Mixture of Ethanol, 2-ethoxy- + Cyclohexane, methyl-
Datasets
-
Mole fraction (4)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Azeotropic temperature, K (2)
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 |
0.0070 |
50.00 |
0.0550 |
0.0200 |
50.00 |
0.1450 |
0.0490 |
50.00 |
0.3010 |
0.0770 |
50.00 |
0.4180 |
0.1170 |
50.00 |
0.5340 |
0.1660 |
50.00 |
0.6350 |
0.3000 |
50.00 |
0.7580 |
0.3580 |
50.00 |
0.7860 |
0.4090 |
50.00 |
0.8050 |
0.4600 |
50.00 |
0.8170 |
0.6560 |
50.00 |
0.8440 |
0.7210 |
50.00 |
0.8510 |
0.7800 |
50.00 |
0.8580 |
0.7940 |
50.00 |
0.8620 |
0.8370 |
50.00 |
0.8660 |
0.8780 |
50.00 |
0.8840 |
0.9220 |
50.00 |
0.9040 |
0.9790 |
50.00 |
0.9600 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
101.33 |
0.0000 |
0.0180 |
101.33 |
0.0950 |
0.0350 |
101.33 |
0.1790 |
0.0460 |
101.33 |
0.2260 |
0.0790 |
101.33 |
0.3460 |
0.0910 |
101.33 |
0.3820 |
0.1170 |
101.33 |
0.4560 |
0.1950 |
101.33 |
0.6120 |
0.2860 |
101.33 |
0.7050 |
0.4090 |
101.33 |
0.7680 |
0.4650 |
101.33 |
0.7840 |
0.5080 |
101.33 |
0.7940 |
0.5650 |
101.33 |
0.8040 |
0.6720 |
101.33 |
0.8170 |
0.7020 |
101.33 |
0.8200 |
0.7530 |
101.33 |
0.8270 |
0.8490 |
101.33 |
0.8470 |
0.8720 |
101.33 |
0.8560 |
0.9360 |
101.33 |
0.8980 |
0.9670 |
101.33 |
0.9360 |
0.9880 |
101.33 |
0.9760 |
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 |
0.8831 |
101.33 |
0.8472 |
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 |
0.0070 |
50.00 |
0.0550 |
0.0200 |
50.00 |
0.1450 |
0.0490 |
50.00 |
0.3010 |
0.0770 |
50.00 |
0.4180 |
0.1170 |
50.00 |
0.5340 |
0.1660 |
50.00 |
0.6350 |
0.3000 |
50.00 |
0.7580 |
0.3580 |
50.00 |
0.7860 |
0.4090 |
50.00 |
0.8050 |
0.4600 |
50.00 |
0.8170 |
0.6560 |
50.00 |
0.8440 |
0.7210 |
50.00 |
0.8510 |
0.7800 |
50.00 |
0.8580 |
0.7940 |
50.00 |
0.8620 |
0.8370 |
50.00 |
0.8660 |
0.8780 |
50.00 |
0.8840 |
0.9220 |
50.00 |
0.9040 |
0.9790 |
50.00 |
0.9600 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
101.33 |
0.0000 |
0.0180 |
101.33 |
0.0950 |
0.0350 |
101.33 |
0.1790 |
0.0460 |
101.33 |
0.2260 |
0.0790 |
101.33 |
0.3460 |
0.0910 |
101.33 |
0.3820 |
0.1170 |
101.33 |
0.4560 |
0.1950 |
101.33 |
0.6120 |
0.2860 |
101.33 |
0.7050 |
0.4090 |
101.33 |
0.7680 |
0.4650 |
101.33 |
0.7840 |
0.5080 |
101.33 |
0.7940 |
0.5650 |
101.33 |
0.8040 |
0.6720 |
101.33 |
0.8170 |
0.7020 |
101.33 |
0.8200 |
0.7530 |
101.33 |
0.8270 |
0.8490 |
101.33 |
0.8470 |
0.8720 |
101.33 |
0.8560 |
0.9360 |
101.33 |
0.8980 |
0.9670 |
101.33 |
0.9360 |
0.9880 |
101.33 |
0.9760 |
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 |
0.8831 |
101.33 |
0.8472 |
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 |
386.58 |
0.0070 |
50.00 |
384.70 |
0.0200 |
50.00 |
382.32 |
0.0490 |
50.00 |
377.45 |
0.0770 |
50.00 |
373.18 |
0.1170 |
50.00 |
368.10 |
0.1660 |
50.00 |
363.05 |
0.3000 |
50.00 |
355.31 |
0.3580 |
50.00 |
353.45 |
0.4090 |
50.00 |
352.25 |
0.4600 |
50.00 |
351.41 |
0.6560 |
50.00 |
349.80 |
0.7210 |
50.00 |
349.60 |
0.7800 |
50.00 |
349.43 |
0.7940 |
50.00 |
349.38 |
0.8370 |
50.00 |
349.27 |
0.8780 |
50.00 |
349.19 |
0.9220 |
50.00 |
349.25 |
0.9790 |
50.00 |
349.87 |
1.0000 |
50.00 |
350.62 |
0.0000 |
101.33 |
408.62 |
0.0180 |
101.33 |
405.76 |
0.0350 |
101.33 |
403.18 |
0.0460 |
101.33 |
401.61 |
0.0790 |
101.33 |
397.23 |
0.0910 |
101.33 |
395.66 |
0.1170 |
101.33 |
392.61 |
0.1950 |
101.33 |
384.65 |
0.2860 |
101.33 |
378.95 |
0.4090 |
101.33 |
374.73 |
0.4650 |
101.33 |
373.64 |
0.5080 |
101.33 |
373.04 |
0.5650 |
101.33 |
372.48 |
0.6720 |
101.33 |
371.87 |
0.7020 |
101.33 |
371.76 |
0.7530 |
101.33 |
371.60 |
0.8490 |
101.33 |
371.44 |
0.8720 |
101.33 |
371.46 |
0.9360 |
101.33 |
371.94 |
0.9670 |
101.33 |
372.59 |
0.9880 |
101.33 |
373.39 |
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 |
386.58 |
0.0070 |
50.00 |
384.70 |
0.0200 |
50.00 |
382.32 |
0.0490 |
50.00 |
377.45 |
0.0770 |
50.00 |
373.18 |
0.1170 |
50.00 |
368.10 |
0.1660 |
50.00 |
363.05 |
0.3000 |
50.00 |
355.31 |
0.3580 |
50.00 |
353.45 |
0.4090 |
50.00 |
352.25 |
0.4600 |
50.00 |
351.41 |
0.6560 |
50.00 |
349.80 |
0.7210 |
50.00 |
349.60 |
0.7800 |
50.00 |
349.43 |
0.7940 |
50.00 |
349.38 |
0.8370 |
50.00 |
349.27 |
0.8780 |
50.00 |
349.19 |
0.9220 |
50.00 |
349.25 |
0.9790 |
50.00 |
349.87 |
1.0000 |
50.00 |
350.62 |
0.0000 |
101.33 |
408.62 |
0.0180 |
101.33 |
405.76 |
0.0350 |
101.33 |
403.18 |
0.0460 |
101.33 |
401.61 |
0.0790 |
101.33 |
397.23 |
0.0910 |
101.33 |
395.66 |
0.1170 |
101.33 |
392.61 |
0.1950 |
101.33 |
384.65 |
0.2860 |
101.33 |
378.95 |
0.4090 |
101.33 |
374.73 |
0.4650 |
101.33 |
373.64 |
0.5080 |
101.33 |
373.04 |
0.5650 |
101.33 |
372.48 |
0.6720 |
101.33 |
371.87 |
0.7020 |
101.33 |
371.76 |
0.7530 |
101.33 |
371.60 |
0.8490 |
101.33 |
371.44 |
0.8720 |
101.33 |
371.46 |
0.9360 |
101.33 |
371.94 |
0.9670 |
101.33 |
372.59 |
0.9880 |
101.33 |
373.39 |
1.0000 |
101.33 |
373.88 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Gas |
Azeotropic temperature, K - Liquid |
50.00 |
349.25 |
101.33 |
371.42 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Gas |
Azeotropic temperature, K - Liquid |
50.00 |
349.25 |
101.33 |
371.42 |
Sources