Operational condition: Pressure, kPa = 101.32 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0005 |
| 288.15 | 0.0500 | 0.0005 |
| 288.15 | 0.1000 | 0.0005 |
| 288.15 | 0.2000 | 0.0005 |
| 288.15 | 0.3000 | 0.0006 |
| 288.15 | 0.4000 | 0.0007 |
| 288.15 | 0.5000 | 0.0008 |
| 288.15 | 0.6000 | 0.0010 |
| 288.15 | 0.7000 | 0.0012 |
| 288.15 | 0.8000 | 0.0015 |
| 288.15 | 0.9000 | 0.0019 |
| 288.15 | 0.9500 | 0.0022 |
| 288.15 | 1.0000 | 0.0025 |
| 298.15 | 0.0000 | 0.0004 |
| 298.15 | 0.0500 | 0.0004 |
| 298.15 | 0.1000 | 0.0004 |
| 298.15 | 0.2000 | 0.0005 |
| 298.15 | 0.3000 | 0.0005 |
| 298.15 | 0.4000 | 0.0006 |
| 298.15 | 0.5000 | 0.0007 |
| 298.15 | 0.6000 | 0.0008 |
| 298.15 | 0.7000 | 0.0010 |
| 298.15 | 0.8000 | 0.0012 |
| 298.15 | 0.9000 | 0.0015 |
| 298.15 | 0.9500 | 0.0017 |
| 298.15 | 1.0000 | 0.0020 |
| 308.15 | 0.0000 | 0.0004 |
| 308.15 | 0.0500 | 0.0004 |
| 308.15 | 0.1000 | 0.0004 |
| 308.15 | 0.2000 | 0.0004 |
| 308.15 | 0.3000 | 0.0004 |
| 308.15 | 0.4000 | 0.0005 |
| 308.15 | 0.5000 | 0.0006 |
| 308.15 | 0.6000 | 0.0007 |
| 308.15 | 0.7000 | 0.0008 |
| 308.15 | 0.8000 | 0.0010 |
| 308.15 | 0.9000 | 0.0012 |
| 308.15 | 0.9500 | 0.0014 |
| 308.15 | 1.0000 | 0.0015 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0005 |
| 288.15 | 0.0500 | 0.0005 |
| 288.15 | 0.1000 | 0.0005 |
| 288.15 | 0.2000 | 0.0005 |
| 288.15 | 0.3000 | 0.0006 |
| 288.15 | 0.4000 | 0.0007 |
| 288.15 | 0.5000 | 0.0008 |
| 288.15 | 0.6000 | 0.0010 |
| 288.15 | 0.7000 | 0.0012 |
| 288.15 | 0.8000 | 0.0015 |
| 288.15 | 0.9000 | 0.0019 |
| 288.15 | 0.9500 | 0.0022 |
| 288.15 | 1.0000 | 0.0025 |
| 298.15 | 0.0000 | 0.0004 |
| 298.15 | 0.0500 | 0.0004 |
| 298.15 | 0.1000 | 0.0004 |
| 298.15 | 0.2000 | 0.0005 |
| 298.15 | 0.3000 | 0.0005 |
| 298.15 | 0.4000 | 0.0006 |
| 298.15 | 0.5000 | 0.0007 |
| 298.15 | 0.6000 | 0.0008 |
| 298.15 | 0.7000 | 0.0010 |
| 298.15 | 0.8000 | 0.0012 |
| 298.15 | 0.9000 | 0.0015 |
| 298.15 | 0.9500 | 0.0017 |
| 298.15 | 1.0000 | 0.0020 |
| 308.15 | 0.0000 | 0.0004 |
| 308.15 | 0.0500 | 0.0004 |
| 308.15 | 0.1000 | 0.0004 |
| 308.15 | 0.2000 | 0.0004 |
| 308.15 | 0.3000 | 0.0004 |
| 308.15 | 0.4000 | 0.0005 |
| 308.15 | 0.5000 | 0.0006 |
| 308.15 | 0.6000 | 0.0007 |
| 308.15 | 0.7000 | 0.0008 |
| 308.15 | 0.8000 | 0.0010 |
| 308.15 | 0.9000 | 0.0012 |
| 308.15 | 0.9500 | 0.0014 |
| 308.15 | 1.0000 | 0.0015 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4045 |
| 288.15 | 0.0500 | 1.4036 |
| 288.15 | 0.1000 | 1.4028 |
| 288.15 | 0.2000 | 1.4013 |
| 288.15 | 0.3000 | 1.3998 |
| 288.15 | 0.4000 | 1.3984 |
| 288.15 | 0.5000 | 1.3968 |
| 288.15 | 0.6000 | 1.3952 |
| 288.15 | 0.7000 | 1.3934 |
| 288.15 | 0.8000 | 1.3914 |
| 288.15 | 0.9000 | 1.3892 |
| 288.15 | 0.9500 | 1.3881 |
| 288.15 | 1.0000 | 1.3869 |
| 298.15 | 0.0000 | 1.3993 |
| 298.15 | 0.0500 | 1.3984 |
| 298.15 | 0.1000 | 1.3976 |
| 298.15 | 0.2000 | 1.3962 |
| 298.15 | 0.3000 | 1.3948 |
| 298.15 | 0.4000 | 1.3934 |
| 298.15 | 0.5000 | 1.3919 |
| 298.15 | 0.6000 | 1.3904 |
| 298.15 | 0.7000 | 1.3888 |
| 298.15 | 0.8000 | 1.387 |
| 298.15 | 0.9000 | 1.385 |
| 298.15 | 0.9500 | 1.384 |
| 298.15 | 1.0000 | 1.3829 |
| 308.15 | 0.0000 | 1.3941 |
| 308.15 | 0.0500 | 1.3931 |
| 308.15 | 0.1000 | 1.3923 |
| 308.15 | 0.2000 | 1.3909 |
| 308.15 | 0.3000 | 1.3895 |
| 308.15 | 0.4000 | 1.3882 |
| 308.15 | 0.5000 | 1.3869 |
| 308.15 | 0.6000 | 1.3855 |
| 308.15 | 0.7000 | 1.384 |
| 308.15 | 0.8000 | 1.3824 |
| 308.15 | 0.9000 | 1.3807 |
| 308.15 | 0.9500 | 1.3798 |
| 308.15 | 1.0000 | 1.3789 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4045 |
| 288.15 | 0.0500 | 1.4036 |
| 288.15 | 0.1000 | 1.4028 |
| 288.15 | 0.2000 | 1.4013 |
| 288.15 | 0.3000 | 1.3998 |
| 288.15 | 0.4000 | 1.3984 |
| 288.15 | 0.5000 | 1.3968 |
| 288.15 | 0.6000 | 1.3952 |
| 288.15 | 0.7000 | 1.3934 |
| 288.15 | 0.8000 | 1.3914 |
| 288.15 | 0.9000 | 1.3892 |
| 288.15 | 0.9500 | 1.3881 |
| 288.15 | 1.0000 | 1.3869 |
| 298.15 | 0.0000 | 1.3993 |
| 298.15 | 0.0500 | 1.3984 |
| 298.15 | 0.1000 | 1.3976 |
| 298.15 | 0.2000 | 1.3962 |
| 298.15 | 0.3000 | 1.3948 |
| 298.15 | 0.4000 | 1.3934 |
| 298.15 | 0.5000 | 1.3919 |
| 298.15 | 0.6000 | 1.3904 |
| 298.15 | 0.7000 | 1.3888 |
| 298.15 | 0.8000 | 1.387 |
| 298.15 | 0.9000 | 1.385 |
| 298.15 | 0.9500 | 1.384 |
| 298.15 | 1.0000 | 1.3829 |
| 308.15 | 0.0000 | 1.3941 |
| 308.15 | 0.0500 | 1.3931 |
| 308.15 | 0.1000 | 1.3923 |
| 308.15 | 0.2000 | 1.3909 |
| 308.15 | 0.3000 | 1.3895 |
| 308.15 | 0.4000 | 1.3882 |
| 308.15 | 0.5000 | 1.3869 |
| 308.15 | 0.6000 | 1.3855 |
| 308.15 | 0.7000 | 1.384 |
| 308.15 | 0.8000 | 1.3824 |
| 308.15 | 0.9000 | 1.3807 |
| 308.15 | 0.9500 | 1.3798 |
| 308.15 | 1.0000 | 1.3789 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 892.2 |
| 288.15 | 0.0500 | 888.3 |
| 288.15 | 0.1000 | 884.9 |
| 288.15 | 0.2000 | 878.2 |
| 288.15 | 0.3000 | 871.2 |
| 288.15 | 0.4000 | 864.0 |
| 288.15 | 0.5000 | 856.3 |
| 288.15 | 0.6000 | 848.1 |
| 288.15 | 0.7000 | 839.2 |
| 288.15 | 0.8000 | 829.6 |
| 288.15 | 0.9000 | 819.2 |
| 288.15 | 0.9500 | 813.5 |
| 288.15 | 1.0000 | 807.6 |
| 298.15 | 0.0000 | 881.0 |
| 298.15 | 0.0500 | 877.2 |
| 298.15 | 0.1000 | 873.8 |
| 298.15 | 0.2000 | 867.3 |
| 298.15 | 0.3000 | 860.5 |
| 298.15 | 0.4000 | 853.5 |
| 298.15 | 0.5000 | 846.1 |
| 298.15 | 0.6000 | 838.3 |
| 298.15 | 0.7000 | 829.8 |
| 298.15 | 0.8000 | 820.7 |
| 298.15 | 0.9000 | 810.7 |
| 298.15 | 0.9500 | 805.3 |
| 298.15 | 1.0000 | 799.6 |
| 308.15 | 0.0000 | 869.7 |
| 308.15 | 0.0500 | 866.0 |
| 308.15 | 0.1000 | 862.6 |
| 308.15 | 0.2000 | 856.2 |
| 308.15 | 0.3000 | 849.7 |
| 308.15 | 0.4000 | 842.9 |
| 308.15 | 0.5000 | 835.8 |
| 308.15 | 0.6000 | 828.3 |
| 308.15 | 0.7000 | 820.3 |
| 308.15 | 0.8000 | 811.5 |
| 308.15 | 0.9000 | 802.0 |
| 308.15 | 0.9500 | 796.9 |
| 308.15 | 1.0000 | 791.5 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Propanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 892.2 |
| 288.15 | 0.0500 | 888.3 |
| 288.15 | 0.1000 | 884.9 |
| 288.15 | 0.2000 | 878.2 |
| 288.15 | 0.3000 | 871.2 |
| 288.15 | 0.4000 | 864.0 |
| 288.15 | 0.5000 | 856.3 |
| 288.15 | 0.6000 | 848.1 |
| 288.15 | 0.7000 | 839.2 |
| 288.15 | 0.8000 | 829.6 |
| 288.15 | 0.9000 | 819.2 |
| 288.15 | 0.9500 | 813.5 |
| 288.15 | 1.0000 | 807.6 |
| 298.15 | 0.0000 | 881.0 |
| 298.15 | 0.0500 | 877.2 |
| 298.15 | 0.1000 | 873.8 |
| 298.15 | 0.2000 | 867.3 |
| 298.15 | 0.3000 | 860.5 |
| 298.15 | 0.4000 | 853.5 |
| 298.15 | 0.5000 | 846.1 |
| 298.15 | 0.6000 | 838.3 |
| 298.15 | 0.7000 | 829.8 |
| 298.15 | 0.8000 | 820.7 |
| 298.15 | 0.9000 | 810.7 |
| 298.15 | 0.9500 | 805.3 |
| 298.15 | 1.0000 | 799.6 |
| 308.15 | 0.0000 | 869.7 |
| 308.15 | 0.0500 | 866.0 |
| 308.15 | 0.1000 | 862.6 |
| 308.15 | 0.2000 | 856.2 |
| 308.15 | 0.3000 | 849.7 |
| 308.15 | 0.4000 | 842.9 |
| 308.15 | 0.5000 | 835.8 |
| 308.15 | 0.6000 | 828.3 |
| 308.15 | 0.7000 | 820.3 |
| 308.15 | 0.8000 | 811.5 |
| 308.15 | 0.9000 | 802.0 |
| 308.15 | 0.9500 | 796.9 |
| 308.15 | 1.0000 | 791.5 |
Operational conditions:
| Mole fraction of Butane, 1-chloro- (2) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0130 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9700 | 0.0000 |
Operational conditions:
| Mole fraction of Butane, 1-chloro- (2) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0130 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9700 | 0.0000 |
Operational conditions:
| Mole fraction of Butane, 1-chloro- (2) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0130 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9700 | 0.0000 |
Operational conditions:
| Mole fraction of Butane, 1-chloro- (2) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0130 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9700 | 0.0000 |