Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
288.15 | 0.1085 | 0.0006 |
288.15 | 0.2061 | 0.0006 |
288.15 | 0.2943 | 0.0006 |
288.15 | 0.3746 | 0.0006 |
288.15 | 0.5150 | 0.0007 |
288.15 | 0.6337 | 0.0008 |
288.15 | 0.6865 | 0.0009 |
288.15 | 0.8237 | 0.0010 |
288.15 | 0.9008 | 0.0012 |
293.15 | 0.1085 | 0.0005 |
293.15 | 0.2061 | 0.0005 |
293.15 | 0.2943 | 0.0006 |
293.15 | 0.3746 | 0.0006 |
293.15 | 0.5150 | 0.0007 |
293.15 | 0.6337 | 0.0007 |
293.15 | 0.6865 | 0.0008 |
293.15 | 0.8237 | 0.0010 |
293.15 | 0.9008 | 0.0011 |
298.15 | 0.1085 | 0.0005 |
298.15 | 0.2061 | 0.0005 |
298.15 | 0.2943 | 0.0005 |
298.15 | 0.3746 | 0.0006 |
298.15 | 0.5150 | 0.0006 |
298.15 | 0.6337 | 0.0007 |
298.15 | 0.6865 | 0.0007 |
298.15 | 0.8237 | 0.0009 |
298.15 | 0.9008 | 0.0010 |
303.15 | 0.1085 | 0.0005 |
303.15 | 0.2061 | 0.0005 |
303.15 | 0.2943 | 0.0005 |
303.15 | 0.3746 | 0.0005 |
303.15 | 0.5150 | 0.0006 |
303.15 | 0.6337 | 0.0007 |
303.15 | 0.6865 | 0.0007 |
303.15 | 0.8237 | 0.0008 |
303.15 | 0.9008 | 0.0009 |
308.15 | 0.1085 | 0.0004 |
308.15 | 0.2061 | 0.0005 |
308.15 | 0.2943 | 0.0005 |
308.15 | 0.3746 | 0.0005 |
308.15 | 0.5150 | 0.0005 |
308.15 | 0.6337 | 0.0006 |
308.15 | 0.6865 | 0.0006 |
308.15 | 0.8237 | 0.0008 |
308.15 | 0.9008 | 0.0009 |
313.15 | 0.1085 | 0.0004 |
313.15 | 0.2061 | 0.0004 |
313.15 | 0.2943 | 0.0005 |
313.15 | 0.3746 | 0.0005 |
313.15 | 0.5150 | 0.0005 |
313.15 | 0.6337 | 0.0006 |
313.15 | 0.6865 | 0.0006 |
313.15 | 0.8237 | 0.0007 |
313.15 | 0.9008 | 0.0008 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
288.15 | 0.1085 | 0.0006 |
288.15 | 0.2061 | 0.0006 |
288.15 | 0.2943 | 0.0006 |
288.15 | 0.3746 | 0.0006 |
288.15 | 0.5150 | 0.0007 |
288.15 | 0.6337 | 0.0008 |
288.15 | 0.6865 | 0.0009 |
288.15 | 0.8237 | 0.0010 |
288.15 | 0.9008 | 0.0012 |
293.15 | 0.1085 | 0.0005 |
293.15 | 0.2061 | 0.0005 |
293.15 | 0.2943 | 0.0006 |
293.15 | 0.3746 | 0.0006 |
293.15 | 0.5150 | 0.0007 |
293.15 | 0.6337 | 0.0007 |
293.15 | 0.6865 | 0.0008 |
293.15 | 0.8237 | 0.0010 |
293.15 | 0.9008 | 0.0011 |
298.15 | 0.1085 | 0.0005 |
298.15 | 0.2061 | 0.0005 |
298.15 | 0.2943 | 0.0005 |
298.15 | 0.3746 | 0.0006 |
298.15 | 0.5150 | 0.0006 |
298.15 | 0.6337 | 0.0007 |
298.15 | 0.6865 | 0.0007 |
298.15 | 0.8237 | 0.0009 |
298.15 | 0.9008 | 0.0010 |
303.15 | 0.1085 | 0.0005 |
303.15 | 0.2061 | 0.0005 |
303.15 | 0.2943 | 0.0005 |
303.15 | 0.3746 | 0.0005 |
303.15 | 0.5150 | 0.0006 |
303.15 | 0.6337 | 0.0007 |
303.15 | 0.6865 | 0.0007 |
303.15 | 0.8237 | 0.0008 |
303.15 | 0.9008 | 0.0009 |
308.15 | 0.1085 | 0.0004 |
308.15 | 0.2061 | 0.0005 |
308.15 | 0.2943 | 0.0005 |
308.15 | 0.3746 | 0.0005 |
308.15 | 0.5150 | 0.0005 |
308.15 | 0.6337 | 0.0006 |
308.15 | 0.6865 | 0.0006 |
308.15 | 0.8237 | 0.0008 |
308.15 | 0.9008 | 0.0009 |
313.15 | 0.1085 | 0.0004 |
313.15 | 0.2061 | 0.0004 |
313.15 | 0.2943 | 0.0005 |
313.15 | 0.3746 | 0.0005 |
313.15 | 0.5150 | 0.0005 |
313.15 | 0.6337 | 0.0006 |
313.15 | 0.6865 | 0.0006 |
313.15 | 0.8237 | 0.0007 |
313.15 | 0.9008 | 0.0008 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.1085 | 716.6 |
288.15 | 0.2061 | 734.0 |
288.15 | 0.2943 | 752.2 |
288.15 | 0.3746 | 774.7 |
288.15 | 0.5150 | 813.8 |
288.15 | 0.6337 | 855.2 |
288.15 | 0.6865 | 878.7 |
288.15 | 0.8237 | 940.5 |
288.15 | 0.9008 | 981.1 |
293.15 | 0.1085 | 712.3 |
293.15 | 0.2061 | 729.6 |
293.15 | 0.2943 | 747.4 |
293.15 | 0.3746 | 770.2 |
293.15 | 0.5150 | 809.0 |
293.15 | 0.6337 | 851.5 |
293.15 | 0.6865 | 874.1 |
293.15 | 0.8237 | 935.1 |
293.15 | 0.9008 | 975.6 |
298.15 | 0.1085 | 707.9 |
298.15 | 0.2061 | 725.1 |
298.15 | 0.2943 | 742.8 |
298.15 | 0.3746 | 766.0 |
298.15 | 0.5150 | 804.4 |
298.15 | 0.6337 | 848.8 |
298.15 | 0.6865 | 869.5 |
298.15 | 0.8237 | 929.7 |
298.15 | 0.9008 | 970.1 |
303.15 | 0.1085 | 703.8 |
303.15 | 0.2061 | 719.7 |
303.15 | 0.2943 | 738.5 |
303.15 | 0.3746 | 761.2 |
303.15 | 0.5150 | 800.0 |
303.15 | 0.6337 | 844.7 |
303.15 | 0.6865 | 864.8 |
303.15 | 0.8237 | 924.4 |
303.15 | 0.9008 | 964.7 |
308.15 | 0.1085 | 699.1 |
308.15 | 0.2061 | 715.1 |
308.15 | 0.2943 | 733.5 |
308.15 | 0.3746 | 756.4 |
308.15 | 0.5150 | 795.2 |
308.15 | 0.6337 | 841.3 |
308.15 | 0.6865 | 861.6 |
308.15 | 0.8237 | 919.4 |
308.15 | 0.9008 | 959.2 |
313.15 | 0.1085 | 694.2 |
313.15 | 0.2061 | 711.6 |
313.15 | 0.2943 | 728.5 |
313.15 | 0.3746 | 751.4 |
313.15 | 0.5150 | 790.7 |
313.15 | 0.6337 | 837.9 |
313.15 | 0.6865 | 855.0 |
313.15 | 0.8237 | 913.4 |
313.15 | 0.9008 | 953.1 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.1085 | 716.6 |
288.15 | 0.2061 | 734.0 |
288.15 | 0.2943 | 752.2 |
288.15 | 0.3746 | 774.7 |
288.15 | 0.5150 | 813.8 |
288.15 | 0.6337 | 855.2 |
288.15 | 0.6865 | 878.7 |
288.15 | 0.8237 | 940.5 |
288.15 | 0.9008 | 981.1 |
293.15 | 0.1085 | 712.3 |
293.15 | 0.2061 | 729.6 |
293.15 | 0.2943 | 747.4 |
293.15 | 0.3746 | 770.2 |
293.15 | 0.5150 | 809.0 |
293.15 | 0.6337 | 851.5 |
293.15 | 0.6865 | 874.1 |
293.15 | 0.8237 | 935.1 |
293.15 | 0.9008 | 975.6 |
298.15 | 0.1085 | 707.9 |
298.15 | 0.2061 | 725.1 |
298.15 | 0.2943 | 742.8 |
298.15 | 0.3746 | 766.0 |
298.15 | 0.5150 | 804.4 |
298.15 | 0.6337 | 848.8 |
298.15 | 0.6865 | 869.5 |
298.15 | 0.8237 | 929.7 |
298.15 | 0.9008 | 970.1 |
303.15 | 0.1085 | 703.8 |
303.15 | 0.2061 | 719.7 |
303.15 | 0.2943 | 738.5 |
303.15 | 0.3746 | 761.2 |
303.15 | 0.5150 | 800.0 |
303.15 | 0.6337 | 844.7 |
303.15 | 0.6865 | 864.8 |
303.15 | 0.8237 | 924.4 |
303.15 | 0.9008 | 964.7 |
308.15 | 0.1085 | 699.1 |
308.15 | 0.2061 | 715.1 |
308.15 | 0.2943 | 733.5 |
308.15 | 0.3746 | 756.4 |
308.15 | 0.5150 | 795.2 |
308.15 | 0.6337 | 841.3 |
308.15 | 0.6865 | 861.6 |
308.15 | 0.8237 | 919.4 |
308.15 | 0.9008 | 959.2 |
313.15 | 0.1085 | 694.2 |
313.15 | 0.2061 | 711.6 |
313.15 | 0.2943 | 728.5 |
313.15 | 0.3746 | 751.4 |
313.15 | 0.5150 | 790.7 |
313.15 | 0.6337 | 837.9 |
313.15 | 0.6865 | 855.0 |
313.15 | 0.8237 | 913.4 |
313.15 | 0.9008 | 953.1 |