Mixture of 1-Methoxy-2-propyl acetate + 2-Propanol, 1-methoxy-
Datasets
-
Mole fraction (4)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 2-Propanol, 1-methoxy- (2)
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Gas |
0.0500 |
53.30 |
0.1270 |
0.0730 |
26.70 |
0.1860 |
0.0790 |
93.30 |
0.1710 |
0.1010 |
53.30 |
0.2320 |
0.1120 |
26.70 |
0.2650 |
0.1300 |
93.30 |
0.2650 |
0.1630 |
53.30 |
0.3340 |
0.1740 |
93.30 |
0.3340 |
0.1950 |
26.70 |
0.4030 |
0.2090 |
93.30 |
0.3780 |
0.2170 |
53.30 |
0.4100 |
0.2430 |
93.30 |
0.4270 |
0.2570 |
26.70 |
0.4830 |
0.2680 |
53.30 |
0.4750 |
0.3220 |
26.70 |
0.5530 |
0.3370 |
93.30 |
0.5340 |
0.3500 |
53.30 |
0.5620 |
0.3570 |
26.70 |
0.5870 |
0.3640 |
93.30 |
0.5630 |
0.4100 |
26.70 |
0.6300 |
0.4110 |
53.30 |
0.6180 |
0.4260 |
93.30 |
0.6220 |
0.4400 |
26.70 |
0.6550 |
0.4400 |
53.30 |
0.6420 |
0.4600 |
93.30 |
0.6530 |
0.4730 |
53.30 |
0.6680 |
0.5040 |
26.70 |
0.7060 |
0.5070 |
53.30 |
0.6990 |
0.5360 |
93.30 |
0.7130 |
0.5390 |
53.30 |
0.7240 |
0.5630 |
26.70 |
0.7460 |
0.5710 |
53.30 |
0.7450 |
0.5740 |
93.30 |
0.7390 |
0.6080 |
93.30 |
0.7650 |
0.6180 |
53.30 |
0.7780 |
0.6230 |
26.70 |
0.7850 |
0.6650 |
93.30 |
0.8030 |
0.6790 |
26.70 |
0.8200 |
0.7040 |
93.30 |
0.8290 |
0.7200 |
53.30 |
0.8410 |
0.7460 |
93.30 |
0.8560 |
0.7690 |
53.30 |
0.8690 |
0.7730 |
93.30 |
0.8730 |
0.7750 |
26.70 |
0.8750 |
0.8180 |
26.70 |
0.8990 |
0.8180 |
53.30 |
0.8990 |
0.8260 |
93.30 |
0.9040 |
0.8540 |
53.30 |
0.9200 |
0.8680 |
26.70 |
0.9270 |
0.8710 |
93.30 |
0.9290 |
0.8960 |
53.30 |
0.9430 |
0.9110 |
93.30 |
0.9510 |
0.9350 |
26.70 |
0.9640 |
0.9370 |
93.30 |
0.9650 |
0.9470 |
93.30 |
0.9710 |
0.9630 |
53.30 |
0.9800 |
Mole fraction of 2-Propanol, 1-methoxy- (2)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Gas |
393.30 |
1.0000 |
1.0000 |
394.40 |
0.9310 |
0.9637 |
395.60 |
0.8544 |
0.9230 |
396.40 |
0.8057 |
0.8963 |
397.70 |
0.7206 |
0.8470 |
400.20 |
0.6136 |
0.7781 |
401.40 |
0.5486 |
0.7311 |
402.90 |
0.4789 |
0.6751 |
404.80 |
0.4108 |
0.6138 |
405.90 |
0.3687 |
0.5720 |
407.90 |
0.2973 |
0.4931 |
409.90 |
0.2293 |
0.4068 |
411.60 |
0.1836 |
0.3416 |
412.50 |
0.1548 |
0.2971 |
413.50 |
0.1307 |
0.2576 |
415.30 |
0.0850 |
0.1764 |
416.00 |
0.0724 |
0.1525 |
416.40 |
0.0550 |
0.1183 |
416.90 |
0.0472 |
0.1024 |
417.40 |
0.0310 |
0.0686 |
418.30 |
0.0113 |
0.0256 |
419.00 |
0.0000 |
0.0000 |
Mole fraction of 2-Propanol, 1-methoxy- (2)
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Gas |
0.0500 |
53.30 |
0.1270 |
0.0730 |
26.70 |
0.1860 |
0.0790 |
93.30 |
0.1710 |
0.1010 |
53.30 |
0.2320 |
0.1120 |
26.70 |
0.2650 |
0.1300 |
93.30 |
0.2650 |
0.1630 |
53.30 |
0.3340 |
0.1740 |
93.30 |
0.3340 |
0.1950 |
26.70 |
0.4030 |
0.2090 |
93.30 |
0.3780 |
0.2170 |
53.30 |
0.4100 |
0.2430 |
93.30 |
0.4270 |
0.2570 |
26.70 |
0.4830 |
0.2680 |
53.30 |
0.4750 |
0.3220 |
26.70 |
0.5530 |
0.3370 |
93.30 |
0.5340 |
0.3500 |
53.30 |
0.5620 |
0.3570 |
26.70 |
0.5870 |
0.3640 |
93.30 |
0.5630 |
0.4100 |
26.70 |
0.6300 |
0.4110 |
53.30 |
0.6180 |
0.4260 |
93.30 |
0.6220 |
0.4400 |
26.70 |
0.6550 |
0.4400 |
53.30 |
0.6420 |
0.4600 |
93.30 |
0.6530 |
0.4730 |
53.30 |
0.6680 |
0.5040 |
26.70 |
0.7060 |
0.5070 |
53.30 |
0.6990 |
0.5360 |
93.30 |
0.7130 |
0.5390 |
53.30 |
0.7240 |
0.5630 |
26.70 |
0.7460 |
0.5710 |
53.30 |
0.7450 |
0.5740 |
93.30 |
0.7390 |
0.6080 |
93.30 |
0.7650 |
0.6180 |
53.30 |
0.7780 |
0.6230 |
26.70 |
0.7850 |
0.6650 |
93.30 |
0.8030 |
0.6790 |
26.70 |
0.8200 |
0.7040 |
93.30 |
0.8290 |
0.7200 |
53.30 |
0.8410 |
0.7460 |
93.30 |
0.8560 |
0.7690 |
53.30 |
0.8690 |
0.7730 |
93.30 |
0.8730 |
0.7750 |
26.70 |
0.8750 |
0.8180 |
26.70 |
0.8990 |
0.8180 |
53.30 |
0.8990 |
0.8260 |
93.30 |
0.9040 |
0.8540 |
53.30 |
0.9200 |
0.8680 |
26.70 |
0.9270 |
0.8710 |
93.30 |
0.9290 |
0.8960 |
53.30 |
0.9430 |
0.9110 |
93.30 |
0.9510 |
0.9350 |
26.70 |
0.9640 |
0.9370 |
93.30 |
0.9650 |
0.9470 |
93.30 |
0.9710 |
0.9630 |
53.30 |
0.9800 |
Mole fraction of 2-Propanol, 1-methoxy- (2)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Gas |
393.30 |
1.0000 |
1.0000 |
394.40 |
0.9310 |
0.9637 |
395.60 |
0.8544 |
0.9230 |
396.40 |
0.8057 |
0.8963 |
397.70 |
0.7206 |
0.8470 |
400.20 |
0.6136 |
0.7781 |
401.40 |
0.5486 |
0.7311 |
402.90 |
0.4789 |
0.6751 |
404.80 |
0.4108 |
0.6138 |
405.90 |
0.3687 |
0.5720 |
407.90 |
0.2973 |
0.4931 |
409.90 |
0.2293 |
0.4068 |
411.60 |
0.1836 |
0.3416 |
412.50 |
0.1548 |
0.2971 |
413.50 |
0.1307 |
0.2576 |
415.30 |
0.0850 |
0.1764 |
416.00 |
0.0724 |
0.1525 |
416.40 |
0.0550 |
0.1183 |
416.90 |
0.0472 |
0.1024 |
417.40 |
0.0310 |
0.0686 |
418.30 |
0.0113 |
0.0256 |
419.00 |
0.0000 |
0.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0500 |
53.30 |
395.34 |
0.0730 |
26.70 |
374.63 |
0.0790 |
93.30 |
411.89 |
0.1010 |
53.30 |
392.99 |
0.1120 |
26.70 |
373.03 |
0.1300 |
93.30 |
409.48 |
0.1630 |
53.30 |
391.04 |
0.1740 |
93.30 |
407.92 |
0.1950 |
26.70 |
369.87 |
0.2090 |
93.30 |
406.75 |
0.2170 |
53.30 |
389.06 |
0.2430 |
93.30 |
405.44 |
0.2570 |
26.70 |
367.95 |
0.2680 |
53.30 |
387.53 |
0.3220 |
26.70 |
366.17 |
0.3370 |
93.30 |
402.26 |
0.3500 |
53.30 |
384.95 |
0.3570 |
26.70 |
365.22 |
0.3640 |
93.30 |
401.47 |
0.4100 |
26.70 |
364.26 |
0.4110 |
53.30 |
383.37 |
0.4260 |
93.30 |
399.98 |
0.4400 |
26.70 |
363.75 |
0.4400 |
53.30 |
382.56 |
0.4600 |
93.30 |
399.08 |
0.4730 |
53.30 |
381.89 |
0.5040 |
26.70 |
362.22 |
0.5070 |
53.30 |
381.18 |
0.5360 |
93.30 |
397.55 |
0.5390 |
53.30 |
380.49 |
0.5630 |
26.70 |
361.13 |
0.5710 |
53.30 |
379.80 |
0.5740 |
93.30 |
396.68 |
0.6080 |
93.30 |
395.93 |
0.6180 |
53.30 |
378.90 |
0.6230 |
26.70 |
360.18 |
0.6650 |
93.30 |
395.00 |
0.6790 |
26.70 |
359.32 |
0.7040 |
93.30 |
394.56 |
0.7200 |
53.30 |
377.30 |
0.7460 |
93.30 |
393.78 |
0.7690 |
53.30 |
376.62 |
0.7730 |
93.30 |
393.32 |
0.7750 |
26.70 |
358.05 |
0.8180 |
26.70 |
357.50 |
0.8180 |
53.30 |
375.91 |
0.8260 |
93.30 |
392.40 |
0.8540 |
53.30 |
375.44 |
0.8680 |
26.70 |
356.92 |
0.8710 |
93.30 |
391.85 |
0.8960 |
53.30 |
374.95 |
0.9110 |
93.30 |
391.28 |
0.9350 |
26.70 |
356.03 |
0.9370 |
93.30 |
390.95 |
0.9470 |
93.30 |
390.76 |
0.9630 |
53.30 |
374.13 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0500 |
53.30 |
395.34 |
0.0730 |
26.70 |
374.63 |
0.0790 |
93.30 |
411.89 |
0.1010 |
53.30 |
392.99 |
0.1120 |
26.70 |
373.03 |
0.1300 |
93.30 |
409.48 |
0.1630 |
53.30 |
391.04 |
0.1740 |
93.30 |
407.92 |
0.1950 |
26.70 |
369.87 |
0.2090 |
93.30 |
406.75 |
0.2170 |
53.30 |
389.06 |
0.2430 |
93.30 |
405.44 |
0.2570 |
26.70 |
367.95 |
0.2680 |
53.30 |
387.53 |
0.3220 |
26.70 |
366.17 |
0.3370 |
93.30 |
402.26 |
0.3500 |
53.30 |
384.95 |
0.3570 |
26.70 |
365.22 |
0.3640 |
93.30 |
401.47 |
0.4100 |
26.70 |
364.26 |
0.4110 |
53.30 |
383.37 |
0.4260 |
93.30 |
399.98 |
0.4400 |
26.70 |
363.75 |
0.4400 |
53.30 |
382.56 |
0.4600 |
93.30 |
399.08 |
0.4730 |
53.30 |
381.89 |
0.5040 |
26.70 |
362.22 |
0.5070 |
53.30 |
381.18 |
0.5360 |
93.30 |
397.55 |
0.5390 |
53.30 |
380.49 |
0.5630 |
26.70 |
361.13 |
0.5710 |
53.30 |
379.80 |
0.5740 |
93.30 |
396.68 |
0.6080 |
93.30 |
395.93 |
0.6180 |
53.30 |
378.90 |
0.6230 |
26.70 |
360.18 |
0.6650 |
93.30 |
395.00 |
0.6790 |
26.70 |
359.32 |
0.7040 |
93.30 |
394.56 |
0.7200 |
53.30 |
377.30 |
0.7460 |
93.30 |
393.78 |
0.7690 |
53.30 |
376.62 |
0.7730 |
93.30 |
393.32 |
0.7750 |
26.70 |
358.05 |
0.8180 |
26.70 |
357.50 |
0.8180 |
53.30 |
375.91 |
0.8260 |
93.30 |
392.40 |
0.8540 |
53.30 |
375.44 |
0.8680 |
26.70 |
356.92 |
0.8710 |
93.30 |
391.85 |
0.8960 |
53.30 |
374.95 |
0.9110 |
93.30 |
391.28 |
0.9350 |
26.70 |
356.03 |
0.9370 |
93.30 |
390.95 |
0.9470 |
93.30 |
390.76 |
0.9630 |
53.30 |
374.13 |
Sources