Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of p-Xylene (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0562 | 941.87 |
293.15 | 0.1211 | 934.47 |
293.15 | 0.1885 | 927.18 |
293.15 | 0.2532 | 920.51 |
293.15 | 0.3225 | 913.72 |
293.15 | 0.3865 | 907.74 |
293.15 | 0.4525 | 901.85 |
293.15 | 0.5121 | 896.75 |
293.15 | 0.5853 | 890.75 |
293.15 | 0.6441 | 886.12 |
293.15 | 0.7154 | 880.72 |
293.15 | 0.7664 | 876.98 |
293.15 | 0.8353 | 872.08 |
293.15 | 0.8901 | 868.29 |
293.15 | 0.9577 | 863.74 |
303.15 | 0.0625 | 931.96 |
303.15 | 0.1321 | 924.04 |
303.15 | 0.1912 | 917.66 |
303.15 | 0.2684 | 909.75 |
303.15 | 0.3325 | 903.53 |
303.15 | 0.3965 | 897.61 |
303.15 | 0.4584 | 892.15 |
303.15 | 0.5214 | 886.82 |
303.15 | 0.5853 | 881.64 |
303.15 | 0.6485 | 876.73 |
303.15 | 0.7112 | 872.04 |
303.15 | 0.7866 | 866.61 |
303.15 | 0.8415 | 862.79 |
303.15 | 0.9054 | 858.48 |
303.15 | 0.9658 | 854.51 |
313.15 | 0.0455 | 924.59 |
313.15 | 0.1112 | 916.97 |
313.15 | 0.1862 | 908.77 |
313.15 | 0.2562 | 901.56 |
313.15 | 0.3215 | 895.19 |
313.15 | 0.3952 | 888.37 |
313.15 | 0.4514 | 883.43 |
313.15 | 0.5111 | 878.4 |
313.15 | 0.5841 | 872.52 |
313.15 | 0.6451 | 867.83 |
313.15 | 0.7124 | 862.86 |
313.15 | 0.7854 | 857.69 |
313.15 | 0.8451 | 853.61 |
313.15 | 0.9011 | 849.9 |
313.15 | 0.9655 | 845.75 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of p-Xylene (1) - Liquid | Mass density, kg/m3 - Liquid |
293.15 | 0.0562 | 941.87 |
293.15 | 0.1211 | 934.47 |
293.15 | 0.1885 | 927.18 |
293.15 | 0.2532 | 920.51 |
293.15 | 0.3225 | 913.72 |
293.15 | 0.3865 | 907.74 |
293.15 | 0.4525 | 901.85 |
293.15 | 0.5121 | 896.75 |
293.15 | 0.5853 | 890.75 |
293.15 | 0.6441 | 886.12 |
293.15 | 0.7154 | 880.72 |
293.15 | 0.7664 | 876.98 |
293.15 | 0.8353 | 872.08 |
293.15 | 0.8901 | 868.29 |
293.15 | 0.9577 | 863.74 |
303.15 | 0.0625 | 931.96 |
303.15 | 0.1321 | 924.04 |
303.15 | 0.1912 | 917.66 |
303.15 | 0.2684 | 909.75 |
303.15 | 0.3325 | 903.53 |
303.15 | 0.3965 | 897.61 |
303.15 | 0.4584 | 892.15 |
303.15 | 0.5214 | 886.82 |
303.15 | 0.5853 | 881.64 |
303.15 | 0.6485 | 876.73 |
303.15 | 0.7112 | 872.04 |
303.15 | 0.7866 | 866.61 |
303.15 | 0.8415 | 862.79 |
303.15 | 0.9054 | 858.48 |
303.15 | 0.9658 | 854.51 |
313.15 | 0.0455 | 924.59 |
313.15 | 0.1112 | 916.97 |
313.15 | 0.1862 | 908.77 |
313.15 | 0.2562 | 901.56 |
313.15 | 0.3215 | 895.19 |
313.15 | 0.3952 | 888.37 |
313.15 | 0.4514 | 883.43 |
313.15 | 0.5111 | 878.4 |
313.15 | 0.5841 | 872.52 |
313.15 | 0.6451 | 867.83 |
313.15 | 0.7124 | 862.86 |
313.15 | 0.7854 | 857.69 |
313.15 | 0.8451 | 853.61 |
313.15 | 0.9011 | 849.9 |
313.15 | 0.9655 | 845.75 |
Operational condition: Pressure, kPa = 95.1 (Liquid)
Mole fraction of p-Xylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 420.95 |
0.0648 | 418.15 |
0.1219 | 415.95 |
0.1724 | 414.35 |
0.2173 | 413.15 |
0.2577 | 412.25 |
0.2943 | 411.45 |
0.3271 | 410.85 |
0.3571 | 410.25 |
0.3847 | 409.85 |
0.4099 | 409.45 |
0.4331 | 409.15 |
0.4546 | 408.85 |
0.4745 | 408.65 |
0.4930 | 408.45 |
0.5103 | 408.25 |
0.5173 | 408.15 |
0.5556 | 407.85 |
0.6001 | 407.55 |
0.6522 | 407.25 |
0.7144 | 407.05 |
0.7899 | 406.95 |
0.8824 | 407.35 |
1.0000 | 408.65 |
Operational condition: Pressure, kPa = 95.1 (Liquid)
Mole fraction of p-Xylene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 420.95 |
0.0648 | 418.15 |
0.1219 | 415.95 |
0.1724 | 414.35 |
0.2173 | 413.15 |
0.2577 | 412.25 |
0.2943 | 411.45 |
0.3271 | 410.85 |
0.3571 | 410.25 |
0.3847 | 409.85 |
0.4099 | 409.45 |
0.4331 | 409.15 |
0.4546 | 408.85 |
0.4745 | 408.65 |
0.4930 | 408.45 |
0.5103 | 408.25 |
0.5173 | 408.15 |
0.5556 | 407.85 |
0.6001 | 407.55 |
0.6522 | 407.25 |
0.7144 | 407.05 |
0.7899 | 406.95 |
0.8824 | 407.35 |
1.0000 | 408.65 |