Mixture of Heptane + Ethanol, 2-(1-methylethoxy)-
Datasets
-
Mole fraction (2)
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Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Heptane (1)
[ref]
Fixed |
Measured |
Mole fraction of Heptane (1) - Gas |
Pressure, kPa - Liquid |
Mole fraction of Heptane (1) - Liquid |
0.0000 |
60.00 |
0.0000 |
0.0000 |
80.00 |
0.0000 |
0.0000 |
100.00 |
0.0000 |
0.0870 |
80.00 |
0.0090 |
0.0970 |
100.00 |
0.0110 |
0.1430 |
60.00 |
0.0170 |
0.2150 |
100.00 |
0.0230 |
0.2380 |
80.00 |
0.0310 |
0.2790 |
60.00 |
0.0360 |
0.3290 |
100.00 |
0.0420 |
0.3610 |
80.00 |
0.0510 |
0.3990 |
60.00 |
0.0590 |
0.5100 |
80.00 |
0.0860 |
0.5770 |
60.00 |
0.1080 |
0.6050 |
100.00 |
0.1260 |
0.6440 |
80.00 |
0.1330 |
0.7190 |
60.00 |
0.1980 |
0.7330 |
80.00 |
0.1900 |
0.7390 |
100.00 |
0.2210 |
0.7830 |
80.00 |
0.2760 |
0.8180 |
60.00 |
0.3300 |
0.8250 |
100.00 |
0.4430 |
0.8390 |
100.00 |
0.5340 |
0.8510 |
80.00 |
0.4950 |
0.8580 |
60.00 |
0.4650 |
0.8750 |
60.00 |
0.5740 |
0.8870 |
60.00 |
0.6980 |
0.9170 |
80.00 |
0.8880 |
0.9210 |
100.00 |
0.8970 |
0.9240 |
60.00 |
0.9050 |
0.9260 |
80.00 |
0.9020 |
0.9300 |
80.00 |
0.9140 |
0.9310 |
100.00 |
0.9160 |
0.9380 |
100.00 |
0.9290 |
0.9440 |
80.00 |
0.9330 |
0.9580 |
80.00 |
0.9560 |
0.9590 |
60.00 |
0.9570 |
0.9610 |
100.00 |
0.9560 |
1.0000 |
60.00 |
1.0000 |
1.0000 |
80.00 |
1.0000 |
1.0000 |
100.00 |
1.0000 |
Mole fraction of Heptane (1)
[ref]
Fixed |
Measured |
Mole fraction of Heptane (1) - Gas |
Pressure, kPa - Liquid |
Mole fraction of Heptane (1) - Liquid |
0.0000 |
60.00 |
0.0000 |
0.0000 |
80.00 |
0.0000 |
0.0000 |
100.00 |
0.0000 |
0.0870 |
80.00 |
0.0090 |
0.0970 |
100.00 |
0.0110 |
0.1430 |
60.00 |
0.0170 |
0.2150 |
100.00 |
0.0230 |
0.2380 |
80.00 |
0.0310 |
0.2790 |
60.00 |
0.0360 |
0.3290 |
100.00 |
0.0420 |
0.3610 |
80.00 |
0.0510 |
0.3990 |
60.00 |
0.0590 |
0.5100 |
80.00 |
0.0860 |
0.5770 |
60.00 |
0.1080 |
0.6050 |
100.00 |
0.1260 |
0.6440 |
80.00 |
0.1330 |
0.7190 |
60.00 |
0.1980 |
0.7330 |
80.00 |
0.1900 |
0.7390 |
100.00 |
0.2210 |
0.7830 |
80.00 |
0.2760 |
0.8180 |
60.00 |
0.3300 |
0.8250 |
100.00 |
0.4430 |
0.8390 |
100.00 |
0.5340 |
0.8510 |
80.00 |
0.4950 |
0.8580 |
60.00 |
0.4650 |
0.8750 |
60.00 |
0.5740 |
0.8870 |
60.00 |
0.6980 |
0.9170 |
80.00 |
0.8880 |
0.9210 |
100.00 |
0.8970 |
0.9240 |
60.00 |
0.9050 |
0.9260 |
80.00 |
0.9020 |
0.9300 |
80.00 |
0.9140 |
0.9310 |
100.00 |
0.9160 |
0.9380 |
100.00 |
0.9290 |
0.9440 |
80.00 |
0.9330 |
0.9580 |
80.00 |
0.9560 |
0.9590 |
60.00 |
0.9570 |
0.9610 |
100.00 |
0.9560 |
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 Heptane (1) - Gas |
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Gas |
0.0000 |
60.00 |
398.12 |
0.0000 |
80.00 |
407.13 |
0.0000 |
100.00 |
414.21 |
0.0870 |
80.00 |
404.40 |
0.0970 |
100.00 |
411.41 |
0.1430 |
60.00 |
393.55 |
0.2150 |
100.00 |
406.53 |
0.2380 |
80.00 |
399.11 |
0.2790 |
60.00 |
389.21 |
0.3290 |
100.00 |
402.25 |
0.3610 |
80.00 |
394.38 |
0.3990 |
60.00 |
384.65 |
0.5100 |
80.00 |
387.13 |
0.5770 |
60.00 |
376.84 |
0.6050 |
100.00 |
388.08 |
0.6440 |
80.00 |
380.24 |
0.7190 |
60.00 |
368.41 |
0.7330 |
80.00 |
375.14 |
0.7390 |
100.00 |
379.87 |
0.7830 |
80.00 |
370.82 |
0.8180 |
60.00 |
360.09 |
0.8250 |
100.00 |
373.51 |
0.8390 |
100.00 |
372.35 |
0.8510 |
80.00 |
365.53 |
0.8580 |
60.00 |
357.72 |
0.8750 |
60.00 |
355.87 |
0.8870 |
60.00 |
355.17 |
0.9170 |
80.00 |
363.57 |
0.9210 |
100.00 |
370.76 |
0.9240 |
60.00 |
354.63 |
0.9260 |
80.00 |
363.51 |
0.9300 |
80.00 |
363.47 |
0.9310 |
100.00 |
370.71 |
0.9380 |
100.00 |
370.63 |
0.9440 |
80.00 |
363.45 |
0.9580 |
80.00 |
363.44 |
0.9590 |
60.00 |
354.48 |
0.9610 |
100.00 |
370.67 |
1.0000 |
60.00 |
354.72 |
1.0000 |
80.00 |
363.74 |
1.0000 |
100.00 |
371.20 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Heptane (1) - Gas |
Pressure, kPa - Gas |
Boiling temperature at pressure P, K - Gas |
0.0000 |
60.00 |
398.12 |
0.0000 |
80.00 |
407.13 |
0.0000 |
100.00 |
414.21 |
0.0870 |
80.00 |
404.40 |
0.0970 |
100.00 |
411.41 |
0.1430 |
60.00 |
393.55 |
0.2150 |
100.00 |
406.53 |
0.2380 |
80.00 |
399.11 |
0.2790 |
60.00 |
389.21 |
0.3290 |
100.00 |
402.25 |
0.3610 |
80.00 |
394.38 |
0.3990 |
60.00 |
384.65 |
0.5100 |
80.00 |
387.13 |
0.5770 |
60.00 |
376.84 |
0.6050 |
100.00 |
388.08 |
0.6440 |
80.00 |
380.24 |
0.7190 |
60.00 |
368.41 |
0.7330 |
80.00 |
375.14 |
0.7390 |
100.00 |
379.87 |
0.7830 |
80.00 |
370.82 |
0.8180 |
60.00 |
360.09 |
0.8250 |
100.00 |
373.51 |
0.8390 |
100.00 |
372.35 |
0.8510 |
80.00 |
365.53 |
0.8580 |
60.00 |
357.72 |
0.8750 |
60.00 |
355.87 |
0.8870 |
60.00 |
355.17 |
0.9170 |
80.00 |
363.57 |
0.9210 |
100.00 |
370.76 |
0.9240 |
60.00 |
354.63 |
0.9260 |
80.00 |
363.51 |
0.9300 |
80.00 |
363.47 |
0.9310 |
100.00 |
370.71 |
0.9380 |
100.00 |
370.63 |
0.9440 |
80.00 |
363.45 |
0.9580 |
80.00 |
363.44 |
0.9590 |
60.00 |
354.48 |
0.9610 |
100.00 |
370.67 |
1.0000 |
60.00 |
354.72 |
1.0000 |
80.00 |
363.74 |
1.0000 |
100.00 |
371.20 |
Sources