Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Diisopropyl ether (1) - Liquid | Mole fraction of Isopropyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
0.0340 | 0.7400 | 349.41 |
0.0410 | 0.3200 | 350.08 |
0.0490 | 0.0390 | 359.63 |
0.0490 | 0.5670 | 348.86 |
0.0530 | 0.9020 | 350.77 |
0.0850 | 0.1720 | 350.97 |
0.0850 | 0.6000 | 348.09 |
0.0940 | 0.0740 | 354.61 |
0.0980 | 0.3790 | 348.59 |
0.0990 | 0.8100 | 348.32 |
0.1360 | 0.6580 | 346.86 |
0.1790 | 0.5050 | 346.62 |
0.1910 | 0.4280 | 346.71 |
0.1910 | 0.7040 | 345.92 |
0.2040 | 0.1700 | 349.13 |
0.2110 | 0.2660 | 347.64 |
0.2360 | 0.0520 | 354.79 |
0.2810 | 0.5170 | 344.50 |
0.2920 | 0.3980 | 345.29 |
0.2930 | 0.3240 | 345.85 |
0.2940 | 0.6030 | 344.06 |
0.2980 | 0.0940 | 350.26 |
0.3060 | 0.6490 | 343.50 |
0.3260 | 0.1600 | 347.47 |
0.3830 | 0.4140 | 343.43 |
0.3980 | 0.2060 | 345.60 |
0.3980 | 0.2890 | 344.49 |
0.3990 | 0.4980 | 342.65 |
0.4510 | 0.0520 | 350.50 |
0.4800 | 0.4870 | 341.53 |
0.4880 | 0.3070 | 342.67 |
0.4990 | 0.1030 | 346.34 |
0.5090 | 0.1780 | 344.21 |
0.5140 | 0.3830 | 341.68 |
0.5960 | 0.1980 | 342.46 |
0.6300 | 0.2700 | 341.05 |
0.6430 | 0.0510 | 346.06 |
0.6990 | 0.0910 | 343.20 |
0.7080 | 0.2520 | 340.34 |
0.7320 | 0.1680 | 340.98 |
0.8210 | 0.0850 | 341.48 |
0.9020 | 0.0540 | 341.54 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Fixed | Measured | |
---|---|---|
Mole fraction of Diisopropyl ether (1) - Gas | Mole fraction of Isopropyl Alcohol (2) - Gas | Boiling temperature at pressure P, K - Gas |
0.0570 | 0.5400 | 350.08 |
0.0640 | 0.6540 | 349.41 |
0.0710 | 0.5880 | 348.86 |
0.0950 | 0.2660 | 359.63 |
0.1210 | 0.4620 | 350.97 |
0.1340 | 0.5190 | 348.59 |
0.1340 | 0.5710 | 348.09 |
0.1560 | 0.3480 | 354.61 |
0.1630 | 0.7510 | 350.77 |
0.2320 | 0.5510 | 346.86 |
0.2380 | 0.6290 | 348.32 |
0.2530 | 0.4760 | 346.71 |
0.2540 | 0.4950 | 346.62 |
0.2620 | 0.4300 | 347.64 |
0.2640 | 0.3940 | 349.13 |
0.3370 | 0.5320 | 345.92 |
0.3560 | 0.4050 | 345.85 |
0.3670 | 0.4200 | 345.29 |
0.3790 | 0.1890 | 354.79 |
0.3910 | 0.3300 | 347.47 |
0.3940 | 0.4420 | 344.50 |
0.3980 | 0.2690 | 350.26 |
0.4470 | 0.4560 | 344.06 |
0.4550 | 0.3260 | 345.60 |
0.4600 | 0.3530 | 344.49 |
0.4790 | 0.3820 | 343.43 |
0.5080 | 0.4510 | 343.50 |
0.5330 | 0.3930 | 342.65 |
0.5570 | 0.3230 | 342.67 |
0.5600 | 0.2740 | 344.21 |
0.5800 | 0.2120 | 346.34 |
0.6060 | 0.1130 | 350.50 |
0.6070 | 0.3340 | 341.68 |
0.6140 | 0.3650 | 341.53 |
0.6370 | 0.2580 | 342.46 |
0.6780 | 0.2750 | 341.05 |
0.7360 | 0.2520 | 340.34 |
0.7470 | 0.1550 | 343.20 |
0.7480 | 0.2110 | 340.98 |
0.7500 | 0.0950 | 346.06 |
0.8340 | 0.1300 | 341.48 |
0.9080 | 0.0820 | 341.54 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Diisopropyl ether (1) - Liquid | Mole fraction of Isopropyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
0.0340 | 0.7400 | 349.41 |
0.0410 | 0.3200 | 350.08 |
0.0490 | 0.0390 | 359.63 |
0.0490 | 0.5670 | 348.86 |
0.0530 | 0.9020 | 350.77 |
0.0850 | 0.1720 | 350.97 |
0.0850 | 0.6000 | 348.09 |
0.0940 | 0.0740 | 354.61 |
0.0980 | 0.3790 | 348.59 |
0.0990 | 0.8100 | 348.32 |
0.1360 | 0.6580 | 346.86 |
0.1790 | 0.5050 | 346.62 |
0.1910 | 0.4280 | 346.71 |
0.1910 | 0.7040 | 345.92 |
0.2040 | 0.1700 | 349.13 |
0.2110 | 0.2660 | 347.64 |
0.2360 | 0.0520 | 354.79 |
0.2810 | 0.5170 | 344.50 |
0.2920 | 0.3980 | 345.29 |
0.2930 | 0.3240 | 345.85 |
0.2940 | 0.6030 | 344.06 |
0.2980 | 0.0940 | 350.26 |
0.3060 | 0.6490 | 343.50 |
0.3260 | 0.1600 | 347.47 |
0.3830 | 0.4140 | 343.43 |
0.3980 | 0.2060 | 345.60 |
0.3980 | 0.2890 | 344.49 |
0.3990 | 0.4980 | 342.65 |
0.4510 | 0.0520 | 350.50 |
0.4800 | 0.4870 | 341.53 |
0.4880 | 0.3070 | 342.67 |
0.4990 | 0.1030 | 346.34 |
0.5090 | 0.1780 | 344.21 |
0.5140 | 0.3830 | 341.68 |
0.5960 | 0.1980 | 342.46 |
0.6300 | 0.2700 | 341.05 |
0.6430 | 0.0510 | 346.06 |
0.6990 | 0.0910 | 343.20 |
0.7080 | 0.2520 | 340.34 |
0.7320 | 0.1680 | 340.98 |
0.8210 | 0.0850 | 341.48 |
0.9020 | 0.0540 | 341.54 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Fixed | Measured | |
---|---|---|
Mole fraction of Diisopropyl ether (1) - Gas | Mole fraction of Isopropyl Alcohol (2) - Gas | Boiling temperature at pressure P, K - Gas |
0.0570 | 0.5400 | 350.08 |
0.0640 | 0.6540 | 349.41 |
0.0710 | 0.5880 | 348.86 |
0.0950 | 0.2660 | 359.63 |
0.1210 | 0.4620 | 350.97 |
0.1340 | 0.5190 | 348.59 |
0.1340 | 0.5710 | 348.09 |
0.1560 | 0.3480 | 354.61 |
0.1630 | 0.7510 | 350.77 |
0.2320 | 0.5510 | 346.86 |
0.2380 | 0.6290 | 348.32 |
0.2530 | 0.4760 | 346.71 |
0.2540 | 0.4950 | 346.62 |
0.2620 | 0.4300 | 347.64 |
0.2640 | 0.3940 | 349.13 |
0.3370 | 0.5320 | 345.92 |
0.3560 | 0.4050 | 345.85 |
0.3670 | 0.4200 | 345.29 |
0.3790 | 0.1890 | 354.79 |
0.3910 | 0.3300 | 347.47 |
0.3940 | 0.4420 | 344.50 |
0.3980 | 0.2690 | 350.26 |
0.4470 | 0.4560 | 344.06 |
0.4550 | 0.3260 | 345.60 |
0.4600 | 0.3530 | 344.49 |
0.4790 | 0.3820 | 343.43 |
0.5080 | 0.4510 | 343.50 |
0.5330 | 0.3930 | 342.65 |
0.5570 | 0.3230 | 342.67 |
0.5600 | 0.2740 | 344.21 |
0.5800 | 0.2120 | 346.34 |
0.6060 | 0.1130 | 350.50 |
0.6070 | 0.3340 | 341.68 |
0.6140 | 0.3650 | 341.53 |
0.6370 | 0.2580 | 342.46 |
0.6780 | 0.2750 | 341.05 |
0.7360 | 0.2520 | 340.34 |
0.7470 | 0.1550 | 343.20 |
0.7480 | 0.2110 | 340.98 |
0.7500 | 0.0950 | 346.06 |
0.8340 | 0.1300 | 341.48 |
0.9080 | 0.0820 | 341.54 |