Mixture of Ethanol, 2-propoxy- + Octane
Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Gas |
0.0000 |
60.00 |
0.0000 |
0.0000 |
80.00 |
0.0000 |
0.0000 |
100.00 |
0.0000 |
0.0100 |
60.00 |
0.0740 |
0.0100 |
80.00 |
0.0720 |
0.0100 |
100.00 |
0.0660 |
0.0190 |
60.00 |
0.1300 |
0.0190 |
80.00 |
0.1250 |
0.0190 |
100.00 |
0.1210 |
0.0310 |
60.00 |
0.2020 |
0.0340 |
80.00 |
0.2140 |
0.0340 |
100.00 |
0.2050 |
0.0720 |
60.00 |
0.3710 |
0.0840 |
80.00 |
0.3930 |
0.0880 |
100.00 |
0.4000 |
0.1470 |
60.00 |
0.5430 |
0.1590 |
80.00 |
0.5390 |
0.1720 |
100.00 |
0.5320 |
0.2610 |
60.00 |
0.6450 |
0.3000 |
80.00 |
0.6440 |
0.4110 |
100.00 |
0.6770 |
0.5890 |
60.00 |
0.7530 |
0.5900 |
100.00 |
0.7370 |
0.6010 |
80.00 |
0.7480 |
0.7470 |
60.00 |
0.8030 |
0.7710 |
100.00 |
0.7960 |
0.7800 |
80.00 |
0.8110 |
0.8220 |
100.00 |
0.8250 |
0.8330 |
80.00 |
0.8300 |
0.8350 |
60.00 |
0.8380 |
0.8400 |
100.00 |
0.8320 |
0.8780 |
80.00 |
0.8550 |
0.8810 |
60.00 |
0.8600 |
0.9100 |
100.00 |
0.8700 |
0.9610 |
60.00 |
0.9300 |
0.9620 |
80.00 |
0.9290 |
0.9640 |
100.00 |
0.9310 |
1.0000 |
60.00 |
1.0000 |
1.0000 |
80.00 |
1.0000 |
1.0000 |
100.00 |
1.0000 |
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Gas |
0.0000 |
60.00 |
0.0000 |
0.0000 |
80.00 |
0.0000 |
0.0000 |
100.00 |
0.0000 |
0.0100 |
60.00 |
0.0740 |
0.0100 |
80.00 |
0.0720 |
0.0100 |
100.00 |
0.0660 |
0.0190 |
60.00 |
0.1300 |
0.0190 |
80.00 |
0.1250 |
0.0190 |
100.00 |
0.1210 |
0.0310 |
60.00 |
0.2020 |
0.0340 |
80.00 |
0.2140 |
0.0340 |
100.00 |
0.2050 |
0.0720 |
60.00 |
0.3710 |
0.0840 |
80.00 |
0.3930 |
0.0880 |
100.00 |
0.4000 |
0.1470 |
60.00 |
0.5430 |
0.1590 |
80.00 |
0.5390 |
0.1720 |
100.00 |
0.5320 |
0.2610 |
60.00 |
0.6450 |
0.3000 |
80.00 |
0.6440 |
0.4110 |
100.00 |
0.6770 |
0.5890 |
60.00 |
0.7530 |
0.5900 |
100.00 |
0.7370 |
0.6010 |
80.00 |
0.7480 |
0.7470 |
60.00 |
0.8030 |
0.7710 |
100.00 |
0.7960 |
0.7800 |
80.00 |
0.8110 |
0.8220 |
100.00 |
0.8250 |
0.8330 |
80.00 |
0.8300 |
0.8350 |
60.00 |
0.8380 |
0.8400 |
100.00 |
0.8320 |
0.8780 |
80.00 |
0.8550 |
0.8810 |
60.00 |
0.8600 |
0.9100 |
100.00 |
0.8700 |
0.9610 |
60.00 |
0.9300 |
0.9620 |
80.00 |
0.9290 |
0.9640 |
100.00 |
0.9310 |
1.0000 |
60.00 |
1.0000 |
1.0000 |
80.00 |
1.0000 |
1.0000 |
100.00 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
60.00 |
406.15 |
0.0000 |
80.00 |
415.30 |
0.0000 |
100.00 |
422.75 |
0.0100 |
60.00 |
404.19 |
0.0100 |
80.00 |
413.19 |
0.0100 |
100.00 |
420.66 |
0.0190 |
60.00 |
402.42 |
0.0190 |
80.00 |
411.43 |
0.0190 |
100.00 |
418.77 |
0.0310 |
60.00 |
400.25 |
0.0340 |
80.00 |
408.58 |
0.0340 |
100.00 |
416.10 |
0.0720 |
60.00 |
394.40 |
0.0840 |
80.00 |
401.95 |
0.0880 |
100.00 |
408.55 |
0.1470 |
60.00 |
387.06 |
0.1590 |
80.00 |
395.65 |
0.1720 |
100.00 |
402.22 |
0.2610 |
60.00 |
382.73 |
0.3000 |
80.00 |
390.75 |
0.4110 |
100.00 |
396.31 |
0.5890 |
60.00 |
378.34 |
0.5900 |
100.00 |
394.80 |
0.6010 |
80.00 |
387.38 |
0.7470 |
60.00 |
377.72 |
0.7710 |
100.00 |
394.23 |
0.7800 |
80.00 |
386.93 |
0.8220 |
100.00 |
394.13 |
0.8330 |
80.00 |
386.73 |
0.8350 |
60.00 |
377.40 |
0.8400 |
100.00 |
394.33 |
0.8780 |
80.00 |
387.19 |
0.8810 |
60.00 |
377.87 |
0.9100 |
100.00 |
395.06 |
0.9610 |
60.00 |
379.25 |
0.9620 |
80.00 |
388.72 |
0.9640 |
100.00 |
396.37 |
1.0000 |
60.00 |
381.00 |
1.0000 |
80.00 |
390.50 |
1.0000 |
100.00 |
398.40 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
60.00 |
406.15 |
0.0000 |
80.00 |
415.30 |
0.0000 |
100.00 |
422.75 |
0.0100 |
60.00 |
404.19 |
0.0100 |
80.00 |
413.19 |
0.0100 |
100.00 |
420.66 |
0.0190 |
60.00 |
402.42 |
0.0190 |
80.00 |
411.43 |
0.0190 |
100.00 |
418.77 |
0.0310 |
60.00 |
400.25 |
0.0340 |
80.00 |
408.58 |
0.0340 |
100.00 |
416.10 |
0.0720 |
60.00 |
394.40 |
0.0840 |
80.00 |
401.95 |
0.0880 |
100.00 |
408.55 |
0.1470 |
60.00 |
387.06 |
0.1590 |
80.00 |
395.65 |
0.1720 |
100.00 |
402.22 |
0.2610 |
60.00 |
382.73 |
0.3000 |
80.00 |
390.75 |
0.4110 |
100.00 |
396.31 |
0.5890 |
60.00 |
378.34 |
0.5900 |
100.00 |
394.80 |
0.6010 |
80.00 |
387.38 |
0.7470 |
60.00 |
377.72 |
0.7710 |
100.00 |
394.23 |
0.7800 |
80.00 |
386.93 |
0.8220 |
100.00 |
394.13 |
0.8330 |
80.00 |
386.73 |
0.8350 |
60.00 |
377.40 |
0.8400 |
100.00 |
394.33 |
0.8780 |
80.00 |
387.19 |
0.8810 |
60.00 |
377.87 |
0.9100 |
100.00 |
395.06 |
0.9610 |
60.00 |
379.25 |
0.9620 |
80.00 |
388.72 |
0.9640 |
100.00 |
396.37 |
1.0000 |
60.00 |
381.00 |
1.0000 |
80.00 |
390.50 |
1.0000 |
100.00 |
398.40 |
Sources