Mixture of Ethanol, 2-methoxy- + Cyclohexane, methyl-
Datasets
-
Activity coefficient (2)
-
Mole fraction (4)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Azeotropic temperature, K (2)
Activity coefficient of Cyclohexane, methyl- (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Activity coefficient of Cyclohexane, methyl- (2) - Liquid |
298.00 |
238.00 |
0.0000 |
14.7 |
Activity coefficient of Cyclohexane, methyl- (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Activity coefficient of Cyclohexane, methyl- (2) - Liquid |
298.00 |
238.00 |
0.0000 |
14.7 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of Cyclohexane, methyl- (2) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0050 |
50.00 |
0.0500 |
0.0130 |
50.00 |
0.1210 |
0.0190 |
50.00 |
0.1610 |
0.0240 |
50.00 |
0.2000 |
0.0400 |
50.00 |
0.2980 |
0.0720 |
50.00 |
0.4500 |
0.1030 |
50.00 |
0.5260 |
0.1540 |
50.00 |
0.6210 |
0.2080 |
50.00 |
0.6820 |
0.2500 |
50.00 |
0.7170 |
0.2780 |
50.00 |
0.7240 |
0.3000 |
50.00 |
0.7310 |
0.3620 |
50.00 |
0.7440 |
0.4030 |
50.00 |
0.7490 |
0.4580 |
50.00 |
0.7470 |
0.5370 |
50.00 |
0.7480 |
0.6820 |
50.00 |
0.7500 |
0.7280 |
50.00 |
0.7550 |
0.7940 |
50.00 |
0.7640 |
0.8630 |
50.00 |
0.7880 |
0.9300 |
50.00 |
0.8470 |
0.9680 |
50.00 |
0.9140 |
0.9810 |
50.00 |
0.9440 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
101.33 |
0.0000 |
0.0030 |
101.33 |
0.0300 |
0.0090 |
101.33 |
0.0740 |
0.0160 |
101.33 |
0.1240 |
0.0320 |
101.33 |
0.2320 |
0.0470 |
101.33 |
0.3100 |
0.0510 |
101.33 |
0.3310 |
0.0640 |
101.33 |
0.3820 |
0.1370 |
101.33 |
0.5640 |
0.2310 |
101.33 |
0.6540 |
0.2960 |
101.33 |
0.6790 |
0.4570 |
101.33 |
0.6990 |
0.5660 |
101.33 |
0.7030 |
0.6160 |
101.33 |
0.7050 |
0.6700 |
101.33 |
0.7100 |
0.7130 |
101.33 |
0.7160 |
0.7550 |
101.33 |
0.7240 |
0.7840 |
101.33 |
0.7330 |
0.8200 |
101.33 |
0.7480 |
0.8480 |
101.33 |
0.7630 |
0.8620 |
101.33 |
0.7730 |
0.8820 |
101.33 |
0.7900 |
0.8980 |
101.33 |
0.8060 |
0.9390 |
101.33 |
0.8610 |
0.9730 |
101.33 |
0.9300 |
1.0000 |
101.33 |
1.0000 |
Azeotropic composition: mole fraction of Cyclohexane, methyl- (2)
[ref]
Pressure, kPa - Gas |
Azeotropic composition: mole fraction of Cyclohexane, methyl- (2) - Liquid |
50.00 |
0.7605 |
101.33 |
0.7165 |
Mole fraction of Cyclohexane, methyl- (2)
[ref]
Fixed |
Measured |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Pressure, kPa - Gas |
Mole fraction of Cyclohexane, methyl- (2) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0050 |
50.00 |
0.0500 |
0.0130 |
50.00 |
0.1210 |
0.0190 |
50.00 |
0.1610 |
0.0240 |
50.00 |
0.2000 |
0.0400 |
50.00 |
0.2980 |
0.0720 |
50.00 |
0.4500 |
0.1030 |
50.00 |
0.5260 |
0.1540 |
50.00 |
0.6210 |
0.2080 |
50.00 |
0.6820 |
0.2500 |
50.00 |
0.7170 |
0.2780 |
50.00 |
0.7240 |
0.3000 |
50.00 |
0.7310 |
0.3620 |
50.00 |
0.7440 |
0.4030 |
50.00 |
0.7490 |
0.4580 |
50.00 |
0.7470 |
0.5370 |
50.00 |
0.7480 |
0.6820 |
50.00 |
0.7500 |
0.7280 |
50.00 |
0.7550 |
0.7940 |
50.00 |
0.7640 |
0.8630 |
50.00 |
0.7880 |
0.9300 |
50.00 |
0.8470 |
0.9680 |
50.00 |
0.9140 |
0.9810 |
50.00 |
0.9440 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
101.33 |
0.0000 |
0.0030 |
101.33 |
0.0300 |
0.0090 |
101.33 |
0.0740 |
0.0160 |
101.33 |
0.1240 |
0.0320 |
101.33 |
0.2320 |
0.0470 |
101.33 |
0.3100 |
0.0510 |
101.33 |
0.3310 |
0.0640 |
101.33 |
0.3820 |
0.1370 |
101.33 |
0.5640 |
0.2310 |
101.33 |
0.6540 |
0.2960 |
101.33 |
0.6790 |
0.4570 |
101.33 |
0.6990 |
0.5660 |
101.33 |
0.7030 |
0.6160 |
101.33 |
0.7050 |
0.6700 |
101.33 |
0.7100 |
0.7130 |
101.33 |
0.7160 |
0.7550 |
101.33 |
0.7240 |
0.7840 |
101.33 |
0.7330 |
0.8200 |
101.33 |
0.7480 |
0.8480 |
101.33 |
0.7630 |
0.8620 |
101.33 |
0.7730 |
0.8820 |
101.33 |
0.7900 |
0.8980 |
101.33 |
0.8060 |
0.9390 |
101.33 |
0.8610 |
0.9730 |
101.33 |
0.9300 |
1.0000 |
101.33 |
1.0000 |
Azeotropic composition: mole fraction of Cyclohexane, methyl- (2)
[ref]
Pressure, kPa - Gas |
Azeotropic composition: mole fraction of Cyclohexane, methyl- (2) - Liquid |
50.00 |
0.7605 |
101.33 |
0.7165 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Gas |
0.0000 |
50.00 |
376.27 |
0.0050 |
50.00 |
374.91 |
0.0130 |
50.00 |
372.92 |
0.0190 |
50.00 |
371.76 |
0.0240 |
50.00 |
370.53 |
0.0400 |
50.00 |
367.35 |
0.0720 |
50.00 |
361.55 |
0.1030 |
50.00 |
358.28 |
0.1540 |
50.00 |
353.49 |
0.2080 |
50.00 |
350.07 |
0.2500 |
50.00 |
348.00 |
0.2780 |
50.00 |
347.59 |
0.3000 |
50.00 |
347.19 |
0.3620 |
50.00 |
346.46 |
0.4030 |
50.00 |
346.19 |
0.4580 |
50.00 |
346.30 |
0.5370 |
50.00 |
346.24 |
0.6820 |
50.00 |
346.21 |
0.7280 |
50.00 |
345.98 |
0.7940 |
50.00 |
346.11 |
0.8630 |
50.00 |
346.27 |
0.9300 |
50.00 |
347.37 |
0.9680 |
50.00 |
348.82 |
0.9810 |
50.00 |
349.46 |
1.0000 |
50.00 |
350.62 |
0.0000 |
101.33 |
397.67 |
0.0030 |
101.33 |
396.77 |
0.0090 |
101.33 |
395.45 |
0.0160 |
101.33 |
393.82 |
0.0320 |
101.33 |
390.14 |
0.0470 |
101.33 |
387.25 |
0.0510 |
101.33 |
386.41 |
0.0640 |
101.33 |
384.24 |
0.1370 |
101.33 |
375.80 |
0.2310 |
101.33 |
370.65 |
0.2960 |
101.33 |
369.17 |
0.4570 |
101.33 |
368.07 |
0.5660 |
101.33 |
367.93 |
0.6160 |
101.33 |
367.87 |
0.6700 |
101.33 |
367.81 |
0.7130 |
101.33 |
367.80 |
0.7550 |
101.33 |
367.83 |
0.7840 |
101.33 |
367.90 |
0.8200 |
101.33 |
368.09 |
0.8480 |
101.33 |
368.35 |
0.8620 |
101.33 |
368.56 |
0.8820 |
101.33 |
368.90 |
0.8980 |
101.33 |
369.32 |
0.9390 |
101.33 |
370.65 |
0.9730 |
101.33 |
372.25 |
1.0000 |
101.33 |
373.88 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Cyclohexane, methyl- (2) - Liquid |
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Gas |
0.0000 |
50.00 |
376.27 |
0.0050 |
50.00 |
374.91 |
0.0130 |
50.00 |
372.92 |
0.0190 |
50.00 |
371.76 |
0.0240 |
50.00 |
370.53 |
0.0400 |
50.00 |
367.35 |
0.0720 |
50.00 |
361.55 |
0.1030 |
50.00 |
358.28 |
0.1540 |
50.00 |
353.49 |
0.2080 |
50.00 |
350.07 |
0.2500 |
50.00 |
348.00 |
0.2780 |
50.00 |
347.59 |
0.3000 |
50.00 |
347.19 |
0.3620 |
50.00 |
346.46 |
0.4030 |
50.00 |
346.19 |
0.4580 |
50.00 |
346.30 |
0.5370 |
50.00 |
346.24 |
0.6820 |
50.00 |
346.21 |
0.7280 |
50.00 |
345.98 |
0.7940 |
50.00 |
346.11 |
0.8630 |
50.00 |
346.27 |
0.9300 |
50.00 |
347.37 |
0.9680 |
50.00 |
348.82 |
0.9810 |
50.00 |
349.46 |
1.0000 |
50.00 |
350.62 |
0.0000 |
101.33 |
397.67 |
0.0030 |
101.33 |
396.77 |
0.0090 |
101.33 |
395.45 |
0.0160 |
101.33 |
393.82 |
0.0320 |
101.33 |
390.14 |
0.0470 |
101.33 |
387.25 |
0.0510 |
101.33 |
386.41 |
0.0640 |
101.33 |
384.24 |
0.1370 |
101.33 |
375.80 |
0.2310 |
101.33 |
370.65 |
0.2960 |
101.33 |
369.17 |
0.4570 |
101.33 |
368.07 |
0.5660 |
101.33 |
367.93 |
0.6160 |
101.33 |
367.87 |
0.6700 |
101.33 |
367.81 |
0.7130 |
101.33 |
367.80 |
0.7550 |
101.33 |
367.83 |
0.7840 |
101.33 |
367.90 |
0.8200 |
101.33 |
368.09 |
0.8480 |
101.33 |
368.35 |
0.8620 |
101.33 |
368.56 |
0.8820 |
101.33 |
368.90 |
0.8980 |
101.33 |
369.32 |
0.9390 |
101.33 |
370.65 |
0.9730 |
101.33 |
372.25 |
1.0000 |
101.33 |
373.88 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Gas |
Azeotropic temperature, K - Liquid |
50.00 |
346.09 |
101.33 |
367.81 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Gas |
Azeotropic temperature, K - Liquid |
50.00 |
346.09 |
101.33 |
367.81 |
Sources