Datasets
-
η - Viscosity, Pa*s (4)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
-
γ - Surface tension liquid-gas, N/m (2)
-
Vapor Liquid Equilibrium at Constant Pressure (3)
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
293.00 |
0.0021 |
0.0000 |
303.00 |
0.0015 |
0.0000 |
313.00 |
0.0011 |
0.0983 |
293.00 |
0.0016 |
0.0983 |
303.00 |
0.0011 |
0.0983 |
313.00 |
0.0009 |
0.2085 |
293.00 |
0.0013 |
0.2085 |
303.00 |
0.0009 |
0.2085 |
313.00 |
0.0007 |
0.2911 |
293.00 |
0.0011 |
0.2911 |
303.00 |
0.0007 |
0.2911 |
313.00 |
0.0006 |
0.3728 |
293.00 |
0.0009 |
0.3728 |
303.00 |
0.0006 |
0.3728 |
313.00 |
0.0005 |
0.5014 |
293.00 |
0.0008 |
0.5014 |
303.00 |
0.0006 |
0.5014 |
313.00 |
0.0005 |
0.5976 |
293.00 |
0.0007 |
0.5976 |
303.00 |
0.0005 |
0.5976 |
313.00 |
0.0005 |
0.7483 |
293.00 |
0.0006 |
0.7483 |
303.00 |
0.0005 |
0.7483 |
313.00 |
0.0004 |
0.8001 |
293.00 |
0.0006 |
0.8001 |
303.00 |
0.0005 |
0.8001 |
313.00 |
0.0004 |
0.8939 |
293.00 |
0.0005 |
0.8939 |
303.00 |
0.0004 |
0.8939 |
313.00 |
0.0004 |
1.0000 |
293.00 |
0.0005 |
1.0000 |
303.00 |
0.0004 |
1.0000 |
313.00 |
0.0004 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Viscosity, Pa*s - Liquid |
288.15 |
0.0000 |
0.0028 |
288.15 |
0.0500 |
0.0022 |
288.15 |
0.1000 |
0.0018 |
288.15 |
0.1500 |
0.0016 |
288.15 |
0.2001 |
0.0014 |
288.15 |
0.2500 |
0.0012 |
288.15 |
0.3000 |
0.0011 |
288.15 |
0.3500 |
0.0010 |
288.15 |
0.4000 |
0.0009 |
288.15 |
0.4500 |
0.0008 |
288.15 |
0.5000 |
0.0008 |
288.15 |
0.5500 |
0.0007 |
288.15 |
0.6000 |
0.0007 |
288.15 |
0.6500 |
0.0006 |
288.15 |
0.7000 |
0.0006 |
288.15 |
0.7500 |
0.0006 |
288.15 |
0.8000 |
0.0006 |
288.15 |
0.8500 |
0.0006 |
288.15 |
0.9000 |
0.0005 |
288.15 |
0.9500 |
0.0005 |
288.15 |
1.0000 |
0.0005 |
298.15 |
0.0000 |
0.0020 |
298.15 |
0.0500 |
0.0017 |
298.15 |
0.1000 |
0.0014 |
298.15 |
0.1500 |
0.0012 |
298.15 |
0.2001 |
0.0011 |
298.15 |
0.2500 |
0.0010 |
298.15 |
0.3000 |
0.0009 |
298.15 |
0.3500 |
0.0008 |
298.15 |
0.4000 |
0.0008 |
298.15 |
0.4500 |
0.0007 |
298.15 |
0.5000 |
0.0007 |
298.15 |
0.5500 |
0.0006 |
298.15 |
0.6000 |
0.0006 |
298.15 |
0.6500 |
0.0006 |
298.15 |
0.7000 |
0.0005 |
298.15 |
0.7500 |
0.0005 |
298.15 |
0.8000 |
0.0005 |
298.15 |
0.8500 |
0.0005 |
298.15 |
0.9000 |
0.0005 |
298.15 |
0.9500 |
0.0005 |
298.15 |
1.0000 |
0.0005 |
308.15 |
0.0000 |
0.0015 |
308.15 |
0.0500 |
0.0013 |
308.15 |
0.1000 |
0.0011 |
308.15 |
0.1500 |
0.0010 |
308.15 |
0.2001 |
0.0009 |
308.15 |
0.2500 |
0.0008 |
308.15 |
0.3000 |
0.0008 |
308.15 |
0.3500 |
0.0007 |
308.15 |
0.4000 |
0.0006 |
308.15 |
0.4500 |
0.0006 |
308.15 |
0.5000 |
0.0006 |
308.15 |
0.5500 |
0.0005 |
308.15 |
0.6000 |
0.0005 |
308.15 |
0.6500 |
0.0005 |
308.15 |
0.7000 |
0.0005 |
308.15 |
0.7500 |
0.0005 |
308.15 |
0.8000 |
0.0005 |
308.15 |
0.8500 |
0.0005 |
308.15 |
0.9000 |
0.0004 |
308.15 |
0.9500 |
0.0004 |
308.15 |
1.0000 |
0.0004 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
293.00 |
0.0021 |
0.0000 |
303.00 |
0.0015 |
0.0000 |
313.00 |
0.0011 |
0.0983 |
293.00 |
0.0016 |
0.0983 |
303.00 |
0.0011 |
0.0983 |
313.00 |
0.0009 |
0.2085 |
293.00 |
0.0013 |
0.2085 |
303.00 |
0.0009 |
0.2085 |
313.00 |
0.0007 |
0.2911 |
293.00 |
0.0011 |
0.2911 |
303.00 |
0.0007 |
0.2911 |
313.00 |
0.0006 |
0.3728 |
293.00 |
0.0009 |
0.3728 |
303.00 |
0.0006 |
0.3728 |
313.00 |
0.0005 |
0.5014 |
293.00 |
0.0008 |
0.5014 |
303.00 |
0.0006 |
0.5014 |
313.00 |
0.0005 |
0.5976 |
293.00 |
0.0007 |
0.5976 |
303.00 |
0.0005 |
0.5976 |
313.00 |
0.0005 |
0.7483 |
293.00 |
0.0006 |
0.7483 |
303.00 |
0.0005 |
0.7483 |
313.00 |
0.0004 |
0.8001 |
293.00 |
0.0006 |
0.8001 |
303.00 |
0.0005 |
0.8001 |
313.00 |
0.0004 |
0.8939 |
293.00 |
0.0005 |
0.8939 |
303.00 |
0.0004 |
0.8939 |
313.00 |
0.0004 |
1.0000 |
293.00 |
0.0005 |
1.0000 |
303.00 |
0.0004 |
1.0000 |
313.00 |
0.0004 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Viscosity, Pa*s - Liquid |
288.15 |
0.0000 |
0.0028 |
288.15 |
0.0500 |
0.0022 |
288.15 |
0.1000 |
0.0018 |
288.15 |
0.1500 |
0.0016 |
288.15 |
0.2001 |
0.0014 |
288.15 |
0.2500 |
0.0012 |
288.15 |
0.3000 |
0.0011 |
288.15 |
0.3500 |
0.0010 |
288.15 |
0.4000 |
0.0009 |
288.15 |
0.4500 |
0.0008 |
288.15 |
0.5000 |
0.0008 |
288.15 |
0.5500 |
0.0007 |
288.15 |
0.6000 |
0.0007 |
288.15 |
0.6500 |
0.0006 |
288.15 |
0.7000 |
0.0006 |
288.15 |
0.7500 |
0.0006 |
288.15 |
0.8000 |
0.0006 |
288.15 |
0.8500 |
0.0006 |
288.15 |
0.9000 |
0.0005 |
288.15 |
0.9500 |
0.0005 |
288.15 |
1.0000 |
0.0005 |
298.15 |
0.0000 |
0.0020 |
298.15 |
0.0500 |
0.0017 |
298.15 |
0.1000 |
0.0014 |
298.15 |
0.1500 |
0.0012 |
298.15 |
0.2001 |
0.0011 |
298.15 |
0.2500 |
0.0010 |
298.15 |
0.3000 |
0.0009 |
298.15 |
0.3500 |
0.0008 |
298.15 |
0.4000 |
0.0008 |
298.15 |
0.4500 |
0.0007 |
298.15 |
0.5000 |
0.0007 |
298.15 |
0.5500 |
0.0006 |
298.15 |
0.6000 |
0.0006 |
298.15 |
0.6500 |
0.0006 |
298.15 |
0.7000 |
0.0005 |
298.15 |
0.7500 |
0.0005 |
298.15 |
0.8000 |
0.0005 |
298.15 |
0.8500 |
0.0005 |
298.15 |
0.9000 |
0.0005 |
298.15 |
0.9500 |
0.0005 |
298.15 |
1.0000 |
0.0005 |
308.15 |
0.0000 |
0.0015 |
308.15 |
0.0500 |
0.0013 |
308.15 |
0.1000 |
0.0011 |
308.15 |
0.1500 |
0.0010 |
308.15 |
0.2001 |
0.0009 |
308.15 |
0.2500 |
0.0008 |
308.15 |
0.3000 |
0.0008 |
308.15 |
0.3500 |
0.0007 |
308.15 |
0.4000 |
0.0006 |
308.15 |
0.4500 |
0.0006 |
308.15 |
0.5000 |
0.0006 |
308.15 |
0.5500 |
0.0005 |
308.15 |
0.6000 |
0.0005 |
308.15 |
0.6500 |
0.0005 |
308.15 |
0.7000 |
0.0005 |
308.15 |
0.7500 |
0.0005 |
308.15 |
0.8000 |
0.0005 |
308.15 |
0.8500 |
0.0005 |
308.15 |
0.9000 |
0.0004 |
308.15 |
0.9500 |
0.0004 |
308.15 |
1.0000 |
0.0004 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3793 |
288.15 |
0.0500 |
1.3808 |
288.15 |
0.1000 |
1.3823 |
288.15 |
0.1500 |
1.3838 |
288.15 |
0.2001 |
1.3852 |
288.15 |
0.2500 |
1.3866 |
288.15 |
0.3000 |
1.388 |
288.15 |
0.3500 |
1.3895 |
288.15 |
0.4000 |
1.3909 |
288.15 |
0.4500 |
1.3923 |
288.15 |
0.5000 |
1.3938 |
288.15 |
0.5500 |
1.3953 |
288.15 |
0.6000 |
1.3968 |
288.15 |
0.6500 |
1.3984 |
288.15 |
0.7000 |
1.4 |
288.15 |
0.7500 |
1.4015 |
288.15 |
0.8000 |
1.403 |
288.15 |
0.8500 |
1.4045 |
288.15 |
0.9000 |
1.4059 |
288.15 |
0.9500 |
1.4073 |
288.15 |
1.0000 |
1.4087 |
298.15 |
0.0000 |
1.3752 |
298.15 |
0.0500 |
1.3766 |
298.15 |
0.1000 |
1.378 |
298.15 |
0.1500 |
1.3795 |
298.15 |
0.2001 |
1.3809 |
298.15 |
0.2500 |
1.3823 |
298.15 |
0.3000 |
1.3837 |
298.15 |
0.3500 |
1.3852 |
298.15 |
0.4000 |
1.3867 |
298.15 |
0.4500 |
1.3882 |
298.15 |
0.5000 |
1.3897 |
298.15 |
0.5500 |
1.3912 |
298.15 |
0.6000 |
1.3927 |
298.15 |
0.6500 |
1.3942 |
298.15 |
0.7000 |
1.3958 |
298.15 |
0.7500 |
1.3974 |
298.15 |
0.8000 |
1.3989 |
298.15 |
0.8500 |
1.4004 |
298.15 |
0.9000 |
1.4019 |
298.15 |
0.9500 |
1.4034 |
298.15 |
1.0000 |
1.4049 |
308.15 |
0.0000 |
1.3706 |
308.15 |
0.0500 |
1.3719 |
308.15 |
0.1000 |
1.3733 |
308.15 |
0.1500 |
1.3746 |
308.15 |
0.2001 |
1.376 |
308.15 |
0.2500 |
1.3774 |
308.15 |
0.3000 |
1.3787 |
308.15 |
0.3500 |
1.3802 |
308.15 |
0.4000 |
1.3816 |
308.15 |
0.4500 |
1.3831 |
308.15 |
0.5000 |
1.3845 |
308.15 |
0.5500 |
1.386 |
308.15 |
0.6000 |
1.3875 |
308.15 |
0.6500 |
1.389 |
308.15 |
0.7000 |
1.3905 |
308.15 |
0.7500 |
1.392 |
308.15 |
0.8000 |
1.3935 |
308.15 |
0.8500 |
1.395 |
308.15 |
0.9000 |
1.3965 |
308.15 |
0.9500 |
1.398 |
308.15 |
1.0000 |
1.3995 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3793 |
288.15 |
0.0500 |
1.3808 |
288.15 |
0.1000 |
1.3823 |
288.15 |
0.1500 |
1.3838 |
288.15 |
0.2001 |
1.3852 |
288.15 |
0.2500 |
1.3866 |
288.15 |
0.3000 |
1.388 |
288.15 |
0.3500 |
1.3895 |
288.15 |
0.4000 |
1.3909 |
288.15 |
0.4500 |
1.3923 |
288.15 |
0.5000 |
1.3938 |
288.15 |
0.5500 |
1.3953 |
288.15 |
0.6000 |
1.3968 |
288.15 |
0.6500 |
1.3984 |
288.15 |
0.7000 |
1.4 |
288.15 |
0.7500 |
1.4015 |
288.15 |
0.8000 |
1.403 |
288.15 |
0.8500 |
1.4045 |
288.15 |
0.9000 |
1.4059 |
288.15 |
0.9500 |
1.4073 |
288.15 |
1.0000 |
1.4087 |
298.15 |
0.0000 |
1.3752 |
298.15 |
0.0500 |
1.3766 |
298.15 |
0.1000 |
1.378 |
298.15 |
0.1500 |
1.3795 |
298.15 |
0.2001 |
1.3809 |
298.15 |
0.2500 |
1.3823 |
298.15 |
0.3000 |
1.3837 |
298.15 |
0.3500 |
1.3852 |
298.15 |
0.4000 |
1.3867 |
298.15 |
0.4500 |
1.3882 |
298.15 |
0.5000 |
1.3897 |
298.15 |
0.5500 |
1.3912 |
298.15 |
0.6000 |
1.3927 |
298.15 |
0.6500 |
1.3942 |
298.15 |
0.7000 |
1.3958 |
298.15 |
0.7500 |
1.3974 |
298.15 |
0.8000 |
1.3989 |
298.15 |
0.8500 |
1.4004 |
298.15 |
0.9000 |
1.4019 |
298.15 |
0.9500 |
1.4034 |
298.15 |
1.0000 |
1.4049 |
308.15 |
0.0000 |
1.3706 |
308.15 |
0.0500 |
1.3719 |
308.15 |
0.1000 |
1.3733 |
308.15 |
0.1500 |
1.3746 |
308.15 |
0.2001 |
1.376 |
308.15 |
0.2500 |
1.3774 |
308.15 |
0.3000 |
1.3787 |
308.15 |
0.3500 |
1.3802 |
308.15 |
0.4000 |
1.3816 |
308.15 |
0.4500 |
1.3831 |
308.15 |
0.5000 |
1.3845 |
308.15 |
0.5500 |
1.386 |
308.15 |
0.6000 |
1.3875 |
308.15 |
0.6500 |
1.389 |
308.15 |
0.7000 |
1.3905 |
308.15 |
0.7500 |
1.392 |
308.15 |
0.8000 |
1.3935 |
308.15 |
0.8500 |
1.395 |
308.15 |
0.9000 |
1.3965 |
308.15 |
0.9500 |
1.398 |
308.15 |
1.0000 |
1.3995 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
789.53 |
288.15 |
0.0500 |
794.84 |
288.15 |
0.1000 |
800.09 |
288.15 |
0.1500 |
805.28 |
288.15 |
0.2001 |
810.47 |
288.15 |
0.2500 |
815.62 |
288.15 |
0.3000 |
820.77 |
288.15 |
0.3500 |
825.9 |
288.15 |
0.4000 |
831.03 |
288.15 |
0.4500 |
836.15 |
288.15 |
0.5000 |
841.26 |
288.15 |
0.5500 |
846.4 |
288.15 |
0.6000 |
851.53 |
288.15 |
0.6500 |
856.68 |
288.15 |
0.7000 |
861.84 |
288.15 |
0.7500 |
867.01 |
288.15 |
0.8000 |
872.19 |
288.15 |
0.8500 |
877.41 |
288.15 |
0.9000 |
882.64 |
288.15 |
0.9500 |
887.78 |
288.15 |
1.0000 |
893.02 |
298.15 |
0.0000 |
781.16 |
298.15 |
0.0500 |
786.31 |
298.15 |
0.1000 |
791.35 |
298.15 |
0.1500 |
796.35 |
298.15 |
0.2001 |
801.35 |
298.15 |
0.2500 |
806.34 |
298.15 |
0.3000 |
811.33 |
298.15 |
0.3500 |
816.33 |
298.15 |
0.4000 |
821.31 |
298.15 |
0.4500 |
826.3 |
298.15 |
0.5000 |
831.29 |
298.15 |
0.5500 |
836.32 |
298.15 |
0.6000 |
841.35 |
298.15 |
0.6500 |
846.39 |
298.15 |
0.7000 |
851.45 |
298.15 |
0.7500 |
856.52 |
298.15 |
0.8000 |
861.66 |
298.15 |
0.8500 |
866.81 |
298.15 |
0.9000 |
872.02 |
298.15 |
0.9500 |
877.21 |
298.15 |
1.0000 |
882.37 |
308.15 |
0.0000 |
772.52 |
308.15 |
0.0500 |
777.45 |
308.15 |
0.1000 |
782.29 |
308.15 |
0.1500 |
787.13 |
308.15 |
0.2001 |
791.97 |
308.15 |
0.2500 |
796.83 |
308.15 |
0.3000 |
801.67 |
308.15 |
0.3500 |
806.53 |
308.15 |
0.4000 |
811.39 |
308.15 |
0.4500 |
816.28 |
308.15 |
0.5000 |
821.17 |
308.15 |
0.5500 |
826.06 |
308.15 |
0.6000 |
830.96 |
308.15 |
0.6500 |
835.86 |
308.15 |
0.7000 |
840.81 |
308.15 |
0.7500 |
845.8 |
308.15 |
0.8000 |
850.82 |
308.15 |
0.8500 |
855.87 |
308.15 |
0.9000 |
860.97 |
308.15 |
0.9500 |
866.17 |
308.15 |
1.0000 |
871.33 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
789.53 |
288.15 |
0.0500 |
794.84 |
288.15 |
0.1000 |
800.09 |
288.15 |
0.1500 |
805.28 |
288.15 |
0.2001 |
810.47 |
288.15 |
0.2500 |
815.62 |
288.15 |
0.3000 |
820.77 |
288.15 |
0.3500 |
825.9 |
288.15 |
0.4000 |
831.03 |
288.15 |
0.4500 |
836.15 |
288.15 |
0.5000 |
841.26 |
288.15 |
0.5500 |
846.4 |
288.15 |
0.6000 |
851.53 |
288.15 |
0.6500 |
856.68 |
288.15 |
0.7000 |
861.84 |
288.15 |
0.7500 |
867.01 |
288.15 |
0.8000 |
872.19 |
288.15 |
0.8500 |
877.41 |
288.15 |
0.9000 |
882.64 |
288.15 |
0.9500 |
887.78 |
288.15 |
1.0000 |
893.02 |
298.15 |
0.0000 |
781.16 |
298.15 |
0.0500 |
786.31 |
298.15 |
0.1000 |
791.35 |
298.15 |
0.1500 |
796.35 |
298.15 |
0.2001 |
801.35 |
298.15 |
0.2500 |
806.34 |
298.15 |
0.3000 |
811.33 |
298.15 |
0.3500 |
816.33 |
298.15 |
0.4000 |
821.31 |
298.15 |
0.4500 |
826.3 |
298.15 |
0.5000 |
831.29 |
298.15 |
0.5500 |
836.32 |
298.15 |
0.6000 |
841.35 |
298.15 |
0.6500 |
846.39 |
298.15 |
0.7000 |
851.45 |
298.15 |
0.7500 |
856.52 |
298.15 |
0.8000 |
861.66 |
298.15 |
0.8500 |
866.81 |
298.15 |
0.9000 |
872.02 |
298.15 |
0.9500 |
877.21 |
298.15 |
1.0000 |
882.37 |
308.15 |
0.0000 |
772.52 |
308.15 |
0.0500 |
777.45 |
308.15 |
0.1000 |
782.29 |
308.15 |
0.1500 |
787.13 |
308.15 |
0.2001 |
791.97 |
308.15 |
0.2500 |
796.83 |
308.15 |
0.3000 |
801.67 |
308.15 |
0.3500 |
806.53 |
308.15 |
0.4000 |
811.39 |
308.15 |
0.4500 |
816.28 |
308.15 |
0.5000 |
821.17 |
308.15 |
0.5500 |
826.06 |
308.15 |
0.6000 |
830.96 |
308.15 |
0.6500 |
835.86 |
308.15 |
0.7000 |
840.81 |
308.15 |
0.7500 |
845.8 |
308.15 |
0.8000 |
850.82 |
308.15 |
0.8500 |
855.87 |
308.15 |
0.9000 |
860.97 |
308.15 |
0.9500 |
866.17 |
308.15 |
1.0000 |
871.33 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
293.00 |
1140.0 |
0.0000 |
303.00 |
1114.0 |
0.0000 |
313.00 |
1085.0 |
0.0983 |
293.00 |
1151.0 |
0.0983 |
303.00 |
1123.0 |
0.0983 |
313.00 |
1093.0 |
0.2085 |
293.00 |
1165.0 |
0.2085 |
303.00 |
1136.0 |
0.2085 |
313.00 |
1103.0 |
0.2911 |
293.00 |
1176.0 |
0.2911 |
303.00 |
1145.0 |
0.2911 |
313.00 |
1110.0 |
0.3728 |
293.00 |
1187.0 |
0.3728 |
303.00 |
1155.0 |
0.3728 |
313.00 |
1118.0 |
0.5014 |
293.00 |
1206.0 |
0.5014 |
303.00 |
1170.0 |
0.5014 |
313.00 |
1131.0 |
0.5976 |
293.00 |
1222.0 |
0.5976 |
303.00 |
1183.0 |
0.5976 |
313.00 |
1142.0 |
0.7483 |
293.00 |
1248.0 |
0.7483 |
303.00 |
1207.0 |
0.7483 |
313.00 |
1162.0 |
0.8001 |
293.00 |
1258.0 |
0.8001 |
303.00 |
1216.0 |
0.8001 |
313.00 |
1170.0 |
0.8939 |
293.00 |
1278.0 |
0.8939 |
303.00 |
1232.0 |
0.8939 |
313.00 |
1185.0 |
1.0000 |
293.00 |
1302.0 |
1.0000 |
303.00 |
1254.0 |
1.0000 |
313.00 |
1202.0 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
293.00 |
1140.0 |
0.0000 |
303.00 |
1114.0 |
0.0000 |
313.00 |
1085.0 |
0.0983 |
293.00 |
1151.0 |
0.0983 |
303.00 |
1123.0 |
0.0983 |
313.00 |
1093.0 |
0.2085 |
293.00 |
1165.0 |
0.2085 |
303.00 |
1136.0 |
0.2085 |
313.00 |
1103.0 |
0.2911 |
293.00 |
1176.0 |
0.2911 |
303.00 |
1145.0 |
0.2911 |
313.00 |
1110.0 |
0.3728 |
293.00 |
1187.0 |
0.3728 |
303.00 |
1155.0 |
0.3728 |
313.00 |
1118.0 |
0.5014 |
293.00 |
1206.0 |
0.5014 |
303.00 |
1170.0 |
0.5014 |
313.00 |
1131.0 |
0.5976 |
293.00 |
1222.0 |
0.5976 |
303.00 |
1183.0 |
0.5976 |
313.00 |
1142.0 |
0.7483 |
293.00 |
1248.0 |
0.7483 |
303.00 |
1207.0 |
0.7483 |
313.00 |
1162.0 |
0.8001 |
293.00 |
1258.0 |
0.8001 |
303.00 |
1216.0 |
0.8001 |
313.00 |
1170.0 |
0.8939 |
293.00 |
1278.0 |
0.8939 |
303.00 |
1232.0 |
0.8939 |
313.00 |
1185.0 |
1.0000 |
293.00 |
1302.0 |
1.0000 |
303.00 |
1254.0 |
1.0000 |
313.00 |
1202.0 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
288.15 |
0.0000 |
0.0217 |
288.15 |
0.0500 |
0.0222 |
288.15 |
0.1000 |
0.0225 |
288.15 |
0.1500 |
0.0228 |
288.15 |
0.2001 |
0.0231 |
288.15 |
0.2500 |
0.0234 |
288.15 |
0.3000 |
0.0237 |
288.15 |
0.3500 |
0.0239 |
288.15 |
0.4000 |
0.0242 |
288.15 |
0.4500 |
0.0245 |
288.15 |
0.5000 |
0.0248 |
288.15 |
0.5500 |
0.0251 |
288.15 |
0.6000 |
0.0255 |
288.15 |
0.6500 |
0.0258 |
288.15 |
0.7000 |
0.0262 |
288.15 |
0.7500 |
0.0265 |
288.15 |
0.8000 |
0.0269 |
288.15 |
0.8500 |
0.0272 |
288.15 |
0.9000 |
0.0276 |
288.15 |
0.9500 |
0.0280 |
288.15 |
1.0000 |
0.0284 |
298.15 |
0.0000 |
0.0209 |
298.15 |
0.0500 |
0.0213 |
298.15 |
0.1000 |
0.0216 |
298.15 |
0.1500 |
0.0220 |
298.15 |
0.2001 |
0.0222 |
298.15 |
0.2500 |
0.0225 |
298.15 |
0.3000 |
0.0227 |
298.15 |
0.3500 |
0.0230 |
298.15 |
0.4000 |
0.0232 |
298.15 |
0.4500 |
0.0235 |
298.15 |
0.5000 |
0.0238 |
298.15 |
0.5500 |
0.0240 |
298.15 |
0.6000 |
0.0243 |
298.15 |
0.6500 |
0.0246 |
298.15 |
0.7000 |
0.0250 |
298.15 |
0.7500 |
0.0253 |
298.15 |
0.8000 |
0.0256 |
298.15 |
0.8500 |
0.0260 |
298.15 |
0.9000 |
0.0263 |
298.15 |
0.9500 |
0.0266 |
298.15 |
1.0000 |
0.0270 |
308.15 |
0.0000 |
0.0202 |
308.15 |
0.0500 |
0.0206 |
308.15 |
0.1000 |
0.0209 |
308.15 |
0.1500 |
0.0212 |
308.15 |
0.2001 |
0.0215 |
308.15 |
0.2500 |
0.0217 |
308.15 |
0.3000 |
0.0220 |
308.15 |
0.3500 |
0.0222 |
308.15 |
0.4000 |
0.0225 |
308.15 |
0.4500 |
0.0227 |
308.15 |
0.5000 |
0.0229 |
308.15 |
0.5500 |
0.0232 |
308.15 |
0.6000 |
0.0235 |
308.15 |
0.6500 |
0.0238 |
308.15 |
0.7000 |
0.0241 |
308.15 |
0.7500 |
0.0244 |
308.15 |
0.8000 |
0.0247 |
308.15 |
0.8500 |
0.0250 |
308.15 |
0.9000 |
0.0253 |
308.15 |
0.9500 |
0.0256 |
308.15 |
1.0000 |
0.0260 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Tetrahydrofuran (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
288.15 |
0.0000 |
0.0217 |
288.15 |
0.0500 |
0.0222 |
288.15 |
0.1000 |
0.0225 |
288.15 |
0.1500 |
0.0228 |
288.15 |
0.2001 |
0.0231 |
288.15 |
0.2500 |
0.0234 |
288.15 |
0.3000 |
0.0237 |
288.15 |
0.3500 |
0.0239 |
288.15 |
0.4000 |
0.0242 |
288.15 |
0.4500 |
0.0245 |
288.15 |
0.5000 |
0.0248 |
288.15 |
0.5500 |
0.0251 |
288.15 |
0.6000 |
0.0255 |
288.15 |
0.6500 |
0.0258 |
288.15 |
0.7000 |
0.0262 |
288.15 |
0.7500 |
0.0265 |
288.15 |
0.8000 |
0.0269 |
288.15 |
0.8500 |
0.0272 |
288.15 |
0.9000 |
0.0276 |
288.15 |
0.9500 |
0.0280 |
288.15 |
1.0000 |
0.0284 |
298.15 |
0.0000 |
0.0209 |
298.15 |
0.0500 |
0.0213 |
298.15 |
0.1000 |
0.0216 |
298.15 |
0.1500 |
0.0220 |
298.15 |
0.2001 |
0.0222 |
298.15 |
0.2500 |
0.0225 |
298.15 |
0.3000 |
0.0227 |
298.15 |
0.3500 |
0.0230 |
298.15 |
0.4000 |
0.0232 |
298.15 |
0.4500 |
0.0235 |
298.15 |
0.5000 |
0.0238 |
298.15 |
0.5500 |
0.0240 |
298.15 |
0.6000 |
0.0243 |
298.15 |
0.6500 |
0.0246 |
298.15 |
0.7000 |
0.0250 |
298.15 |
0.7500 |
0.0253 |
298.15 |
0.8000 |
0.0256 |
298.15 |
0.8500 |
0.0260 |
298.15 |
0.9000 |
0.0263 |
298.15 |
0.9500 |
0.0266 |
298.15 |
1.0000 |
0.0270 |
308.15 |
0.0000 |
0.0202 |
308.15 |
0.0500 |
0.0206 |
308.15 |
0.1000 |
0.0209 |
308.15 |
0.1500 |
0.0212 |
308.15 |
0.2001 |
0.0215 |
308.15 |
0.2500 |
0.0217 |
308.15 |
0.3000 |
0.0220 |
308.15 |
0.3500 |
0.0222 |
308.15 |
0.4000 |
0.0225 |
308.15 |
0.4500 |
0.0227 |
308.15 |
0.5000 |
0.0229 |
308.15 |
0.5500 |
0.0232 |
308.15 |
0.6000 |
0.0235 |
308.15 |
0.6500 |
0.0238 |
308.15 |
0.7000 |
0.0241 |
308.15 |
0.7500 |
0.0244 |
308.15 |
0.8000 |
0.0247 |
308.15 |
0.8500 |
0.0250 |
308.15 |
0.9000 |
0.0253 |
308.15 |
0.9500 |
0.0256 |
308.15 |
1.0000 |
0.0260 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
Fixed |
Measured |
T [K] - VLE |
x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
y1[mol/mol] of Tetrahydrofuran (2) - Vapour |
355.38 |
0.0000 |
0.0000 |
353.88 |
0.0500 |
0.1050 |
352.55 |
0.1000 |
0.1957 |
350.33 |
0.2000 |
0.3460 |
348.45 |
0.3000 |
0.4650 |
346.69 |
0.4000 |
0.5651 |
345.0 |
0.5000 |
0.6510 |
343.49 |
0.6000 |
0.7279 |
342.17 |
0.7000 |
0.7991 |
341.0 |
0.8000 |
0.8672 |
339.89 |
0.9000 |
0.9336 |
339.39 |
0.9500 |
0.9667 |
338.88 |
1.0000 |
1.0000 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
79.9 (VLE)
x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
y1[mol/mol] of Tetrahydrofuran (2) - Vapour |
0.9550 |
0.9699 |
0.9800 |
0.9866 |
0.9850 |
0.9900 |
0.9900 |
0.9933 |
0.9950 |
0.9967 |
0.9980 |
0.9987 |
0.9999 |
0.9999 |
1.0000 |
1.0000 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
T [K] - VLE |
x1[mol/mol] of Tetrahydrofuran (2) - Liquid |
354.95 |
0.0000 |
353.95 |
0.0500 |
352.85 |
0.1000 |
350.65 |
0.2000 |
348.55 |
0.3000 |
346.55 |
0.4000 |
344.75 |
0.5000 |
343.35 |
0.6000 |
342.15 |
0.7000 |
340.95 |
0.8000 |
339.95 |
0.9000 |
339.45 |
0.9500 |
338.95 |
1.0000 |
Sources