Mixture of Ethanol + Phenol
Datasets
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Tboil - Boiling temperature at pressure P, K (2)
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Binary diffusion coefficient, m2/s (2)
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Phenol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
9.00 |
0.1000 |
303.09 |
9.00 |
0.1980 |
305.10 |
9.00 |
0.3000 |
310.04 |
9.00 |
0.4000 |
313.16 |
9.00 |
0.4950 |
319.73 |
9.00 |
0.5880 |
325.77 |
9.00 |
0.6920 |
333.65 |
9.00 |
0.7940 |
342.26 |
9.00 |
0.8830 |
353.85 |
15.00 |
0.1000 |
312.58 |
15.00 |
0.1980 |
315.16 |
15.00 |
0.3000 |
319.57 |
15.00 |
0.4000 |
323.66 |
15.00 |
0.4950 |
330.26 |
15.00 |
0.5880 |
337.31 |
15.00 |
0.6920 |
345.08 |
15.00 |
0.7940 |
355.05 |
15.00 |
0.8830 |
366.57 |
33.00 |
0.1000 |
328.70 |
33.00 |
0.1980 |
331.35 |
33.00 |
0.3000 |
336.15 |
33.00 |
0.4000 |
339.90 |
33.00 |
0.4950 |
347.78 |
33.00 |
0.5880 |
355.56 |
33.00 |
0.6920 |
364.32 |
33.00 |
0.7940 |
376.11 |
33.00 |
0.8830 |
388.50 |
55.00 |
0.1000 |
340.09 |
55.00 |
0.1980 |
342.95 |
55.00 |
0.3000 |
348.05 |
55.00 |
0.4000 |
352.38 |
55.00 |
0.4950 |
360.94 |
55.00 |
0.5880 |
369.17 |
55.00 |
0.6920 |
378.58 |
55.00 |
0.7940 |
389.90 |
75.00 |
0.1000 |
347.53 |
75.00 |
0.1980 |
350.61 |
75.00 |
0.3000 |
355.78 |
75.00 |
0.4000 |
360.18 |
75.00 |
0.4950 |
369.28 |
75.00 |
0.5880 |
378.05 |
75.00 |
0.6920 |
387.67 |
85.10 |
0.1000 |
350.58 |
85.10 |
0.1980 |
353.70 |
85.10 |
0.3000 |
359.06 |
85.10 |
0.4000 |
363.56 |
85.10 |
0.4950 |
373.06 |
85.10 |
0.5880 |
381.78 |
98.60 |
0.1000 |
354.51 |
98.60 |
0.1980 |
357.65 |
98.60 |
0.3000 |
362.97 |
98.60 |
0.4000 |
367.75 |
98.60 |
0.4950 |
376.85 |
98.60 |
0.5880 |
386.30 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Phenol (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
9.00 |
0.1000 |
303.09 |
9.00 |
0.1980 |
305.10 |
9.00 |
0.3000 |
310.04 |
9.00 |
0.4000 |
313.16 |
9.00 |
0.4950 |
319.73 |
9.00 |
0.5880 |
325.77 |
9.00 |
0.6920 |
333.65 |
9.00 |
0.7940 |
342.26 |
9.00 |
0.8830 |
353.85 |
15.00 |
0.1000 |
312.58 |
15.00 |
0.1980 |
315.16 |
15.00 |
0.3000 |
319.57 |
15.00 |
0.4000 |
323.66 |
15.00 |
0.4950 |
330.26 |
15.00 |
0.5880 |
337.31 |
15.00 |
0.6920 |
345.08 |
15.00 |
0.7940 |
355.05 |
15.00 |
0.8830 |
366.57 |
33.00 |
0.1000 |
328.70 |
33.00 |
0.1980 |
331.35 |
33.00 |
0.3000 |
336.15 |
33.00 |
0.4000 |
339.90 |
33.00 |
0.4950 |
347.78 |
33.00 |
0.5880 |
355.56 |
33.00 |
0.6920 |
364.32 |
33.00 |
0.7940 |
376.11 |
33.00 |
0.8830 |
388.50 |
55.00 |
0.1000 |
340.09 |
55.00 |
0.1980 |
342.95 |
55.00 |
0.3000 |
348.05 |
55.00 |
0.4000 |
352.38 |
55.00 |
0.4950 |
360.94 |
55.00 |
0.5880 |
369.17 |
55.00 |
0.6920 |
378.58 |
55.00 |
0.7940 |
389.90 |
75.00 |
0.1000 |
347.53 |
75.00 |
0.1980 |
350.61 |
75.00 |
0.3000 |
355.78 |
75.00 |
0.4000 |
360.18 |
75.00 |
0.4950 |
369.28 |
75.00 |
0.5880 |
378.05 |
75.00 |
0.6920 |
387.67 |
85.10 |
0.1000 |
350.58 |
85.10 |
0.1980 |
353.70 |
85.10 |
0.3000 |
359.06 |
85.10 |
0.4000 |
363.56 |
85.10 |
0.4950 |
373.06 |
85.10 |
0.5880 |
381.78 |
98.60 |
0.1000 |
354.51 |
98.60 |
0.1980 |
357.65 |
98.60 |
0.3000 |
362.97 |
98.60 |
0.4000 |
367.75 |
98.60 |
0.4950 |
376.85 |
98.60 |
0.5880 |
386.30 |
Binary diffusion coefficient, m2/s
[ref]
Fixed |
Measured |
Mole fraction of Phenol (2) - Liquid |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
0.0000 |
101.00 |
298.15 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Fixed |
Measured |
Mole fraction of Phenol (2) - Liquid |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
0.0000 |
101.00 |
298.15 |
0.0000 |
Sources