Datasets
-
Azeotropic composition: mole fraction (4)
-
η - Viscosity, Pa*s (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (2)
-
γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (4)
-
Azeotropic temperature, K (2)
Azeotropic composition: mole fraction of Isopropyl Alcohol (1)
[ref]
| Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid |
| 101.30 |
0.6680 |
Mole fraction of Isopropyl Alcohol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Gas |
| 0.0000 |
0.0000 |
| 0.0820 |
0.1350 |
| 0.1620 |
0.2340 |
| 0.2350 |
0.3060 |
| 0.3010 |
0.3670 |
| 0.3730 |
0.4250 |
| 0.4280 |
0.4710 |
| 0.4870 |
0.5180 |
| 0.5490 |
0.5690 |
| 0.6130 |
0.6220 |
| 0.6560 |
0.6580 |
| 0.7090 |
0.7040 |
| 0.7470 |
0.7390 |
| 0.7920 |
0.7820 |
| 0.8270 |
0.8150 |
| 0.8610 |
0.8500 |
| 0.8910 |
0.8830 |
| 0.9160 |
0.9100 |
| 0.9460 |
0.9420 |
| 0.9770 |
0.9760 |
| 1.0000 |
1.0000 |
Azeotropic composition: mole fraction of Isopropyl Alcohol (1)
[ref]
| Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Isopropyl Alcohol (1) - Liquid |
| 101.30 |
0.6680 |
Mole fraction of Isopropyl Alcohol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Gas |
| 0.0000 |
0.0000 |
| 0.0820 |
0.1350 |
| 0.1620 |
0.2340 |
| 0.2350 |
0.3060 |
| 0.3010 |
0.3670 |
| 0.3730 |
0.4250 |
| 0.4280 |
0.4710 |
| 0.4870 |
0.5180 |
| 0.5490 |
0.5690 |
| 0.6130 |
0.6220 |
| 0.6560 |
0.6580 |
| 0.7090 |
0.7040 |
| 0.7470 |
0.7390 |
| 0.7920 |
0.7820 |
| 0.8270 |
0.8150 |
| 0.8610 |
0.8500 |
| 0.8910 |
0.8830 |
| 0.9160 |
0.9100 |
| 0.9460 |
0.9420 |
| 0.9770 |
0.9760 |
| 1.0000 |
1.0000 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Viscosity, Pa*s - Liquid |
| 293.15 |
0.0000 |
0.0009 |
| 293.15 |
0.0501 |
0.0009 |
| 293.15 |
0.0999 |
0.0008 |
| 293.15 |
0.1499 |
0.0008 |
| 293.15 |
0.2003 |
0.0008 |
| 293.15 |
0.2506 |
0.0009 |
| 293.15 |
0.2999 |
0.0009 |
| 293.15 |
0.3500 |
0.0009 |
| 293.15 |
0.3999 |
0.0009 |
| 293.15 |
0.4499 |
0.0009 |
| 293.15 |
0.5001 |
0.0009 |
| 293.15 |
0.5502 |
0.0010 |
| 293.15 |
0.6001 |
0.0010 |
| 293.15 |
0.6499 |
0.0011 |
| 293.15 |
0.7001 |
0.0012 |
| 293.15 |
0.7499 |
0.0013 |
| 293.15 |
0.8000 |
0.0014 |
| 293.15 |
0.8501 |
0.0015 |
| 293.15 |
0.9001 |
0.0017 |
| 293.15 |
0.9499 |
0.0020 |
| 293.15 |
1.0000 |
0.0024 |
| 303.15 |
0.0000 |
0.0007 |
| 303.15 |
0.0502 |
0.0007 |
| 303.15 |
0.1001 |
0.0007 |
| 303.15 |
0.1501 |
0.0007 |
| 303.15 |
0.1998 |
0.0007 |
| 303.15 |
0.2499 |
0.0007 |
| 303.15 |
0.3000 |
0.0007 |
| 303.15 |
0.3499 |
0.0008 |
| 303.15 |
0.4001 |
0.0008 |
| 303.15 |
0.4501 |
0.0008 |
| 303.15 |
0.5001 |
0.0008 |
| 303.15 |
0.5500 |
0.0008 |
| 303.15 |
0.6000 |
0.0009 |
| 303.15 |
0.6500 |
0.0009 |
| 303.15 |
0.6999 |
0.0010 |
| 303.15 |
0.7499 |
0.0010 |
| 303.15 |
0.8001 |
0.0011 |
| 303.15 |
0.8500 |
0.0012 |
| 303.15 |
0.8998 |
0.0014 |
| 303.15 |
0.9499 |
0.0015 |
| 303.15 |
1.0000 |
0.0018 |
| 313.15 |
0.0000 |
0.0007 |
| 313.15 |
0.0500 |
0.0006 |
| 313.15 |
0.1000 |
0.0006 |
| 313.15 |
0.1501 |
0.0006 |
| 313.15 |
0.2000 |
0.0006 |
| 313.15 |
0.2499 |
0.0006 |
| 313.15 |
0.2997 |
0.0006 |
| 313.15 |
0.3499 |
0.0006 |
| 313.15 |
0.4000 |
0.0007 |
| 313.15 |
0.4504 |
0.0007 |
| 313.15 |
0.5001 |
0.0007 |
| 313.15 |
0.5500 |
0.0007 |
| 313.15 |
0.5999 |
0.0007 |
| 313.15 |
0.6500 |
0.0008 |
| 313.15 |
0.7001 |
0.0008 |
| 313.15 |
0.7502 |
0.0008 |
| 313.15 |
0.7999 |
0.0009 |
| 313.15 |
0.8500 |
0.0010 |
| 313.15 |
0.8998 |
0.0011 |
| 313.15 |
0.9498 |
0.0012 |
| 313.15 |
1.0000 |
0.0013 |
| 323.15 |
0.0000 |
0.0006 |
| 323.15 |
0.0500 |
0.0006 |
| 323.15 |
0.1000 |
0.0006 |
| 323.15 |
0.1501 |
0.0006 |
| 323.15 |
0.2000 |
0.0006 |
| 323.15 |
0.2499 |
0.0006 |
| 323.15 |
0.2997 |
0.0006 |
| 323.15 |
0.3499 |
0.0006 |
| 323.15 |
0.4000 |
0.0006 |
| 323.15 |
0.4504 |
0.0006 |
| 323.15 |
0.5001 |
0.0006 |
| 323.15 |
0.5501 |
0.0006 |
| 323.15 |
0.6000 |
0.0006 |
| 323.15 |
0.6500 |
0.0006 |
| 323.15 |
0.6999 |
0.0007 |
| 323.15 |
0.7502 |
0.0007 |
| 323.15 |
0.8002 |
0.0007 |
| 323.15 |
0.8501 |
0.0008 |
| 323.15 |
0.8998 |
0.0008 |
| 323.15 |
0.9501 |
0.0009 |
| 323.15 |
1.0000 |
0.0010 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Viscosity, Pa*s - Liquid |
| 293.15 |
0.0000 |
0.0009 |
| 293.15 |
0.0501 |
0.0009 |
| 293.15 |
0.0999 |
0.0008 |
| 293.15 |
0.1499 |
0.0008 |
| 293.15 |
0.2003 |
0.0008 |
| 293.15 |
0.2506 |
0.0009 |
| 293.15 |
0.2999 |
0.0009 |
| 293.15 |
0.3500 |
0.0009 |
| 293.15 |
0.3999 |
0.0009 |
| 293.15 |
0.4499 |
0.0009 |
| 293.15 |
0.5001 |
0.0009 |
| 293.15 |
0.5502 |
0.0010 |
| 293.15 |
0.6001 |
0.0010 |
| 293.15 |
0.6499 |
0.0011 |
| 293.15 |
0.7001 |
0.0012 |
| 293.15 |
0.7499 |
0.0013 |
| 293.15 |
0.8000 |
0.0014 |
| 293.15 |
0.8501 |
0.0015 |
| 293.15 |
0.9001 |
0.0017 |
| 293.15 |
0.9499 |
0.0020 |
| 293.15 |
1.0000 |
0.0024 |
| 303.15 |
0.0000 |
0.0007 |
| 303.15 |
0.0502 |
0.0007 |
| 303.15 |
0.1001 |
0.0007 |
| 303.15 |
0.1501 |
0.0007 |
| 303.15 |
0.1998 |
0.0007 |
| 303.15 |
0.2499 |
0.0007 |
| 303.15 |
0.3000 |
0.0007 |
| 303.15 |
0.3499 |
0.0008 |
| 303.15 |
0.4001 |
0.0008 |
| 303.15 |
0.4501 |
0.0008 |
| 303.15 |
0.5001 |
0.0008 |
| 303.15 |
0.5500 |
0.0008 |
| 303.15 |
0.6000 |
0.0009 |
| 303.15 |
0.6500 |
0.0009 |
| 303.15 |
0.6999 |
0.0010 |
| 303.15 |
0.7499 |
0.0010 |
| 303.15 |
0.8001 |
0.0011 |
| 303.15 |
0.8500 |
0.0012 |
| 303.15 |
0.8998 |
0.0014 |
| 303.15 |
0.9499 |
0.0015 |
| 303.15 |
1.0000 |
0.0018 |
| 313.15 |
0.0000 |
0.0007 |
| 313.15 |
0.0500 |
0.0006 |
| 313.15 |
0.1000 |
0.0006 |
| 313.15 |
0.1501 |
0.0006 |
| 313.15 |
0.2000 |
0.0006 |
| 313.15 |
0.2499 |
0.0006 |
| 313.15 |
0.2997 |
0.0006 |
| 313.15 |
0.3499 |
0.0006 |
| 313.15 |
0.4000 |
0.0007 |
| 313.15 |
0.4504 |
0.0007 |
| 313.15 |
0.5001 |
0.0007 |
| 313.15 |
0.5500 |
0.0007 |
| 313.15 |
0.5999 |
0.0007 |
| 313.15 |
0.6500 |
0.0008 |
| 313.15 |
0.7001 |
0.0008 |
| 313.15 |
0.7502 |
0.0008 |
| 313.15 |
0.7999 |
0.0009 |
| 313.15 |
0.8500 |
0.0010 |
| 313.15 |
0.8998 |
0.0011 |
| 313.15 |
0.9498 |
0.0012 |
| 313.15 |
1.0000 |
0.0013 |
| 323.15 |
0.0000 |
0.0006 |
| 323.15 |
0.0500 |
0.0006 |
| 323.15 |
0.1000 |
0.0006 |
| 323.15 |
0.1501 |
0.0006 |
| 323.15 |
0.2000 |
0.0006 |
| 323.15 |
0.2499 |
0.0006 |
| 323.15 |
0.2997 |
0.0006 |
| 323.15 |
0.3499 |
0.0006 |
| 323.15 |
0.4000 |
0.0006 |
| 323.15 |
0.4504 |
0.0006 |
| 323.15 |
0.5001 |
0.0006 |
| 323.15 |
0.5501 |
0.0006 |
| 323.15 |
0.6000 |
0.0006 |
| 323.15 |
0.6500 |
0.0006 |
| 323.15 |
0.6999 |
0.0007 |
| 323.15 |
0.7502 |
0.0007 |
| 323.15 |
0.8002 |
0.0007 |
| 323.15 |
0.8501 |
0.0008 |
| 323.15 |
0.8998 |
0.0008 |
| 323.15 |
0.9501 |
0.0009 |
| 323.15 |
1.0000 |
0.0010 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 293.15 |
0.0000 |
1.3916 |
| 293.15 |
0.0501 |
1.3908 |
| 293.15 |
0.0999 |
1.3902 |
| 293.15 |
0.1499 |
1.3895 |
| 293.15 |
0.2003 |
1.389 |
| 293.15 |
0.2506 |
1.3884 |
| 293.15 |
0.2999 |
1.3878 |
| 293.15 |
0.3500 |
1.3872 |
| 293.15 |
0.3999 |
1.3866 |
| 293.15 |
0.4499 |
1.386 |
| 293.15 |
0.5001 |
1.3854 |
| 293.15 |
0.5502 |
1.3848 |
| 293.15 |
0.6001 |
1.3841 |
| 293.15 |
0.6499 |
1.3835 |
| 293.15 |
0.7001 |
1.3827 |
| 293.15 |
0.7499 |
1.3819 |
| 293.15 |
0.8000 |
1.3811 |
| 293.15 |
0.8501 |
1.3802 |
| 293.15 |
0.9001 |
1.3793 |
| 293.15 |
0.9499 |
1.3783 |
| 293.15 |
1.0000 |
1.3772 |
| 303.15 |
0.0000 |
1.3866 |
| 303.15 |
0.0502 |
1.3857 |
| 303.15 |
0.1001 |
1.385 |
| 303.15 |
0.1501 |
1.3844 |
| 303.15 |
0.1998 |
1.3838 |
| 303.15 |
0.2499 |
1.3832 |
| 303.15 |
0.3000 |
1.3826 |
| 303.15 |
0.3499 |
1.382 |
| 303.15 |
0.4001 |
1.3814 |
| 303.15 |
0.4501 |
1.3809 |
| 303.15 |
0.5001 |
1.3803 |
| 303.15 |
0.5500 |
1.3797 |
| 303.15 |
0.6000 |
1.379 |
| 303.15 |
0.6500 |
1.3784 |
| 303.15 |
0.6999 |
1.3778 |
| 303.15 |
0.7499 |
1.377 |
| 303.15 |
0.8001 |
1.3763 |
| 303.15 |
0.8500 |
1.3755 |
| 303.15 |
0.8998 |
1.3747 |
| 303.15 |
0.9499 |
1.3738 |
| 303.15 |
1.0000 |
1.3729 |
| 313.15 |
0.0000 |
1.3814 |
| 313.15 |
0.0500 |
1.3806 |
| 313.15 |
0.1000 |
1.38 |
| 313.15 |
0.1501 |
1.3793 |
| 313.15 |
0.2000 |
1.3787 |
| 313.15 |
0.2499 |
1.3781 |
| 313.15 |
0.2997 |
1.3775 |
| 313.15 |
0.3499 |
1.3769 |
| 313.15 |
0.4000 |
1.3763 |
| 313.15 |
0.4504 |
1.3757 |
| 313.15 |
0.5001 |
1.3751 |
| 313.15 |
0.5500 |
1.3746 |
| 313.15 |
0.5999 |
1.374 |
| 313.15 |
0.6500 |
1.3734 |
| 313.15 |
0.7001 |
1.3728 |
| 313.15 |
0.7502 |
1.3722 |
| 313.15 |
0.7999 |
1.3715 |
| 313.15 |
0.8500 |
1.3708 |
| 313.15 |
0.8998 |
1.37 |
| 313.15 |
0.9498 |
1.3693 |
| 313.15 |
1.0000 |
1.3685 |
| 323.15 |
0.0000 |
1.3763 |
| 323.15 |
0.0500 |
1.3752 |
| 323.15 |
0.1000 |
1.3744 |
| 323.15 |
0.1501 |
1.3738 |
| 323.15 |
0.2000 |
1.3731 |
| 323.15 |
0.2499 |
1.3725 |
| 323.15 |
0.2997 |
1.3719 |
| 323.15 |
0.3499 |
1.3713 |
| 323.15 |
0.4000 |
1.3707 |
| 323.15 |
0.4504 |
1.3701 |
| 323.15 |
0.5001 |
1.3695 |
| 323.15 |
0.5501 |
1.369 |
| 323.15 |
0.6000 |
1.3684 |
| 323.15 |
0.6500 |
1.3679 |
| 323.15 |
0.6999 |
1.3673 |
| 323.15 |
0.7502 |
1.3666 |
| 323.15 |
0.8002 |
1.3661 |
| 323.15 |
0.8501 |
1.3654 |
| 323.15 |
0.8998 |
1.3648 |
| 323.15 |
0.9501 |
1.3642 |
| 323.15 |
1.0000 |
1.3636 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
| 293.15 |
0.0000 |
1.3916 |
| 293.15 |
0.0501 |
1.3908 |
| 293.15 |
0.0999 |
1.3902 |
| 293.15 |
0.1499 |
1.3895 |
| 293.15 |
0.2003 |
1.389 |
| 293.15 |
0.2506 |
1.3884 |
| 293.15 |
0.2999 |
1.3878 |
| 293.15 |
0.3500 |
1.3872 |
| 293.15 |
0.3999 |
1.3866 |
| 293.15 |
0.4499 |
1.386 |
| 293.15 |
0.5001 |
1.3854 |
| 293.15 |
0.5502 |
1.3848 |
| 293.15 |
0.6001 |
1.3841 |
| 293.15 |
0.6499 |
1.3835 |
| 293.15 |
0.7001 |
1.3827 |
| 293.15 |
0.7499 |
1.3819 |
| 293.15 |
0.8000 |
1.3811 |
| 293.15 |
0.8501 |
1.3802 |
| 293.15 |
0.9001 |
1.3793 |
| 293.15 |
0.9499 |
1.3783 |
| 293.15 |
1.0000 |
1.3772 |
| 303.15 |
0.0000 |
1.3866 |
| 303.15 |
0.0502 |
1.3857 |
| 303.15 |
0.1001 |
1.385 |
| 303.15 |
0.1501 |
1.3844 |
| 303.15 |
0.1998 |
1.3838 |
| 303.15 |
0.2499 |
1.3832 |
| 303.15 |
0.3000 |
1.3826 |
| 303.15 |
0.3499 |
1.382 |
| 303.15 |
0.4001 |
1.3814 |
| 303.15 |
0.4501 |
1.3809 |
| 303.15 |
0.5001 |
1.3803 |
| 303.15 |
0.5500 |
1.3797 |
| 303.15 |
0.6000 |
1.379 |
| 303.15 |
0.6500 |
1.3784 |
| 303.15 |
0.6999 |
1.3778 |
| 303.15 |
0.7499 |
1.377 |
| 303.15 |
0.8001 |
1.3763 |
| 303.15 |
0.8500 |
1.3755 |
| 303.15 |
0.8998 |
1.3747 |
| 303.15 |
0.9499 |
1.3738 |
| 303.15 |
1.0000 |
1.3729 |
| 313.15 |
0.0000 |
1.3814 |
| 313.15 |
0.0500 |
1.3806 |
| 313.15 |
0.1000 |
1.38 |
| 313.15 |
0.1501 |
1.3793 |
| 313.15 |
0.2000 |
1.3787 |
| 313.15 |
0.2499 |
1.3781 |
| 313.15 |
0.2997 |
1.3775 |
| 313.15 |
0.3499 |
1.3769 |
| 313.15 |
0.4000 |
1.3763 |
| 313.15 |
0.4504 |
1.3757 |
| 313.15 |
0.5001 |
1.3751 |
| 313.15 |
0.5500 |
1.3746 |
| 313.15 |
0.5999 |
1.374 |
| 313.15 |
0.6500 |
1.3734 |
| 313.15 |
0.7001 |
1.3728 |
| 313.15 |
0.7502 |
1.3722 |
| 313.15 |
0.7999 |
1.3715 |
| 313.15 |
0.8500 |
1.3708 |
| 313.15 |
0.8998 |
1.37 |
| 313.15 |
0.9498 |
1.3693 |
| 313.15 |
1.0000 |
1.3685 |
| 323.15 |
0.0000 |
1.3763 |
| 323.15 |
0.0500 |
1.3752 |
| 323.15 |
0.1000 |
1.3744 |
| 323.15 |
0.1501 |
1.3738 |
| 323.15 |
0.2000 |
1.3731 |
| 323.15 |
0.2499 |
1.3725 |
| 323.15 |
0.2997 |
1.3719 |
| 323.15 |
0.3499 |
1.3713 |
| 323.15 |
0.4000 |
1.3707 |
| 323.15 |
0.4504 |
1.3701 |
| 323.15 |
0.5001 |
1.3695 |
| 323.15 |
0.5501 |
1.369 |
| 323.15 |
0.6000 |
1.3684 |
| 323.15 |
0.6500 |
1.3679 |
| 323.15 |
0.6999 |
1.3673 |
| 323.15 |
0.7502 |
1.3666 |
| 323.15 |
0.8002 |
1.3661 |
| 323.15 |
0.8501 |
1.3654 |
| 323.15 |
0.8998 |
1.3648 |
| 323.15 |
0.9501 |
1.3642 |
| 323.15 |
1.0000 |
1.3636 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 293.15 |
0.0000 |
884.27 |
| 293.15 |
0.0501 |
879.89 |
| 293.15 |
0.0999 |
875.5 |
| 293.15 |
0.1499 |
871.09 |
| 293.15 |
0.2003 |
866.62 |
| 293.15 |
0.2506 |
862.13 |
| 293.15 |
0.2999 |
857.7 |
| 293.15 |
0.3500 |
853.13 |
| 293.15 |
0.3999 |
848.52 |
| 293.15 |
0.4499 |
843.87 |
| 293.15 |
0.5001 |
839.07 |
| 293.15 |
0.5502 |
834.22 |
| 293.15 |
0.6001 |
829.28 |
| 293.15 |
0.6499 |
824.23 |
| 293.15 |
0.7001 |
819.03 |
| 293.15 |
0.7499 |
813.78 |
| 293.15 |
0.8000 |
808.34 |
| 293.15 |
0.8501 |
802.8 |
| 293.15 |
0.9001 |
797.15 |
| 293.15 |
0.9499 |
791.36 |
| 293.15 |
1.0000 |
785.44 |
| 303.15 |
0.0000 |
874.07 |
| 303.15 |
0.0502 |
869.6 |
| 303.15 |
0.1001 |
865.24 |
| 303.15 |
0.1501 |
860.87 |
| 303.15 |
0.1998 |
856.52 |
| 303.15 |
0.2499 |
852.09 |
| 303.15 |
0.3000 |
847.66 |
| 303.15 |
0.3499 |
843.17 |
| 303.15 |
0.4001 |
838.59 |
| 303.15 |
0.4501 |
833.98 |
| 303.15 |
0.5001 |
829.29 |
| 303.15 |
0.5500 |
824.54 |
| 303.15 |
0.6000 |
819.65 |
| 303.15 |
0.6500 |
814.69 |
| 303.15 |
0.6999 |
809.62 |
| 303.15 |
0.7499 |
804.47 |
| 303.15 |
0.8001 |
799.17 |
| 303.15 |
0.8500 |
793.77 |
| 303.15 |
0.8998 |
788.25 |
| 303.15 |
0.9499 |
782.59 |
| 303.15 |
1.0000 |
776.75 |
| 313.15 |
0.0000 |
863.76 |
| 313.15 |
0.0500 |
859.32 |
| 313.15 |
0.1000 |
854.97 |
| 313.15 |
0.1501 |
850.64 |
| 313.15 |
0.2000 |
846.27 |
| 313.15 |
0.2499 |
841.92 |
| 313.15 |
0.2997 |
837.55 |
| 313.15 |
0.3499 |
833.09 |
| 313.15 |
0.4000 |
828.58 |
| 313.15 |
0.4504 |
823.98 |
| 313.15 |
0.5001 |
819.37 |
| 313.15 |
0.5500 |
814.68 |
| 313.15 |
0.5999 |
809.9 |
| 313.15 |
0.6500 |
805.04 |
| 313.15 |
0.7001 |
800.07 |
| 313.15 |
0.7502 |
794.95 |
| 313.15 |
0.7999 |
789.8 |
| 313.15 |
0.8500 |
784.49 |
| 313.15 |
0.8998 |
779.1 |
| 313.15 |
0.9498 |
773.58 |
| 313.15 |
1.0000 |
767.93 |
| 323.15 |
0.0000 |
666.8 |
| 323.15 |
0.0501 |
667.65 |
| 323.15 |
0.1000 |
669.08 |
| 323.15 |
0.1500 |
670.98 |
| 323.15 |
0.1998 |
673.08 |
| 323.15 |
0.2500 |
675.42 |
| 323.15 |
0.3000 |
677.99 |
| 323.15 |
0.3500 |
680.86 |
| 323.15 |
0.4000 |
683.93 |
| 323.15 |
0.4499 |
687.34 |
| 323.15 |
0.5000 |
691.07 |
| 323.15 |
0.5501 |
695.17 |
| 323.15 |
0.6000 |
699.74 |
| 323.15 |
0.6500 |
704.78 |
| 323.15 |
0.7000 |
710.22 |
| 323.15 |
0.7499 |
716.22 |
| 323.15 |
0.7999 |
722.88 |
| 323.15 |
0.8500 |
730.48 |
| 323.15 |
0.9000 |
738.82 |
| 323.15 |
0.9500 |
748.16 |
| 323.15 |
1.0000 |
758.9 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 293.15 |
0.0000 |
884.27 |
| 293.15 |
0.0501 |
879.89 |
| 293.15 |
0.0999 |
875.5 |
| 293.15 |
0.1499 |
871.09 |
| 293.15 |
0.2003 |
866.62 |
| 293.15 |
0.2506 |
862.13 |
| 293.15 |
0.2999 |
857.7 |
| 293.15 |
0.3500 |
853.13 |
| 293.15 |
0.3999 |
848.52 |
| 293.15 |
0.4499 |
843.87 |
| 293.15 |
0.5001 |
839.07 |
| 293.15 |
0.5502 |
834.22 |
| 293.15 |
0.6001 |
829.28 |
| 293.15 |
0.6499 |
824.23 |
| 293.15 |
0.7001 |
819.03 |
| 293.15 |
0.7499 |
813.78 |
| 293.15 |
0.8000 |
808.34 |
| 293.15 |
0.8501 |
802.8 |
| 293.15 |
0.9001 |
797.15 |
| 293.15 |
0.9499 |
791.36 |
| 293.15 |
1.0000 |
785.44 |
| 303.15 |
0.0000 |
874.07 |
| 303.15 |
0.0502 |
869.6 |
| 303.15 |
0.1001 |
865.24 |
| 303.15 |
0.1501 |
860.87 |
| 303.15 |
0.1998 |
856.52 |
| 303.15 |
0.2499 |
852.09 |
| 303.15 |
0.3000 |
847.66 |
| 303.15 |
0.3499 |
843.17 |
| 303.15 |
0.4001 |
838.59 |
| 303.15 |
0.4501 |
833.98 |
| 303.15 |
0.5001 |
829.29 |
| 303.15 |
0.5500 |
824.54 |
| 303.15 |
0.6000 |
819.65 |
| 303.15 |
0.6500 |
814.69 |
| 303.15 |
0.6999 |
809.62 |
| 303.15 |
0.7499 |
804.47 |
| 303.15 |
0.8001 |
799.17 |
| 303.15 |
0.8500 |
793.77 |
| 303.15 |
0.8998 |
788.25 |
| 303.15 |
0.9499 |
782.59 |
| 303.15 |
1.0000 |
776.75 |
| 313.15 |
0.0000 |
863.76 |
| 313.15 |
0.0500 |
859.32 |
| 313.15 |
0.1000 |
854.97 |
| 313.15 |
0.1501 |
850.64 |
| 313.15 |
0.2000 |
846.27 |
| 313.15 |
0.2499 |
841.92 |
| 313.15 |
0.2997 |
837.55 |
| 313.15 |
0.3499 |
833.09 |
| 313.15 |
0.4000 |
828.58 |
| 313.15 |
0.4504 |
823.98 |
| 313.15 |
0.5001 |
819.37 |
| 313.15 |
0.5500 |
814.68 |
| 313.15 |
0.5999 |
809.9 |
| 313.15 |
0.6500 |
805.04 |
| 313.15 |
0.7001 |
800.07 |
| 313.15 |
0.7502 |
794.95 |
| 313.15 |
0.7999 |
789.8 |
| 313.15 |
0.8500 |
784.49 |
| 313.15 |
0.8998 |
779.1 |
| 313.15 |
0.9498 |
773.58 |
| 313.15 |
1.0000 |
767.93 |
| 323.15 |
0.0000 |
666.8 |
| 323.15 |
0.0501 |
667.65 |
| 323.15 |
0.1000 |
669.08 |
| 323.15 |
0.1500 |
670.98 |
| 323.15 |
0.1998 |
673.08 |
| 323.15 |
0.2500 |
675.42 |
| 323.15 |
0.3000 |
677.99 |
| 323.15 |
0.3500 |
680.86 |
| 323.15 |
0.4000 |
683.93 |
| 323.15 |
0.4499 |
687.34 |
| 323.15 |
0.5000 |
691.07 |
| 323.15 |
0.5501 |
695.17 |
| 323.15 |
0.6000 |
699.74 |
| 323.15 |
0.6500 |
704.78 |
| 323.15 |
0.7000 |
710.22 |
| 323.15 |
0.7499 |
716.22 |
| 323.15 |
0.7999 |
722.88 |
| 323.15 |
0.8500 |
730.48 |
| 323.15 |
0.9000 |
738.82 |
| 323.15 |
0.9500 |
748.16 |
| 323.15 |
1.0000 |
758.9 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 293.15 |
0.0000 |
0.0275 |
| 293.15 |
0.0501 |
0.0272 |
| 293.15 |
0.0999 |
0.0269 |
| 293.15 |
0.1499 |
0.0266 |
| 293.15 |
0.2003 |
0.0263 |
| 293.15 |
0.2506 |
0.0260 |
| 293.15 |
0.2999 |
0.0257 |
| 293.15 |
0.3500 |
0.0254 |
| 293.15 |
0.3999 |
0.0250 |
| 293.15 |
0.4499 |
0.0247 |
| 293.15 |
0.5001 |
0.0244 |
| 293.15 |
0.5502 |
0.0240 |
| 293.15 |
0.6001 |
0.0237 |
| 293.15 |
0.6499 |
0.0234 |
| 293.15 |
0.7001 |
0.0231 |
| 293.15 |
0.7499 |
0.0227 |
| 293.15 |
0.8000 |
0.0224 |
| 293.15 |
0.8501 |
0.0221 |
| 293.15 |
0.9001 |
0.0219 |
| 293.15 |
0.9499 |
0.0216 |
| 293.15 |
1.0000 |
0.0213 |
| 303.15 |
0.0000 |
0.0262 |
| 303.15 |
0.0502 |
0.0260 |
| 303.15 |
0.1001 |
0.0257 |
| 303.15 |
0.1501 |
0.0254 |
| 303.15 |
0.1998 |
0.0251 |
| 303.15 |
0.2499 |
0.0248 |
| 303.15 |
0.3000 |
0.0245 |
| 303.15 |
0.3499 |
0.0242 |
| 303.15 |
0.4001 |
0.0239 |
| 303.15 |
0.4501 |
0.0236 |
| 303.15 |
0.5001 |
0.0233 |
| 303.15 |
0.5500 |
0.0229 |
| 303.15 |
0.6000 |
0.0226 |
| 303.15 |
0.6500 |
0.0223 |
| 303.15 |
0.6999 |
0.0220 |
| 303.15 |
0.7499 |
0.0217 |
| 303.15 |
0.8001 |
0.0214 |
| 303.15 |
0.8500 |
0.0212 |
| 303.15 |
0.8998 |
0.0209 |
| 303.15 |
0.9499 |
0.0206 |
| 303.15 |
1.0000 |
0.0204 |
| 313.15 |
0.0000 |
0.0251 |
| 313.15 |
0.0500 |
0.0249 |
| 313.15 |
0.1000 |
0.0246 |
| 313.15 |
0.1501 |
0.0243 |
| 313.15 |
0.2000 |
0.0241 |
| 313.15 |
0.2499 |
0.0238 |
| 313.15 |
0.2997 |
0.0235 |
| 313.15 |
0.3499 |
0.0232 |
| 313.15 |
0.4000 |
0.0229 |
| 313.15 |
0.4504 |
0.0226 |
| 313.15 |
0.5001 |
0.0223 |
| 313.15 |
0.5500 |
0.0220 |
| 313.15 |
0.5999 |
0.0217 |
| 313.15 |
0.6500 |
0.0214 |
| 313.15 |
0.7001 |
0.0211 |
| 313.15 |
0.7502 |
0.0208 |
| 313.15 |
0.7999 |
0.0206 |
| 313.15 |
0.8500 |
0.0203 |
| 313.15 |
0.8998 |
0.0201 |
| 313.15 |
0.9498 |
0.0198 |
| 313.15 |
1.0000 |
0.0196 |
| 323.15 |
0.0000 |
0.0238 |
| 323.15 |
0.0500 |
0.0235 |
| 323.15 |
0.1000 |
0.0233 |
| 323.15 |
0.1501 |
0.0231 |
| 323.15 |
0.2000 |
0.0228 |
| 323.15 |
0.2499 |
0.0226 |
| 323.15 |
0.2997 |
0.0223 |
| 323.15 |
0.3499 |
0.0220 |
| 323.15 |
0.4000 |
0.0218 |
| 323.15 |
0.4504 |
0.0215 |
| 323.15 |
0.5001 |
0.0212 |
| 323.15 |
0.5501 |
0.0209 |
| 323.15 |
0.6000 |
0.0207 |
| 323.15 |
0.6500 |
0.0204 |
| 323.15 |
0.6999 |
0.0201 |
| 323.15 |
0.7502 |
0.0199 |
| 323.15 |
0.8002 |
0.0196 |
| 323.15 |
0.8501 |
0.0194 |
| 323.15 |
0.8998 |
0.0192 |
| 323.15 |
0.9501 |
0.0190 |
| 323.15 |
1.0000 |
0.0188 |
Surface tension liquid-gas, N/m
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Isopropyl Alcohol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 293.15 |
0.0000 |
0.0275 |
| 293.15 |
0.0501 |
0.0272 |
| 293.15 |
0.0999 |
0.0269 |
| 293.15 |
0.1499 |
0.0266 |
| 293.15 |
0.2003 |
0.0263 |
| 293.15 |
0.2506 |
0.0260 |
| 293.15 |
0.2999 |
0.0257 |
| 293.15 |
0.3500 |
0.0254 |
| 293.15 |
0.3999 |
0.0250 |
| 293.15 |
0.4499 |
0.0247 |
| 293.15 |
0.5001 |
0.0244 |
| 293.15 |
0.5502 |
0.0240 |
| 293.15 |
0.6001 |
0.0237 |
| 293.15 |
0.6499 |
0.0234 |
| 293.15 |
0.7001 |
0.0231 |
| 293.15 |
0.7499 |
0.0227 |
| 293.15 |
0.8000 |
0.0224 |
| 293.15 |
0.8501 |
0.0221 |
| 293.15 |
0.9001 |
0.0219 |
| 293.15 |
0.9499 |
0.0216 |
| 293.15 |
1.0000 |
0.0213 |
| 303.15 |
0.0000 |
0.0262 |
| 303.15 |
0.0502 |
0.0260 |
| 303.15 |
0.1001 |
0.0257 |
| 303.15 |
0.1501 |
0.0254 |
| 303.15 |
0.1998 |
0.0251 |
| 303.15 |
0.2499 |
0.0248 |
| 303.15 |
0.3000 |
0.0245 |
| 303.15 |
0.3499 |
0.0242 |
| 303.15 |
0.4001 |
0.0239 |
| 303.15 |
0.4501 |
0.0236 |
| 303.15 |
0.5001 |
0.0233 |
| 303.15 |
0.5500 |
0.0229 |
| 303.15 |
0.6000 |
0.0226 |
| 303.15 |
0.6500 |
0.0223 |
| 303.15 |
0.6999 |
0.0220 |
| 303.15 |
0.7499 |
0.0217 |
| 303.15 |
0.8001 |
0.0214 |
| 303.15 |
0.8500 |
0.0212 |
| 303.15 |
0.8998 |
0.0209 |
| 303.15 |
0.9499 |
0.0206 |
| 303.15 |
1.0000 |
0.0204 |
| 313.15 |
0.0000 |
0.0251 |
| 313.15 |
0.0500 |
0.0249 |
| 313.15 |
0.1000 |
0.0246 |
| 313.15 |
0.1501 |
0.0243 |
| 313.15 |
0.2000 |
0.0241 |
| 313.15 |
0.2499 |
0.0238 |
| 313.15 |
0.2997 |
0.0235 |
| 313.15 |
0.3499 |
0.0232 |
| 313.15 |
0.4000 |
0.0229 |
| 313.15 |
0.4504 |
0.0226 |
| 313.15 |
0.5001 |
0.0223 |
| 313.15 |
0.5500 |
0.0220 |
| 313.15 |
0.5999 |
0.0217 |
| 313.15 |
0.6500 |
0.0214 |
| 313.15 |
0.7001 |
0.0211 |
| 313.15 |
0.7502 |
0.0208 |
| 313.15 |
0.7999 |
0.0206 |
| 313.15 |
0.8500 |
0.0203 |
| 313.15 |
0.8998 |
0.0201 |
| 313.15 |
0.9498 |
0.0198 |
| 313.15 |
1.0000 |
0.0196 |
| 323.15 |
0.0000 |
0.0238 |
| 323.15 |
0.0500 |
0.0235 |
| 323.15 |
0.1000 |
0.0233 |
| 323.15 |
0.1501 |
0.0231 |
| 323.15 |
0.2000 |
0.0228 |
| 323.15 |
0.2499 |
0.0226 |
| 323.15 |
0.2997 |
0.0223 |
| 323.15 |
0.3499 |
0.0220 |
| 323.15 |
0.4000 |
0.0218 |
| 323.15 |
0.4504 |
0.0215 |
| 323.15 |
0.5001 |
0.0212 |
| 323.15 |
0.5501 |
0.0209 |
| 323.15 |
0.6000 |
0.0207 |
| 323.15 |
0.6500 |
0.0204 |
| 323.15 |
0.6999 |
0.0201 |
| 323.15 |
0.7502 |
0.0199 |
| 323.15 |
0.8002 |
0.0196 |
| 323.15 |
0.8501 |
0.0194 |
| 323.15 |
0.8998 |
0.0192 |
| 323.15 |
0.9501 |
0.0190 |
| 323.15 |
1.0000 |
0.0188 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Isopropyl Alcohol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
361.09 |
| 0.0820 |
358.71 |
| 0.1620 |
357.30 |
| 0.2350 |
356.49 |
| 0.3010 |
355.94 |
| 0.3730 |
355.50 |
| 0.4280 |
355.25 |
| 0.4870 |
355.04 |
| 0.5490 |
354.89 |
| 0.6130 |
354.80 |
| 0.6560 |
354.78 |
| 0.7090 |
354.79 |
| 0.7470 |
354.80 |
| 0.7920 |
354.86 |
| 0.8270 |
354.91 |
| 0.8610 |
354.98 |
| 0.8910 |
355.05 |
| 0.9160 |
355.11 |
| 0.9460 |
355.17 |
| 0.9770 |
355.30 |
| 1.0000 |
355.39 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of Tetrahydropyran (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
40.00 |
333.94 |
| 0.0000 |
53.33 |
340.18 |
| 0.0000 |
66.66 |
345.25 |
| 0.0000 |
79.99 |
349.55 |
| 0.0000 |
93.32 |
353.30 |
| 0.0000 |
98.66 |
354.67 |
| 0.1037 |
40.00 |
332.77 |
| 0.1037 |
53.33 |
339.26 |
| 0.1037 |
66.66 |
344.52 |
| 0.1037 |
79.99 |
348.97 |
| 0.1037 |
93.32 |
352.84 |
| 0.1037 |
98.66 |
354.27 |
| 0.1968 |
40.00 |
331.83 |
| 0.1968 |
53.33 |
338.51 |
| 0.1968 |
66.66 |
343.91 |
| 0.1968 |
79.99 |
348.48 |
| 0.1968 |
93.32 |
352.46 |
| 0.1968 |
98.66 |
353.92 |
| 0.2966 |
40.00 |
331.08 |
| 0.2966 |
53.33 |
337.93 |
| 0.2966 |
66.66 |
343.47 |
| 0.2966 |
79.99 |
348.15 |
| 0.2966 |
93.32 |
352.24 |
| 0.2966 |
98.66 |
353.74 |
| 0.4067 |
40.00 |
330.51 |
| 0.4067 |
53.33 |
337.52 |
| 0.4067 |
66.66 |
343.19 |
| 0.4067 |
79.99 |
348.00 |
| 0.4067 |
93.32 |
352.19 |
| 0.4067 |
98.66 |
353.73 |
| 0.5080 |
40.00 |
330.20 |
| 0.5080 |
53.33 |
337.35 |
| 0.5080 |
66.66 |
343.15 |
| 0.5080 |
79.99 |
348.07 |
| 0.5080 |
93.32 |
352.36 |
| 0.5080 |
98.66 |
353.94 |
| 0.6065 |
40.00 |
330.10 |
| 0.6065 |
53.33 |
337.40 |
| 0.6065 |
66.66 |
343.32 |
| 0.6065 |
79.99 |
348.34 |
| 0.6065 |
93.32 |
352.73 |
| 0.6065 |
98.66 |
354.34 |
| 0.7066 |
40.00 |
330.20 |
| 0.7066 |
53.33 |
337.66 |
| 0.7066 |
66.66 |
343.72 |
| 0.7066 |
79.99 |
348.88 |
| 0.7066 |
93.32 |
353.38 |
| 0.7066 |
98.66 |
355.05 |
| 0.8075 |
40.00 |
330.60 |
| 0.8075 |
53.33 |
338.24 |
| 0.8075 |
66.66 |
344.47 |
| 0.8075 |
79.99 |
349.78 |
| 0.8075 |
93.32 |
354.42 |
| 0.8075 |
98.66 |
356.13 |
| 0.9012 |
40.00 |
331.42 |
| 0.9012 |
53.33 |
339.27 |
| 0.9012 |
66.66 |
345.68 |
| 0.9012 |
79.99 |
351.16 |
| 0.9012 |
93.32 |
355.95 |
| 0.9012 |
98.66 |
357.72 |
| 1.0000 |
40.00 |
332.98 |
| 1.0000 |
53.33 |
341.09 |
| 1.0000 |
66.66 |
347.72 |
| 1.0000 |
79.99 |
353.38 |
| 1.0000 |
93.32 |
358.37 |
| 1.0000 |
98.66 |
360.22 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Isopropyl Alcohol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
361.09 |
| 0.0820 |
358.71 |
| 0.1620 |
357.30 |
| 0.2350 |
356.49 |
| 0.3010 |
355.94 |
| 0.3730 |
355.50 |
| 0.4280 |
355.25 |
| 0.4870 |
355.04 |
| 0.5490 |
354.89 |
| 0.6130 |
354.80 |
| 0.6560 |
354.78 |
| 0.7090 |
354.79 |
| 0.7470 |
354.80 |
| 0.7920 |
354.86 |
| 0.8270 |
354.91 |
| 0.8610 |
354.98 |
| 0.8910 |
355.05 |
| 0.9160 |
355.11 |
| 0.9460 |
355.17 |
| 0.9770 |
355.30 |
| 1.0000 |
355.39 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of Tetrahydropyran (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
40.00 |
333.94 |
| 0.0000 |
53.33 |
340.18 |
| 0.0000 |
66.66 |
345.25 |
| 0.0000 |
79.99 |
349.55 |
| 0.0000 |
93.32 |
353.30 |
| 0.0000 |
98.66 |
354.67 |
| 0.1037 |
40.00 |
332.77 |
| 0.1037 |
53.33 |
339.26 |
| 0.1037 |
66.66 |
344.52 |
| 0.1037 |
79.99 |
348.97 |
| 0.1037 |
93.32 |
352.84 |
| 0.1037 |
98.66 |
354.27 |
| 0.1968 |
40.00 |
331.83 |
| 0.1968 |
53.33 |
338.51 |
| 0.1968 |
66.66 |
343.91 |
| 0.1968 |
79.99 |
348.48 |
| 0.1968 |
93.32 |
352.46 |
| 0.1968 |
98.66 |
353.92 |
| 0.2966 |
40.00 |
331.08 |
| 0.2966 |
53.33 |
337.93 |
| 0.2966 |
66.66 |
343.47 |
| 0.2966 |
79.99 |
348.15 |
| 0.2966 |
93.32 |
352.24 |
| 0.2966 |
98.66 |
353.74 |
| 0.4067 |
40.00 |
330.51 |
| 0.4067 |
53.33 |
337.52 |
| 0.4067 |
66.66 |
343.19 |
| 0.4067 |
79.99 |
348.00 |
| 0.4067 |
93.32 |
352.19 |
| 0.4067 |
98.66 |
353.73 |
| 0.5080 |
40.00 |
330.20 |
| 0.5080 |
53.33 |
337.35 |
| 0.5080 |
66.66 |
343.15 |
| 0.5080 |
79.99 |
348.07 |
| 0.5080 |
93.32 |
352.36 |
| 0.5080 |
98.66 |
353.94 |
| 0.6065 |
40.00 |
330.10 |
| 0.6065 |
53.33 |
337.40 |
| 0.6065 |
66.66 |
343.32 |
| 0.6065 |
79.99 |
348.34 |
| 0.6065 |
93.32 |
352.73 |
| 0.6065 |
98.66 |
354.34 |
| 0.7066 |
40.00 |
330.20 |
| 0.7066 |
53.33 |
337.66 |
| 0.7066 |
66.66 |
343.72 |
| 0.7066 |
79.99 |
348.88 |
| 0.7066 |
93.32 |
353.38 |
| 0.7066 |
98.66 |
355.05 |
| 0.8075 |
40.00 |
330.60 |
| 0.8075 |
53.33 |
338.24 |
| 0.8075 |
66.66 |
344.47 |
| 0.8075 |
79.99 |
349.78 |
| 0.8075 |
93.32 |
354.42 |
| 0.8075 |
98.66 |
356.13 |
| 0.9012 |
40.00 |
331.42 |
| 0.9012 |
53.33 |
339.27 |
| 0.9012 |
66.66 |
345.68 |
| 0.9012 |
79.99 |
351.16 |
| 0.9012 |
93.32 |
355.95 |
| 0.9012 |
98.66 |
357.72 |
| 1.0000 |
40.00 |
332.98 |
| 1.0000 |
53.33 |
341.09 |
| 1.0000 |
66.66 |
347.72 |
| 1.0000 |
79.99 |
353.38 |
| 1.0000 |
93.32 |
358.37 |
| 1.0000 |
98.66 |
360.22 |
Azeotropic temperature, K
[ref]
| Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
| 101.30 |
354.78 |
Azeotropic temperature, K
[ref]
| Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
| 101.30 |
354.78 |
Sources
-
Densities, viscosities, refractive indices, and surface tensions for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane
-
(Vapour + liquid) equilibria for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane at P = 101.3 kPa
-
Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems