Datasets
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Mole fraction (4)
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γ - Surface tension liquid-gas, N/m (2)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Azeotropic temperature, K (2)
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0470 |
50.00 |
0.3070 |
0.0910 |
50.00 |
0.4030 |
0.1390 |
50.00 |
0.4570 |
0.1790 |
50.00 |
0.4870 |
0.2160 |
50.00 |
0.4980 |
0.2760 |
50.00 |
0.5190 |
0.3190 |
50.00 |
0.5250 |
0.3740 |
50.00 |
0.5410 |
0.4240 |
50.00 |
0.5470 |
0.4780 |
50.00 |
0.5570 |
0.5360 |
50.00 |
0.5720 |
0.5890 |
50.00 |
0.5830 |
0.6430 |
50.00 |
0.6000 |
0.6920 |
50.00 |
0.6180 |
0.7380 |
50.00 |
0.6390 |
0.7870 |
50.00 |
0.6680 |
0.8380 |
50.00 |
0.7070 |
0.8920 |
50.00 |
0.7650 |
0.9430 |
50.00 |
0.8410 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
75.00 |
0.0000 |
0.0460 |
75.00 |
0.2980 |
0.0900 |
75.00 |
0.3970 |
0.1320 |
75.00 |
0.4580 |
0.1700 |
75.00 |
0.4820 |
0.2130 |
75.00 |
0.5100 |
0.2680 |
75.00 |
0.5280 |
0.3120 |
75.00 |
0.5370 |
0.3760 |
75.00 |
0.5640 |
0.4210 |
75.00 |
0.5680 |
0.4780 |
75.00 |
0.5760 |
0.5340 |
75.00 |
0.5900 |
0.5880 |
75.00 |
0.6030 |
0.6410 |
75.00 |
0.6210 |
0.6930 |
75.00 |
0.6390 |
0.7390 |
75.00 |
0.6600 |
0.7880 |
75.00 |
0.6880 |
0.8400 |
75.00 |
0.7270 |
0.8910 |
75.00 |
0.7800 |
0.9440 |
75.00 |
0.8560 |
1.0000 |
75.00 |
1.0000 |
0.0000 |
94.00 |
0.0000 |
0.0470 |
94.00 |
0.2740 |
0.0850 |
94.00 |
0.3950 |
0.1280 |
94.00 |
0.4510 |
0.1690 |
94.00 |
0.4840 |
0.2110 |
94.00 |
0.5150 |
0.2610 |
94.00 |
0.5360 |
0.3090 |
94.00 |
0.5490 |
0.3670 |
94.00 |
0.5650 |
0.4190 |
94.00 |
0.5760 |
0.4740 |
94.00 |
0.5890 |
0.5330 |
94.00 |
0.6000 |
0.5890 |
94.00 |
0.6150 |
0.6430 |
94.00 |
0.6320 |
0.6920 |
94.00 |
0.6500 |
0.7370 |
94.00 |
0.6720 |
0.7870 |
94.00 |
0.6990 |
0.8510 |
94.00 |
0.7430 |
0.8930 |
94.00 |
0.7880 |
0.9430 |
94.00 |
0.8620 |
1.0000 |
94.00 |
1.0000 |
Azeotropic composition: mole fraction of Ethanol (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Ethanol (1) - Liquid |
50.00 |
0.5770 |
75.00 |
0.6110 |
94.00 |
0.6270 |
Mole fraction of Ethanol (1)
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethanol (1) - Gas |
0.0000 |
50.00 |
0.0000 |
0.0470 |
50.00 |
0.3070 |
0.0910 |
50.00 |
0.4030 |
0.1390 |
50.00 |
0.4570 |
0.1790 |
50.00 |
0.4870 |
0.2160 |
50.00 |
0.4980 |
0.2760 |
50.00 |
0.5190 |
0.3190 |
50.00 |
0.5250 |
0.3740 |
50.00 |
0.5410 |
0.4240 |
50.00 |
0.5470 |
0.4780 |
50.00 |
0.5570 |
0.5360 |
50.00 |
0.5720 |
0.5890 |
50.00 |
0.5830 |
0.6430 |
50.00 |
0.6000 |
0.6920 |
50.00 |
0.6180 |
0.7380 |
50.00 |
0.6390 |
0.7870 |
50.00 |
0.6680 |
0.8380 |
50.00 |
0.7070 |
0.8920 |
50.00 |
0.7650 |
0.9430 |
50.00 |
0.8410 |
1.0000 |
50.00 |
1.0000 |
0.0000 |
75.00 |
0.0000 |
0.0460 |
75.00 |
0.2980 |
0.0900 |
75.00 |
0.3970 |
0.1320 |
75.00 |
0.4580 |
0.1700 |
75.00 |
0.4820 |
0.2130 |
75.00 |
0.5100 |
0.2680 |
75.00 |
0.5280 |
0.3120 |
75.00 |
0.5370 |
0.3760 |
75.00 |
0.5640 |
0.4210 |
75.00 |
0.5680 |
0.4780 |
75.00 |
0.5760 |
0.5340 |
75.00 |
0.5900 |
0.5880 |
75.00 |
0.6030 |
0.6410 |
75.00 |
0.6210 |
0.6930 |
75.00 |
0.6390 |
0.7390 |
75.00 |
0.6600 |
0.7880 |
75.00 |
0.6880 |
0.8400 |
75.00 |
0.7270 |
0.8910 |
75.00 |
0.7800 |
0.9440 |
75.00 |
0.8560 |
1.0000 |
75.00 |
1.0000 |
0.0000 |
94.00 |
0.0000 |
0.0470 |
94.00 |
0.2740 |
0.0850 |
94.00 |
0.3950 |
0.1280 |
94.00 |
0.4510 |
0.1690 |
94.00 |
0.4840 |
0.2110 |
94.00 |
0.5150 |
0.2610 |
94.00 |
0.5360 |
0.3090 |
94.00 |
0.5490 |
0.3670 |
94.00 |
0.5650 |
0.4190 |
94.00 |
0.5760 |
0.4740 |
94.00 |
0.5890 |
0.5330 |
94.00 |
0.6000 |
0.5890 |
94.00 |
0.6150 |
0.6430 |
94.00 |
0.6320 |
0.6920 |
94.00 |
0.6500 |
0.7370 |
94.00 |
0.6720 |
0.7870 |
94.00 |
0.6990 |
0.8510 |
94.00 |
0.7430 |
0.8930 |
94.00 |
0.7880 |
0.9430 |
94.00 |
0.8620 |
1.0000 |
94.00 |
1.0000 |
Azeotropic composition: mole fraction of Ethanol (1)
[ref]
Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of Ethanol (1) - Liquid |
50.00 |
0.5770 |
75.00 |
0.6110 |
94.00 |
0.6270 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0000 |
0.0251 |
0.0490 |
0.0250 |
0.0900 |
0.0249 |
0.1760 |
0.0247 |
0.2900 |
0.0244 |
0.3860 |
0.0242 |
0.4920 |
0.0239 |
0.5940 |
0.0237 |
0.7010 |
0.0234 |
0.8040 |
0.0230 |
0.9150 |
0.0227 |
0.9630 |
0.0225 |
1.0000 |
0.0221 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Ethanol (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0000 |
0.0251 |
0.0490 |
0.0250 |
0.0900 |
0.0249 |
0.1760 |
0.0247 |
0.2900 |
0.0244 |
0.3860 |
0.0242 |
0.4920 |
0.0239 |
0.5940 |
0.0237 |
0.7010 |
0.0234 |
0.8040 |
0.0230 |
0.9150 |
0.0227 |
0.9630 |
0.0225 |
1.0000 |
0.0221 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
50.00 |
345.20 |
0.0470 |
50.00 |
336.70 |
0.0910 |
50.00 |
333.33 |
0.1390 |
50.00 |
331.56 |
0.1790 |
50.00 |
330.69 |
0.2160 |
50.00 |
330.09 |
0.2760 |
50.00 |
329.55 |
0.3190 |
50.00 |
329.20 |
0.3740 |
50.00 |
328.79 |
0.4240 |
50.00 |
328.64 |
0.4780 |
50.00 |
328.61 |
0.5360 |
50.00 |
328.60 |
0.5890 |
50.00 |
328.61 |
0.6430 |
50.00 |
328.69 |
0.6920 |
50.00 |
328.72 |
0.7380 |
50.00 |
328.96 |
0.7870 |
50.00 |
329.24 |
0.8380 |
50.00 |
329.57 |
0.8920 |
50.00 |
330.47 |
0.9430 |
50.00 |
331.44 |
1.0000 |
50.00 |
334.57 |
0.0000 |
75.00 |
357.18 |
0.0460 |
75.00 |
348.48 |
0.0900 |
75.00 |
344.61 |
0.1320 |
75.00 |
342.55 |
0.1700 |
75.00 |
341.46 |
0.2130 |
75.00 |
340.58 |
0.2680 |
75.00 |
339.86 |
0.3120 |
75.00 |
339.39 |
0.3760 |
75.00 |
338.67 |
0.4210 |
75.00 |
338.64 |
0.4780 |
75.00 |
338.54 |
0.5340 |
75.00 |
338.49 |
0.5880 |
75.00 |
338.50 |
0.6410 |
75.00 |
338.53 |
0.6930 |
75.00 |
338.59 |
0.7390 |
75.00 |
338.74 |
0.7880 |
75.00 |
338.99 |
0.8400 |
75.00 |
339.36 |
0.8910 |
75.00 |
340.39 |
0.9440 |
75.00 |
341.40 |
1.0000 |
75.00 |
344.02 |
0.0000 |
94.00 |
364.36 |
0.0470 |
94.00 |
355.62 |
0.0850 |
94.00 |
351.43 |
0.1280 |
94.00 |
349.15 |
0.1690 |
94.00 |
347.85 |
0.2110 |
94.00 |
346.78 |
0.2610 |
94.00 |
345.94 |
0.3090 |
94.00 |
345.42 |
0.3670 |
94.00 |
344.89 |
0.4190 |
94.00 |
344.63 |
0.4740 |
94.00 |
344.41 |
0.5330 |
94.00 |
344.32 |
0.5890 |
94.00 |
344.31 |
0.6430 |
94.00 |
344.34 |
0.6920 |
94.00 |
344.42 |
0.7370 |
94.00 |
344.54 |
0.7870 |
94.00 |
344.69 |
0.8510 |
94.00 |
345.17 |
0.8930 |
94.00 |
345.98 |
0.9430 |
94.00 |
347.09 |
1.0000 |
94.00 |
349.56 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of Ethanol (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
50.00 |
345.20 |
0.0470 |
50.00 |
336.70 |
0.0910 |
50.00 |
333.33 |
0.1390 |
50.00 |
331.56 |
0.1790 |
50.00 |
330.69 |
0.2160 |
50.00 |
330.09 |
0.2760 |
50.00 |
329.55 |
0.3190 |
50.00 |
329.20 |
0.3740 |
50.00 |
328.79 |
0.4240 |
50.00 |
328.64 |
0.4780 |
50.00 |
328.61 |
0.5360 |
50.00 |
328.60 |
0.5890 |
50.00 |
328.61 |
0.6430 |
50.00 |
328.69 |
0.6920 |
50.00 |
328.72 |
0.7380 |
50.00 |
328.96 |
0.7870 |
50.00 |
329.24 |
0.8380 |
50.00 |
329.57 |
0.8920 |
50.00 |
330.47 |
0.9430 |
50.00 |
331.44 |
1.0000 |
50.00 |
334.57 |
0.0000 |
75.00 |
357.18 |
0.0460 |
75.00 |
348.48 |
0.0900 |
75.00 |
344.61 |
0.1320 |
75.00 |
342.55 |
0.1700 |
75.00 |
341.46 |
0.2130 |
75.00 |
340.58 |
0.2680 |
75.00 |
339.86 |
0.3120 |
75.00 |
339.39 |
0.3760 |
75.00 |
338.67 |
0.4210 |
75.00 |
338.64 |
0.4780 |
75.00 |
338.54 |
0.5340 |
75.00 |
338.49 |
0.5880 |
75.00 |
338.50 |
0.6410 |
75.00 |
338.53 |
0.6930 |
75.00 |
338.59 |
0.7390 |
75.00 |
338.74 |
0.7880 |
75.00 |
338.99 |
0.8400 |
75.00 |
339.36 |
0.8910 |
75.00 |
340.39 |
0.9440 |
75.00 |
341.40 |
1.0000 |
75.00 |
344.02 |
0.0000 |
94.00 |
364.36 |
0.0470 |
94.00 |
355.62 |
0.0850 |
94.00 |
351.43 |
0.1280 |
94.00 |
349.15 |
0.1690 |
94.00 |
347.85 |
0.2110 |
94.00 |
346.78 |
0.2610 |
94.00 |
345.94 |
0.3090 |
94.00 |
345.42 |
0.3670 |
94.00 |
344.89 |
0.4190 |
94.00 |
344.63 |
0.4740 |
94.00 |
344.41 |
0.5330 |
94.00 |
344.32 |
0.5890 |
94.00 |
344.31 |
0.6430 |
94.00 |
344.34 |
0.6920 |
94.00 |
344.42 |
0.7370 |
94.00 |
344.54 |
0.7870 |
94.00 |
344.69 |
0.8510 |
94.00 |
345.17 |
0.8930 |
94.00 |
345.98 |
0.9430 |
94.00 |
347.09 |
1.0000 |
94.00 |
349.56 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
50.00 |
328.61 |
75.00 |
338.51 |
94.00 |
344.32 |
Azeotropic temperature, K
[ref]
Pressure, kPa - Liquid |
Azeotropic temperature, K - Liquid |
50.00 |
328.61 |
75.00 |
338.51 |
94.00 |
344.32 |
Sources