 |
0.0231 |
318.15 |
0.8000 |
0.0232 |
318.15 |
0.8500 |
0.0233 |
318.15 |
0.9000 |
0.0234 |
318.15 |
0.9500 |
0.0235 |
318.15 |
1.0000 |
0.0236 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
288.15 |
0.0000 |
0.0230 |
288.15 |
0.0500 |
0.0234 |
288.15 |
0.1000 |
0.0238 |
288.15 |
0.1500 |
0.0241 |
288.15 |
0.2000 |
0.0243 |
288.15 |
0.2500 |
0.0245 |
288.15 |
0.3000 |
0.0247 |
288.15 |
0.3500 |
0.0249 |
288.15 |
0.4000 |
0.0251 |
288.15 |
0.4500 |
0.0252 |
288.15 |
0.5000 |
0.0254 |
288.15 |
0.5500 |
0.0255 |
288.15 |
0.6000 |
0.0256 |
288.15 |
0.6500 |
0.0257 |
288.15 |
0.7000 |
0.0258 |
288.15 |
0.7500 |
0.0259 |
288.15 |
0.8000 |
0.0260 |
288.15 |
0.8500 |
0.0261 |
288.15 |
0.9000 |
0.0262 |
288.15 |
0.9500 |
0.0263 |
288.15 |
1.0000 |
0.0264 |
298.15 |
0.0000 |
0.0223 |
298.15 |
0.0500 |
0.0227 |
298.15 |
0.1000 |
0.0230 |
298.15 |
0.1500 |
0.0232 |
298.15 |
0.2000 |
0.0235 |
298.15 |
0.2500 |
0.0237 |
298.15 |
0.3000 |
0.0239 |
298.15 |
0.3500 |
0.0240 |
298.15 |
0.4000 |
0.0242 |
298.15 |
0.4500 |
0.0243 |
298.15 |
0.5000 |
0.0244 |
298.15 |
0.5500 |
0.0245 |
298.15 |
0.6000 |
0.0246 |
298.15 |
0.6500 |
0.0247 |
298.15 |
0.7000 |
0.0249 |
298.15 |
0.7500 |
0.0250 |
298.15 |
0.8000 |
0.0251 |
298.15 |
0.8500 |
0.0251 |
298.15 |
0.9000 |
0.0252 |
298.15 |
0.9500 |
0.0253 |
298.15 |
1.0000 |
0.0254 |
308.15 |
0.0000 |
0.0215 |
308.15 |
0.0500 |
0.0218 |
308.15 |
0.1000 |
0.0221 |
308.15 |
0.1500 |
0.0224 |
308.15 |
0.2000 |
0.0226 |
308.15 |
0.2500 |
0.0228 |
308.15 |
0.3000 |
0.0230 |
308.15 |
0.3500 |
0.0231 |
308.15 |
0.4000 |
0.0233 |
308.15 |
0.4500 |
0.0234 |
308.15 |
0.5000 |
0.0235 |
308.15 |
0.5500 |
0.0236 |
308.15 |
0.6000 |
0.0237 |
308.15 |
0.6500 |
0.0238 |
308.15 |
0.7000 |
0.0239 |
308.15 |
0.7500 |
0.0240 |
308.15 |
0.8000 |
0.0241 |
308.15 |
0.8500 |
0.0242 |
308.15 |
0.9000 |
0.0243 |
308.15 |
0.9500 |
0.0244 |
308.15 |
1.0000 |
0.0245 |
318.15 |
0.0000 |
0.0206 |
318.15 |
0.0500 |
0.0209 |
318.15 |
0.1000 |
0.0212 |
318.15 |
0.1500 |
0.0215 |
318.15 |
0.2000 |
0.0217 |
318.15 |
0.2500 |
0.0219 |
318.15 |
0.3000 |
0.0220 |
318.15 |
0.3500 |
0.0222 |
318.15 |
0.4000 |
0.0223 |
318.15 |
0.4500 |
0.0225 |
318.15 |
0.5000 |
0.0226 |
318.15 |
0.5500 |
0.0227 |
318.15 |
0.6000 |
0.0228 |
318.15 |
0.6500 |
0.0229 |
318.15 |
0.7000 |
0.0230 |
318.15 |
0.7500 |
0.0231 |
318.15 |
0.8000 |
0.0232 |
318.15 |
0.8500 |
0.0233 |
318.15 |
0.9000 |
0.0234 |
318.15 |
0.9500 |
0.0235 |
318.15 |
1.0000 |
0.0236 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
40.00 |
0.0000 |
408.31 |
40.00 |
0.0501 |
384.52 |
40.00 |
0.1001 |
371.26 |
40.00 |
0.2001 |
356.64 |
40.00 |
0.3001 |
347.77 |
40.00 |
0.3999 |
342.37 |
40.00 |
0.5000 |
338.61 |
40.00 |
0.6000 |
336.21 |
40.00 |
0.6998 |
334.13 |
40.00 |
0.7999 |
332.21 |
40.00 |
0.9000 |
330.55 |
40.00 |
1.0000 |
329.69 |
53.33 |
0.0000 |
417.74 |
53.33 |
0.1001 |
382.39 |
53.33 |
0.2001 |
366.27 |
53.33 |
0.3001 |
355.49 |
53.33 |
0.3999 |
349.92 |
53.33 |
0.5000 |
345.66 |
53.33 |
0.6000 |
343.10 |
53.33 |
0.6998 |
340.86 |
53.33 |
0.7999 |
338.87 |
53.33 |
0.9000 |
336.92 |
53.33 |
1.0000 |
336.07 |
66.66 |
0.0000 |
425.39 |
66.66 |
0.0501 |
402.56 |
66.66 |
0.1001 |
390.53 |
66.66 |
0.2001 |
373.46 |
66.66 |
0.3001 |
363.17 |
66.66 |
0.3999 |
356.09 |
66.66 |
0.5000 |
351.39 |
66.66 |
0.6000 |
348.62 |
66.66 |
0.6998 |
346.55 |
66.66 |
0.7999 |
344.21 |
66.66 |
0.9000 |
342.21 |
66.66 |
1.0000 |
341.23 |
79.99 |
0.0000 |
431.86 |
79.99 |
0.0501 |
408.96 |
79.99 |
0.1001 |
396.15 |
79.99 |
0.1999 |
381.35 |
79.99 |
0.3001 |
369.43 |
79.99 |
0.3999 |
362.50 |
79.99 |
0.4998 |
356.53 |
79.99 |
0.6000 |
353.62 |
79.99 |
0.6998 |
351.31 |
79.99 |
0.8000 |
349.05 |
79.99 |
0.9000 |
347.06 |
79.99 |
1.0000 |
345.60 |
93.32 |
0.0000 |
437.53 |
93.32 |
0.1001 |
401.71 |
93.32 |
0.1999 |
386.08 |
93.32 |
0.3001 |
374.92 |
93.32 |
0.3997 |
366.56 |
93.32 |
0.5000 |
361.18 |
93.32 |
0.6000 |
357.85 |
93.32 |
0.6998 |
355.37 |
93.32 |
0.7999 |
353.08 |
93.32 |
0.8997 |
351.37 |
93.32 |
1.0000 |
349.39 |
101.30 |
0.0000 |
440.57 |
101.30 |
0.0501 |
418.52 |
101.30 |
0.1001 |
404.83 |
101.30 |
0.1999 |
388.82 |
101.30 |
0.3001 |
378.01 |
101.30 |
0.3997 |
369.05 |
101.30 |
0.5000 |
363.61 |
101.30 |
0.6000 |
360.07 |
101.30 |
0.7000 |
357.19 |
101.30 |
0.8000 |
355.13 |
101.30 |
0.9000 |
353.32 |
101.30 |
1.0000 |
351.44 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
40.00 |
0.0000 |
408.31 |
40.00 |
0.0501 |
384.52 |
40.00 |
0.1001 |
371.26 |
40.00 |
0.2001 |
356.64 |
40.00 |
0.3001 |
347.77 |
40.00 |
0.3999 |
342.37 |
40.00 |
0.5000 |
338.61 |
40.00 |
0.6000 |
336.21 |
40.00 |
0.6998 |
334.13 |
40.00 |
0.7999 |
332.21 |
40.00 |
0.9000 |
330.55 |
40.00 |
1.0000 |
329.69 |
53.33 |
0.0000 |
417.74 |
53.33 |
0.1001 |
382.39 |
53.33 |
0.2001 |
366.27 |
53.33 |
0.3001 |
355.49 |
53.33 |
0.3999 |
349.92 |
53.33 |
0.5000 |
345.66 |
53.33 |
0.6000 |
343.10 |
53.33 |
0.6998 |
340.86 |
53.33 |
0.7999 |
338.87 |
53.33 |
0.9000 |
336.92 |
53.33 |
1.0000 |
336.07 |
66.66 |
0.0000 |
425.39 |
66.66 |
0.0501 |
402.56 |
66.66 |
0.1001 |
390.53 |
66.66 |
0.2001 |
373.46 |
66.66 |
0.3001 |
363.17 |
66.66 |
0.3999 |
356.09 |
66.66 |
0.5000 |
351.39 |
66.66 |
0.6000 |
348.62 |
66.66 |
0.6998 |
346.55 |
66.66 |
0.7999 |
344.21 |
66.66 |
0.9000 |
342.21 |
66.66 |
1.0000 |
341.23 |
79.99 |
0.0000 |
431.86 |
79.99 |
0.0501 |
408.96 |
79.99 |
0.1001 |
396.15 |
79.99 |
0.1999 |
381.35 |
79.99 |
0.3001 |
369.43 |
79.99 |
0.3999 |
362.50 |
79.99 |
0.4998 |
356.53 |
79.99 |
0.6000 |
353.62 |
79.99 |
0.6998 |
351.31 |
79.99 |
0.8000 |
349.05 |
79.99 |
0.9000 |
347.06 |
79.99 |
1.0000 |
345.60 |
93.32 |
0.0000 |
437.53 |
93.32 |
0.1001 |
401.71 |
93.32 |
0.1999 |
386.08 |
93.32 |
0.3001 |
374.92 |
93.32 |
0.3997 |
366.56 |
93.32 |
0.5000 |
361.18 |
93.32 |
0.6000 |
357.85 |
93.32 |
0.6998 |
355.37 |
93.32 |
0.7999 |
353.08 |
93.32 |
0.8997 |
351.37 |
93.32 |
1.0000 |
349.39 |
101.30 |
0.0000 |
440.57 |
101.30 |
0.0501 |
418.52 |
101.30 |
0.1001 |
404.83 |
101.30 |
0.1999 |
388.82 |
101.30 |
0.3001 |
378.01 |
101.30 |
0.3997 |
369.05 |
101.30 |
0.5000 |
363.61 |
101.30 |
0.6000 |
360.07 |
101.30 |
0.7000 |
357.19 |
101.30 |
0.8000 |
355.13 |
101.30 |
0.9000 |
353.32 |
101.30 |
1.0000 |
351.44 |
Sources
-
Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, and 313.15) K
-
Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
-
Refractive Indices and Surface Tensions of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
-
Ebulliometric Determination and Prediction of Vapor Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate