Datasets
-
Mole fraction (6)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
-
Tboil - Boiling temperature at pressure P, K (4)
Mole fraction of Methyl Alcohol (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Gas)
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0000 |
0.0000 |
0.0390 |
0.1140 |
0.0790 |
0.2040 |
0.1210 |
0.2780 |
0.1760 |
0.3610 |
0.2220 |
0.4160 |
0.2800 |
0.4750 |
0.3260 |
0.5120 |
0.3930 |
0.5550 |
0.4370 |
0.5860 |
0.4860 |
0.6210 |
0.5480 |
0.6600 |
0.5990 |
0.6890 |
0.6410 |
0.7130 |
0.6880 |
0.7380 |
0.7400 |
0.7720 |
0.7910 |
0.8020 |
0.8520 |
0.8490 |
0.9000 |
0.8860 |
0.9560 |
0.9460 |
1.0000 |
1.0000 |
Mole fraction of Methyl Alcohol (2)
[ref]
Operational condition: Pressure, kPa =
101.23 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0910 |
0.2400 |
0.1450 |
0.3210 |
0.1910 |
0.3730 |
0.3440 |
0.5200 |
0.3900 |
0.5550 |
0.4930 |
0.6280 |
0.5480 |
0.6560 |
0.5940 |
0.6900 |
0.6240 |
0.7020 |
0.6540 |
0.7250 |
0.7010 |
0.7460 |
0.7540 |
0.7770 |
0.8020 |
0.8110 |
0.9020 |
0.8880 |
0.9020 |
0.8890 |
0.9500 |
0.9390 |
0.9760 |
0.9680 |
1.0000 |
1.0000 |
Mole fraction of Methyl Alcohol (2)
[ref]
Fixed |
Measured |
Mole fraction of Methyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0000 |
383.30 |
0.0000 |
0.1310 |
383.30 |
0.2660 |
0.2920 |
383.30 |
0.4800 |
0.3850 |
383.30 |
0.5730 |
0.5450 |
383.30 |
0.7010 |
0.5990 |
383.30 |
0.7310 |
0.7200 |
383.30 |
0.8000 |
0.7780 |
383.30 |
0.8340 |
0.8630 |
383.30 |
0.8900 |
0.9060 |
383.30 |
0.9170 |
0.9740 |
383.30 |
0.9750 |
1.0000 |
383.30 |
1.0000 |
0.0000 |
398.10 |
0.0000 |
0.1650 |
398.10 |
0.3380 |
0.3050 |
398.10 |
0.5210 |
0.3820 |
398.10 |
0.5910 |
0.4590 |
398.10 |
0.6560 |
0.5480 |
398.10 |
0.7030 |
0.6930 |
398.10 |
0.7980 |
0.8490 |
398.10 |
0.8870 |
1.0000 |
398.10 |
1.0000 |
0.0000 |
413.20 |
0.0000 |
0.1130 |
413.20 |
0.2560 |
0.1710 |
413.20 |
0.3480 |
0.2540 |
413.20 |
0.4590 |
0.3510 |
413.20 |
0.5510 |
0.4340 |
413.20 |
0.6280 |
0.5500 |
413.20 |
0.7150 |
0.6730 |
413.20 |
0.7860 |
0.7800 |
413.20 |
0.8500 |
0.8890 |
413.20 |
0.9140 |
1.0000 |
413.20 |
1.0000 |
Mole fraction of Methyl Alcohol (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Gas)
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0000 |
0.0000 |
0.0390 |
0.1140 |
0.0790 |
0.2040 |
0.1210 |
0.2780 |
0.1760 |
0.3610 |
0.2220 |
0.4160 |
0.2800 |
0.4750 |
0.3260 |
0.5120 |
0.3930 |
0.5550 |
0.4370 |
0.5860 |
0.4860 |
0.6210 |
0.5480 |
0.6600 |
0.5990 |
0.6890 |
0.6410 |
0.7130 |
0.6880 |
0.7380 |
0.7400 |
0.7720 |
0.7910 |
0.8020 |
0.8520 |
0.8490 |
0.9000 |
0.8860 |
0.9560 |
0.9460 |
1.0000 |
1.0000 |
Mole fraction of Methyl Alcohol (2)
[ref]
Operational condition: Pressure, kPa =
101.23 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0910 |
0.2400 |
0.1450 |
0.3210 |
0.1910 |
0.3730 |
0.3440 |
0.5200 |
0.3900 |
0.5550 |
0.4930 |
0.6280 |
0.5480 |
0.6560 |
0.5940 |
0.6900 |
0.6240 |
0.7020 |
0.6540 |
0.7250 |
0.7010 |
0.7460 |
0.7540 |
0.7770 |
0.8020 |
0.8110 |
0.9020 |
0.8880 |
0.9020 |
0.8890 |
0.9500 |
0.9390 |
0.9760 |
0.9680 |
1.0000 |
1.0000 |
Mole fraction of Methyl Alcohol (2)
[ref]
Fixed |
Measured |
Mole fraction of Methyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Methyl Alcohol (2) - Gas |
0.0000 |
383.30 |
0.0000 |
0.1310 |
383.30 |
0.2660 |
0.2920 |
383.30 |
0.4800 |
0.3850 |
383.30 |
0.5730 |
0.5450 |
383.30 |
0.7010 |
0.5990 |
383.30 |
0.7310 |
0.7200 |
383.30 |
0.8000 |
0.7780 |
383.30 |
0.8340 |
0.8630 |
383.30 |
0.8900 |
0.9060 |
383.30 |
0.9170 |
0.9740 |
383.30 |
0.9750 |
1.0000 |
383.30 |
1.0000 |
0.0000 |
398.10 |
0.0000 |
0.1650 |
398.10 |
0.3380 |
0.3050 |
398.10 |
0.5210 |
0.3820 |
398.10 |
0.5910 |
0.4590 |
398.10 |
0.6560 |
0.5480 |
398.10 |
0.7030 |
0.6930 |
398.10 |
0.7980 |
0.8490 |
398.10 |
0.8870 |
1.0000 |
398.10 |
1.0000 |
0.0000 |
413.20 |
0.0000 |
0.1130 |
413.20 |
0.2560 |
0.1710 |
413.20 |
0.3480 |
0.2540 |
413.20 |
0.4590 |
0.3510 |
413.20 |
0.5510 |
0.4340 |
413.20 |
0.6280 |
0.5500 |
413.20 |
0.7150 |
0.6730 |
413.20 |
0.7860 |
0.7800 |
413.20 |
0.8500 |
0.8890 |
413.20 |
0.9140 |
1.0000 |
413.20 |
1.0000 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Methyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
383.30 |
245.60 |
0.1310 |
383.30 |
305.90 |
0.2920 |
383.30 |
359.30 |
0.3850 |
383.30 |
387.00 |
0.5450 |
383.30 |
427.10 |
0.5990 |
383.30 |
436.40 |
0.7200 |
383.30 |
455.30 |
0.7780 |
383.30 |
463.50 |
0.8630 |
383.30 |
472.10 |
0.9060 |
383.30 |
476.30 |
0.9740 |
383.30 |
479.40 |
1.0000 |
383.30 |
480.70 |
0.0000 |
398.10 |
358.50 |
0.1650 |
398.10 |
466.30 |
0.3050 |
398.10 |
540.70 |
0.3820 |
398.10 |
576.70 |
0.4590 |
398.10 |
608.00 |
0.5480 |
398.10 |
637.00 |
0.6930 |
398.10 |
678.70 |
0.8490 |
398.10 |
713.20 |
1.0000 |
398.10 |
733.70 |
0.0000 |
413.20 |
506.60 |
0.1130 |
413.20 |
619.80 |
0.1710 |
413.20 |
668.00 |
0.2540 |
413.20 |
731.70 |
0.3510 |
413.20 |
800.60 |
0.4340 |
413.20 |
853.50 |
0.5500 |
413.20 |
920.20 |
0.6730 |
413.20 |
981.10 |
0.7800 |
413.20 |
1024.60 |
0.8890 |
413.20 |
1059.50 |
1.0000 |
413.20 |
1086.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Methyl Alcohol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
383.30 |
245.60 |
0.1310 |
383.30 |
305.90 |
0.2920 |
383.30 |
359.30 |
0.3850 |
383.30 |
387.00 |
0.5450 |
383.30 |
427.10 |
0.5990 |
383.30 |
436.40 |
0.7200 |
383.30 |
455.30 |
0.7780 |
383.30 |
463.50 |
0.8630 |
383.30 |
472.10 |
0.9060 |
383.30 |
476.30 |
0.9740 |
383.30 |
479.40 |
1.0000 |
383.30 |
480.70 |
0.0000 |
398.10 |
358.50 |
0.1650 |
398.10 |
466.30 |
0.3050 |
398.10 |
540.70 |
0.3820 |
398.10 |
576.70 |
0.4590 |
398.10 |
608.00 |
0.5480 |
398.10 |
637.00 |
0.6930 |
398.10 |
678.70 |
0.8490 |
398.10 |
713.20 |
1.0000 |
398.10 |
733.70 |
0.0000 |
413.20 |
506.60 |
0.1130 |
413.20 |
619.80 |
0.1710 |
413.20 |
668.00 |
0.2540 |
413.20 |
731.70 |
0.3510 |
413.20 |
800.60 |
0.4340 |
413.20 |
853.50 |
0.5500 |
413.20 |
920.20 |
0.6730 |
413.20 |
981.10 |
0.7800 |
413.20 |
1024.60 |
0.8890 |
413.20 |
1059.50 |
1.0000 |
413.20 |
1086.00 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
293.15 |
791.283 |
0.0000 |
298.15 |
786.577 |
0.0000 |
303.15 |
781.849 |
0.0000 |
308.15 |
777.101 |
0.0000 |
313.15 |
772.316 |
0.0000 |
318.15 |
767.513 |
0.0000 |
323.15 |
762.669 |
0.0962 |
293.15 |
795.933 |
0.0962 |
298.15 |
791.075 |
0.0962 |
303.15 |
786.188 |
0.0962 |
308.15 |
781.263 |
0.0962 |
313.15 |
776.323 |
0.0962 |
318.15 |
771.341 |
0.0962 |
323.15 |
766.318 |
0.2200 |
293.15 |
799.736 |
0.2200 |
298.15 |
794.761 |
0.2200 |
303.15 |
789.746 |
0.2200 |
308.15 |
784.692 |
0.2200 |
313.15 |
779.594 |
0.2200 |
318.15 |
774.457 |
0.2200 |
323.15 |
769.28 |
0.3083 |
293.15 |
801.566 |
0.3083 |
298.15 |
796.52 |
0.3083 |
303.15 |
791.443 |
0.3083 |
308.15 |
786.319 |
0.3083 |
313.15 |
781.154 |
0.3083 |
318.15 |
775.936 |
0.3083 |
323.15 |
770.68 |
0.3858 |
293.15 |
802.742 |
0.3858 |
298.15 |
797.675 |
0.3858 |
303.15 |
792.552 |
0.3858 |
308.15 |
787.383 |
0.3858 |
313.15 |
782.172 |
0.3858 |
318.15 |
776.91 |
0.3858 |
323.15 |
771.601 |
0.4983 |
293.15 |
803.936 |
0.4983 |
298.15 |
798.805 |
0.4983 |
303.15 |
793.636 |
0.4983 |
308.15 |
788.417 |
0.4983 |
313.15 |
783.159 |
0.4983 |
318.15 |
777.848 |
0.4983 |
323.15 |
772.478 |
0.5781 |
293.15 |
804.516 |
0.5781 |
298.15 |
799.344 |
0.5781 |
303.15 |
794.136 |
0.5781 |
308.15 |
788.889 |
0.5781 |
313.15 |
783.601 |
0.5781 |
318.15 |
778.265 |
0.5781 |
323.15 |
772.868 |
0.6964 |
293.15 |
805.035 |
0.6964 |
298.15 |
799.83 |
0.6964 |
303.15 |
794.583 |
0.6964 |
308.15 |
789.292 |
0.6964 |
313.15 |
783.968 |
0.6964 |
318.15 |
778.602 |
0.6964 |
323.15 |
773.192 |
0.7943 |
293.15 |
805.218 |
0.7943 |
298.15 |
799.991 |
0.7943 |
303.15 |
794.727 |
0.7943 |
308.15 |
789.419 |
0.7943 |
313.15 |
784.079 |
0.7943 |
318.15 |
778.7 |
0.7943 |
323.15 |
773.276 |
0.8857 |
293.15 |
805.214 |
0.8857 |
298.15 |
799.977 |
0.8857 |
303.15 |
794.706 |
0.8857 |
308.15 |
789.4 |
0.8857 |
313.15 |
784.049 |
0.8857 |
318.15 |
778.666 |
0.8857 |
323.15 |
773.245 |
1.0000 |
293.15 |
804.965 |
1.0000 |
298.15 |
799.739 |
1.0000 |
303.15 |
794.471 |
1.0000 |
308.15 |
789.176 |
1.0000 |
313.15 |
783.846 |
1.0000 |
318.15 |
778.481 |
1.0000 |
323.15 |
773.086 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
293.15 |
791.283 |
0.0000 |
298.15 |
786.577 |
0.0000 |
303.15 |
781.849 |
0.0000 |
308.15 |
777.101 |
0.0000 |
313.15 |
772.316 |
0.0000 |
318.15 |
767.513 |
0.0000 |
323.15 |
762.669 |
0.0962 |
293.15 |
795.933 |
0.0962 |
298.15 |
791.075 |
0.0962 |
303.15 |
786.188 |
0.0962 |
308.15 |
781.263 |
0.0962 |
313.15 |
776.323 |
0.0962 |
318.15 |
771.341 |
0.0962 |
323.15 |
766.318 |
0.2200 |
293.15 |
799.736 |
0.2200 |
298.15 |
794.761 |
0.2200 |
303.15 |
789.746 |
0.2200 |
308.15 |
784.692 |
0.2200 |
313.15 |
779.594 |
0.2200 |
318.15 |
774.457 |
0.2200 |
323.15 |
769.28 |
0.3083 |
293.15 |
801.566 |
0.3083 |
298.15 |
796.52 |
0.3083 |
303.15 |
791.443 |
0.3083 |
308.15 |
786.319 |
0.3083 |
313.15 |
781.154 |
0.3083 |
318.15 |
775.936 |
0.3083 |
323.15 |
770.68 |
0.3858 |
293.15 |
802.742 |
0.3858 |
298.15 |
797.675 |
0.3858 |
303.15 |
792.552 |
0.3858 |
308.15 |
787.383 |
0.3858 |
313.15 |
782.172 |
0.3858 |
318.15 |
776.91 |
0.3858 |
323.15 |
771.601 |
0.4983 |
293.15 |
803.936 |
0.4983 |
298.15 |
798.805 |
0.4983 |
303.15 |
793.636 |
0.4983 |
308.15 |
788.417 |
0.4983 |
313.15 |
783.159 |
0.4983 |
318.15 |
777.848 |
0.4983 |
323.15 |
772.478 |
0.5781 |
293.15 |
804.516 |
0.5781 |
298.15 |
799.344 |
0.5781 |
303.15 |
794.136 |
0.5781 |
308.15 |
788.889 |
0.5781 |
313.15 |
783.601 |
0.5781 |
318.15 |
778.265 |
0.5781 |
323.15 |
772.868 |
0.6964 |
293.15 |
805.035 |
0.6964 |
298.15 |
799.83 |
0.6964 |
303.15 |
794.583 |
0.6964 |
308.15 |
789.292 |
0.6964 |
313.15 |
783.968 |
0.6964 |
318.15 |
778.602 |
0.6964 |
323.15 |
773.192 |
0.7943 |
293.15 |
805.218 |
0.7943 |
298.15 |
799.991 |
0.7943 |
303.15 |
794.727 |
0.7943 |
308.15 |
789.419 |
0.7943 |
313.15 |
784.079 |
0.7943 |
318.15 |
778.7 |
0.7943 |
323.15 |
773.276 |
0.8857 |
293.15 |
805.214 |
0.8857 |
298.15 |
799.977 |
0.8857 |
303.15 |
794.706 |
0.8857 |
308.15 |
789.4 |
0.8857 |
313.15 |
784.049 |
0.8857 |
318.15 |
778.666 |
0.8857 |
323.15 |
773.245 |
1.0000 |
293.15 |
804.965 |
1.0000 |
298.15 |
799.739 |
1.0000 |
303.15 |
794.471 |
1.0000 |
308.15 |
789.176 |
1.0000 |
313.15 |
783.846 |
1.0000 |
318.15 |
778.481 |
1.0000 |
323.15 |
773.086 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (1) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
293.15 |
1119.3 |
0.0000 |
298.15 |
1102.81 |
0.0000 |
303.15 |
1086.39 |
0.0000 |
308.15 |
1070.16 |
0.0000 |
313.15 |
1053.93 |
0.0000 |
318.15 |
1037.89 |
0.0000 |
323.15 |
1021.87 |
0.0962 |
293.15 |
1142.79 |
0.0962 |
298.15 |
1125.4 |
0.0962 |
303.15 |
1107.98 |
0.0962 |
308.15 |
1090.54 |
0.0962 |
313.15 |
1073.35 |
0.0962 |
318.15 |
1056.21 |
0.0962 |
323.15 |
1039.12 |
0.2200 |
293.15 |
1163.88 |
0.2200 |
298.15 |
1145.63 |
0.2200 |
303.15 |
1127.31 |
0.2200 |
308.15 |
1109.04 |
0.2200 |
313.15 |
1090.78 |
0.2200 |
318.15 |
1072.56 |
0.2200 |
323.15 |
1054.46 |
0.3083 |
293.15 |
1175.12 |
0.3083 |
298.15 |
1156.23 |
0.3083 |
303.15 |
1137.56 |
0.3083 |
308.15 |
1118.75 |
0.3083 |
313.15 |
1100.0 |
0.3083 |
318.15 |
1081.2 |
0.3083 |
323.15 |
1062.51 |
0.3858 |
293.15 |
1183.56 |
0.3858 |
298.15 |
1164.26 |
0.3858 |
303.15 |
1144.93 |
0.3858 |
308.15 |
1125.71 |
0.3858 |
313.15 |
1106.54 |
0.3858 |
318.15 |
1087.37 |
0.3858 |
323.15 |
1068.25 |
0.4983 |
293.15 |
1193.21 |
0.4983 |
298.15 |
1173.52 |
0.4983 |
303.15 |
1153.77 |
0.4983 |
308.15 |
1134.01 |
0.4983 |
313.15 |
1114.3 |
0.4983 |
318.15 |
1094.65 |
0.4983 |
323.15 |
1074.91 |
0.5781 |
293.15 |
1198.84 |
0.5781 |
298.15 |
1178.83 |
0.5781 |
303.15 |
1158.73 |
0.5781 |
308.15 |
1138.7 |
0.5781 |
313.15 |
1118.69 |
0.5781 |
318.15 |
1098.69 |
0.5781 |
323.15 |
1078.58 |
0.6964 |
293.15 |
1205.53 |
0.6964 |
298.15 |
1185.3 |
0.6964 |
303.15 |
1164.78 |
0.6964 |
308.15 |
1144.22 |
0.6964 |
313.15 |
1123.78 |
0.6964 |
318.15 |
1103.38 |
0.6964 |
323.15 |
1083.0 |
0.7943 |
293.15 |
1209.85 |
0.7943 |
298.15 |
1189.19 |
0.7943 |
303.15 |
1168.35 |
0.7943 |
308.15 |
1147.47 |
0.7943 |
313.15 |
1126.71 |
0.7943 |
318.15 |
1106.0 |
0.7943 |
323.15 |
1085.3 |
0.8857 |
293.15 |
1212.45 |
0.8857 |
298.15 |
1191.48 |
0.8857 |
303.15 |
1170.36 |
0.8857 |
308.15 |
1149.3 |
0.8857 |
313.15 |
1128.19 |
0.8857 |
318.15 |
1107.23 |
0.8857 |
323.15 |
1086.29 |
1.0000 |
293.15 |
1213.15 |
1.0000 |
298.15 |
1191.97 |
1.0000 |
303.15 |
1170.57 |
1.0000 |
308.15 |
1149.31 |
1.0000 |
313.15 |
1128.08 |
1.0000 |
318.15 |
1106.94 |
1.0000 |
323.15 |
1085.89 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (1) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
293.15 |
1119.3 |
0.0000 |
298.15 |
1102.81 |
0.0000 |
303.15 |
1086.39 |
0.0000 |
308.15 |
1070.16 |
0.0000 |
313.15 |
1053.93 |
0.0000 |
318.15 |
1037.89 |
0.0000 |
323.15 |
1021.87 |
0.0962 |
293.15 |
1142.79 |
0.0962 |
298.15 |
1125.4 |
0.0962 |
303.15 |
1107.98 |
0.0962 |
308.15 |
1090.54 |
0.0962 |
313.15 |
1073.35 |
0.0962 |
318.15 |
1056.21 |
0.0962 |
323.15 |
1039.12 |
0.2200 |
293.15 |
1163.88 |
0.2200 |
298.15 |
1145.63 |
0.2200 |
303.15 |
1127.31 |
0.2200 |
308.15 |
1109.04 |
0.2200 |
313.15 |
1090.78 |
0.2200 |
318.15 |
1072.56 |
0.2200 |
323.15 |
1054.46 |
0.3083 |
293.15 |
1175.12 |
0.3083 |
298.15 |
1156.23 |
0.3083 |
303.15 |
1137.56 |
0.3083 |
308.15 |
1118.75 |
0.3083 |
313.15 |
1100.0 |
0.3083 |
318.15 |
1081.2 |
0.3083 |
323.15 |
1062.51 |
0.3858 |
293.15 |
1183.56 |
0.3858 |
298.15 |
1164.26 |
0.3858 |
303.15 |
1144.93 |
0.3858 |
308.15 |
1125.71 |
0.3858 |
313.15 |
1106.54 |
0.3858 |
318.15 |
1087.37 |
0.3858 |
323.15 |
1068.25 |
0.4983 |
293.15 |
1193.21 |
0.4983 |
298.15 |
1173.52 |
0.4983 |
303.15 |
1153.77 |
0.4983 |
308.15 |
1134.01 |
0.4983 |
313.15 |
1114.3 |
0.4983 |
318.15 |
1094.65 |
0.4983 |
323.15 |
1074.91 |
0.5781 |
293.15 |
1198.84 |
0.5781 |
298.15 |
1178.83 |
0.5781 |
303.15 |
1158.73 |
0.5781 |
308.15 |
1138.7 |
0.5781 |
313.15 |
1118.69 |
0.5781 |
318.15 |
1098.69 |
0.5781 |
323.15 |
1078.58 |
0.6964 |
293.15 |
1205.53 |
0.6964 |
298.15 |
1185.3 |
0.6964 |
303.15 |
1164.78 |
0.6964 |
308.15 |
1144.22 |
0.6964 |
313.15 |
1123.78 |
0.6964 |
318.15 |
1103.38 |
0.6964 |
323.15 |
1083.0 |
0.7943 |
293.15 |
1209.85 |
0.7943 |
298.15 |
1189.19 |
0.7943 |
303.15 |
1168.35 |
0.7943 |
308.15 |
1147.47 |
0.7943 |
313.15 |
1126.71 |
0.7943 |
318.15 |
1106.0 |
0.7943 |
323.15 |
1085.3 |
0.8857 |
293.15 |
1212.45 |
0.8857 |
298.15 |
1191.48 |
0.8857 |
303.15 |
1170.36 |
0.8857 |
308.15 |
1149.3 |
0.8857 |
313.15 |
1128.19 |
0.8857 |
318.15 |
1107.23 |
0.8857 |
323.15 |
1086.29 |
1.0000 |
293.15 |
1213.15 |
1.0000 |
298.15 |
1191.97 |
1.0000 |
303.15 |
1170.57 |
1.0000 |
308.15 |
1149.31 |
1.0000 |
313.15 |
1128.08 |
1.0000 |
318.15 |
1106.94 |
1.0000 |
323.15 |
1085.89 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
352.80 |
0.0390 |
349.80 |
0.0790 |
347.70 |
0.1210 |
345.70 |
0.1760 |
344.10 |
0.2220 |
342.70 |
0.2800 |
341.70 |
0.3260 |
340.80 |
0.3930 |
340.00 |
0.4370 |
339.60 |
0.4860 |
339.00 |
0.5480 |
338.60 |
0.5990 |
338.20 |
0.6410 |
338.00 |
0.6880 |
337.70 |
0.7400 |
337.50 |
0.7910 |
337.40 |
0.8520 |
337.40 |
0.9000 |
337.40 |
0.9560 |
337.60 |
1.0000 |
337.90 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0910 |
348.20 |
0.1450 |
345.90 |
0.1910 |
344.50 |
0.3440 |
340.90 |
0.3900 |
340.50 |
0.4930 |
339.30 |
0.5480 |
338.70 |
0.5940 |
338.30 |
0.6240 |
338.10 |
0.6540 |
337.80 |
0.7010 |
337.70 |
0.7540 |
337.50 |
0.8020 |
337.40 |
0.9020 |
337.50 |
0.9020 |
337.60 |
0.9500 |
337.80 |
0.9760 |
337.90 |
1.0000 |
338.20 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
352.80 |
0.0390 |
349.80 |
0.0790 |
347.70 |
0.1210 |
345.70 |
0.1760 |
344.10 |
0.2220 |
342.70 |
0.2800 |
341.70 |
0.3260 |
340.80 |
0.3930 |
340.00 |
0.4370 |
339.60 |
0.4860 |
339.00 |
0.5480 |
338.60 |
0.5990 |
338.20 |
0.6410 |
338.00 |
0.6880 |
337.70 |
0.7400 |
337.50 |
0.7910 |
337.40 |
0.8520 |
337.40 |
0.9000 |
337.40 |
0.9560 |
337.60 |
1.0000 |
337.90 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
Mole fraction of Methyl Alcohol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0910 |
348.20 |
0.1450 |
345.90 |
0.1910 |
344.50 |
0.3440 |
340.90 |
0.3900 |
340.50 |
0.4930 |
339.30 |
0.5480 |
338.70 |
0.5940 |
338.30 |
0.6240 |
338.10 |
0.6540 |
337.80 |
0.7010 |
337.70 |
0.7540 |
337.50 |
0.8020 |
337.40 |
0.9020 |
337.50 |
0.9020 |
337.60 |
0.9500 |
337.80 |
0.9760 |
337.90 |
1.0000 |
338.20 |
Sources