Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.1835 | 0.0045 |
| 283.15 | 0.2675 | 0.0035 |
| 283.15 | 0.3850 | 0.0028 |
| 283.15 | 0.4933 | 0.0023 |
| 283.15 | 0.5935 | 0.0020 |
| 283.15 | 0.6866 | 0.0018 |
| 283.15 | 0.7731 | 0.0017 |
| 283.15 | 0.8795 | 0.0016 |
| 293.15 | 0.1835 | 0.0032 |
| 293.15 | 0.2675 | 0.0027 |
| 293.15 | 0.3850 | 0.0022 |
| 293.15 | 0.4933 | 0.0018 |
| 293.15 | 0.5935 | 0.0016 |
| 293.15 | 0.6866 | 0.0016 |
| 293.15 | 0.7731 | 0.0014 |
| 293.15 | 0.8795 | 0.0013 |
| 303.15 | 0.1835 | 0.0026 |
| 303.15 | 0.2675 | 0.0021 |
| 303.15 | 0.3850 | 0.0017 |
| 303.15 | 0.4933 | 0.0015 |
| 303.15 | 0.5935 | 0.0013 |
| 303.15 | 0.6866 | 0.0012 |
| 303.15 | 0.7731 | 0.0012 |
| 303.15 | 0.8795 | 0.0010 |
| 313.15 | 0.1835 | 0.0023 |
| 313.15 | 0.2675 | 0.0017 |
| 313.15 | 0.3850 | 0.0014 |
| 313.15 | 0.4933 | 0.0013 |
| 313.15 | 0.5935 | 0.0011 |
| 313.15 | 0.6866 | 0.0011 |
| 313.15 | 0.7731 | 0.0010 |
| 313.15 | 0.8795 | 0.0010 |
| 323.15 | 0.1835 | 0.0017 |
| 323.15 | 0.2675 | 0.0014 |
| 323.15 | 0.3850 | 0.0012 |
| 323.15 | 0.4933 | 0.0011 |
| 323.15 | 0.5935 | 0.0010 |
| 323.15 | 0.6866 | 0.0009 |
| 323.15 | 0.7731 | 0.0009 |
| 323.15 | 0.8795 | 0.0008 |
| 333.15 | 0.1835 | 0.0013 |
| 333.15 | 0.2675 | 0.0012 |
| 333.15 | 0.3850 | 0.0010 |
| 333.15 | 0.4933 | 0.0009 |
| 333.15 | 0.5935 | 0.0008 |
| 333.15 | 0.6866 | 0.0008 |
| 333.15 | 0.7731 | 0.0008 |
| 333.15 | 0.8795 | 0.0007 |
| 343.15 | 0.1835 | 0.0011 |
| 343.15 | 0.2675 | 0.0010 |
| 343.15 | 0.3850 | 0.0009 |
| 343.15 | 0.4933 | 0.0008 |
| 343.15 | 0.5935 | 0.0007 |
| 343.15 | 0.6866 | 0.0007 |
| 343.15 | 0.7731 | 0.0007 |
| 343.15 | 0.8795 | 0.0007 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
| 283.15 | 0.1835 | 0.0045 |
| 283.15 | 0.2675 | 0.0035 |
| 283.15 | 0.3850 | 0.0028 |
| 283.15 | 0.4933 | 0.0023 |
| 283.15 | 0.5935 | 0.0020 |
| 283.15 | 0.6866 | 0.0018 |
| 283.15 | 0.7731 | 0.0017 |
| 283.15 | 0.8795 | 0.0016 |
| 293.15 | 0.1835 | 0.0032 |
| 293.15 | 0.2675 | 0.0027 |
| 293.15 | 0.3850 | 0.0022 |
| 293.15 | 0.4933 | 0.0018 |
| 293.15 | 0.5935 | 0.0016 |
| 293.15 | 0.6866 | 0.0016 |
| 293.15 | 0.7731 | 0.0014 |
| 293.15 | 0.8795 | 0.0013 |
| 303.15 | 0.1835 | 0.0026 |
| 303.15 | 0.2675 | 0.0021 |
| 303.15 | 0.3850 | 0.0017 |
| 303.15 | 0.4933 | 0.0015 |
| 303.15 | 0.5935 | 0.0013 |
| 303.15 | 0.6866 | 0.0012 |
| 303.15 | 0.7731 | 0.0012 |
| 303.15 | 0.8795 | 0.0010 |
| 313.15 | 0.1835 | 0.0023 |
| 313.15 | 0.2675 | 0.0017 |
| 313.15 | 0.3850 | 0.0014 |
| 313.15 | 0.4933 | 0.0013 |
| 313.15 | 0.5935 | 0.0011 |
| 313.15 | 0.6866 | 0.0011 |
| 313.15 | 0.7731 | 0.0010 |
| 313.15 | 0.8795 | 0.0010 |
| 323.15 | 0.1835 | 0.0017 |
| 323.15 | 0.2675 | 0.0014 |
| 323.15 | 0.3850 | 0.0012 |
| 323.15 | 0.4933 | 0.0011 |
| 323.15 | 0.5935 | 0.0010 |
| 323.15 | 0.6866 | 0.0009 |
| 323.15 | 0.7731 | 0.0009 |
| 323.15 | 0.8795 | 0.0008 |
| 333.15 | 0.1835 | 0.0013 |
| 333.15 | 0.2675 | 0.0012 |
| 333.15 | 0.3850 | 0.0010 |
| 333.15 | 0.4933 | 0.0009 |
| 333.15 | 0.5935 | 0.0008 |
| 333.15 | 0.6866 | 0.0008 |
| 333.15 | 0.7731 | 0.0008 |
| 333.15 | 0.8795 | 0.0007 |
| 343.15 | 0.1835 | 0.0011 |
| 343.15 | 0.2675 | 0.0010 |
| 343.15 | 0.3850 | 0.0009 |
| 343.15 | 0.4933 | 0.0008 |
| 343.15 | 0.5935 | 0.0007 |
| 343.15 | 0.6866 | 0.0007 |
| 343.15 | 0.7731 | 0.0007 |
| 343.15 | 0.8795 | 0.0007 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.1835 | 860.24 |
| 283.15 | 0.2675 | 873.31 |
| 283.15 | 0.3850 | 896.72 |
| 283.15 | 0.4933 | 916.23 |
| 283.15 | 0.5935 | 938.47 |
| 283.15 | 0.6866 | 957.86 |
| 283.15 | 0.7731 | 981.11 |
| 283.15 | 0.8795 | 1013.54 |
| 293.15 | 0.1835 | 853.33 |
| 293.15 | 0.2675 | 865.64 |
| 293.15 | 0.3850 | 889.2 |
| 293.15 | 0.4933 | 903.63 |
| 293.15 | 0.5935 | 929.82 |
| 293.15 | 0.6866 | 951.11 |
| 293.15 | 0.7731 | 973.8 |
| 293.15 | 0.8795 | 1002.74 |
| 303.15 | 0.1835 | 845.02 |
| 303.15 | 0.2675 | 857.53 |
| 303.15 | 0.3850 | 879.87 |
| 303.15 | 0.4933 | 898.36 |
| 303.15 | 0.5935 | 920.31 |
| 303.15 | 0.6866 | 941.43 |
| 303.15 | 0.7731 | 963.84 |
| 303.15 | 0.8795 | 990.21 |
| 313.15 | 0.1835 | 836.88 |
| 313.15 | 0.2675 | 849.44 |
| 313.15 | 0.3850 | 871.16 |
| 313.15 | 0.4933 | 889.72 |
| 313.15 | 0.5935 | 909.94 |
| 313.15 | 0.6866 | 931.85 |
| 313.15 | 0.7731 | 953.63 |
| 313.15 | 0.8795 | 980.82 |
| 323.15 | 0.1835 | 829.74 |
| 323.15 | 0.2675 | 841.13 |
| 323.15 | 0.3850 | 864.56 |
| 323.15 | 0.4933 | 880.42 |
| 323.15 | 0.5935 | 900.9 |
| 323.15 | 0.6866 | 921.84 |
| 323.15 | 0.7731 | 943.38 |
| 323.15 | 0.8795 | 971.57 |
| 333.15 | 0.1835 | 821.17 |
| 333.15 | 0.2675 | 833.54 |
| 333.15 | 0.3850 | 856.26 |
| 333.15 | 0.4933 | 869.91 |
| 333.15 | 0.5935 | 890.93 |
| 333.15 | 0.6866 | 911.92 |
| 333.15 | 0.7731 | 933.31 |
| 333.15 | 0.8795 | 958.09 |
| 343.15 | 0.1835 | 815.14 |
| 343.15 | 0.2675 | 824.52 |
| 343.15 | 0.3850 | 843.77 |
| 343.15 | 0.4933 | 862.93 |
| 343.15 | 0.5935 | 881.04 |
| 343.15 | 0.6866 | 905.05 |
| 343.15 | 0.7731 | 923.91 |
| 343.15 | 0.8795 | 947.05 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 0.1835 | 860.24 |
| 283.15 | 0.2675 | 873.31 |
| 283.15 | 0.3850 | 896.72 |
| 283.15 | 0.4933 | 916.23 |
| 283.15 | 0.5935 | 938.47 |
| 283.15 | 0.6866 | 957.86 |
| 283.15 | 0.7731 | 981.11 |
| 283.15 | 0.8795 | 1013.54 |
| 293.15 | 0.1835 | 853.33 |
| 293.15 | 0.2675 | 865.64 |
| 293.15 | 0.3850 | 889.2 |
| 293.15 | 0.4933 | 903.63 |
| 293.15 | 0.5935 | 929.82 |
| 293.15 | 0.6866 | 951.11 |
| 293.15 | 0.7731 | 973.8 |
| 293.15 | 0.8795 | 1002.74 |
| 303.15 | 0.1835 | 845.02 |
| 303.15 | 0.2675 | 857.53 |
| 303.15 | 0.3850 | 879.87 |
| 303.15 | 0.4933 | 898.36 |
| 303.15 | 0.5935 | 920.31 |
| 303.15 | 0.6866 | 941.43 |
| 303.15 | 0.7731 | 963.84 |
| 303.15 | 0.8795 | 990.21 |
| 313.15 | 0.1835 | 836.88 |
| 313.15 | 0.2675 | 849.44 |
| 313.15 | 0.3850 | 871.16 |
| 313.15 | 0.4933 | 889.72 |
| 313.15 | 0.5935 | 909.94 |
| 313.15 | 0.6866 | 931.85 |
| 313.15 | 0.7731 | 953.63 |
| 313.15 | 0.8795 | 980.82 |
| 323.15 | 0.1835 | 829.74 |
| 323.15 | 0.2675 | 841.13 |
| 323.15 | 0.3850 | 864.56 |
| 323.15 | 0.4933 | 880.42 |
| 323.15 | 0.5935 | 900.9 |
| 323.15 | 0.6866 | 921.84 |
| 323.15 | 0.7731 | 943.38 |
| 323.15 | 0.8795 | 971.57 |
| 333.15 | 0.1835 | 821.17 |
| 333.15 | 0.2675 | 833.54 |
| 333.15 | 0.3850 | 856.26 |
| 333.15 | 0.4933 | 869.91 |
| 333.15 | 0.5935 | 890.93 |
| 333.15 | 0.6866 | 911.92 |
| 333.15 | 0.7731 | 933.31 |
| 333.15 | 0.8795 | 958.09 |
| 343.15 | 0.1835 | 815.14 |
| 343.15 | 0.2675 | 824.52 |
| 343.15 | 0.3850 | 843.77 |
| 343.15 | 0.4933 | 862.93 |
| 343.15 | 0.5935 | 881.04 |
| 343.15 | 0.6866 | 905.05 |
| 343.15 | 0.7731 | 923.91 |
| 343.15 | 0.8795 | 947.05 |