Mixture of p-Xylene + Ethanol

Datasets

1. Mole fraction
2. T_boil - Boiling temperature at pressure P, K (2)
3. Vapor Liquid Equilibrium at Constant Pressure (2)
4. Vapor Liquid Equilibrium at Constant Temperature

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
0.0080	0.1890
0.0310	0.4790
0.0820	0.7340
0.1230	0.7950
0.1960	0.8350
0.2550	0.8470
0.3130	0.8570
0.3490	0.8630
0.3970	0.8750
0.4640	0.8810
0.4880	0.8830
0.5530	0.8870
0.6000	0.8930
0.6500	0.8980
0.7060	0.9020
0.7500	0.9060
0.8020	0.9150
0.8500	0.9270
0.8960	0.9400
0.9490	0.9620
0.9790	0.9820

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0080	404.93
0.0310	391.42
0.0820	372.38
0.1230	366.03
0.1960	361.22
0.2550	359.31
0.3130	358.12
0.3490	357.30
0.3970	356.39
0.4640	355.72
0.4880	355.34
0.5530	354.74
0.6000	354.28
0.6500	353.89
0.7060	353.45
0.7500	353.09
0.8020	352.70
0.8500	352.32
0.8960	351.99
0.9490	351.63
0.9790	351.48

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
40.00	0.0000	379.81
40.00	0.1000	339.47
40.00	0.2000	335.39
40.00	0.3007	334.54
40.00	0.4000	333.19
40.00	0.4997	332.04
40.00	0.6000	331.51
40.00	0.7000	330.87
40.00	0.7999	330.53
40.00	0.9000	329.95
40.00	1.0000	329.69
53.33	0.0000	388.96
53.33	0.1000	347.29
53.33	0.1501	344.42
53.33	0.2000	342.87
53.33	0.2499	342.41
53.33	0.3007	341.67
53.33	0.4000	340.31
53.33	0.4997	338.65
53.33	0.6000	338.15
53.33	0.7000	337.48
53.33	0.7999	337.06
53.33	0.9000	336.39
53.33	1.0000	336.07
66.66	0.0000	396.45
66.66	0.1000	353.52
66.66	0.1501	350.52
66.66	0.2000	349.05
66.66	0.3007	347.09
66.66	0.4000	345.78
66.66	0.4997	344.14
66.66	0.6000	343.57
66.66	0.7000	342.89
66.66	0.7999	342.31
66.66	0.9000	341.62
66.66	1.0000	341.23
79.99	0.0000	402.82
79.99	0.1000	359.33
79.99	0.1501	355.63
79.99	0.2000	354.37
79.99	0.2499	353.17
79.99	0.3007	351.39
79.99	0.4000	350.32
79.99	0.4997	348.85
79.99	0.6000	348.18
79.99	0.7000	347.45
79.99	0.7999	346.75
79.99	0.9000	346.03
79.99	1.0000	345.60
93.32	0.0000	408.40
93.32	0.1000	364.14
93.32	0.1501	359.98
93.32	0.2000	359.14
93.32	0.3007	355.86
93.32	0.4000	354.43
93.32	0.4997	352.97
93.32	0.6000	352.21
93.32	0.7000	351.41
93.32	0.7999	350.63
93.32	0.9000	349.87
93.32	1.0000	349.39
101.30	0.0000	411.48
101.30	0.1000	369.38
101.30	0.2000	361.88
101.30	0.2499	359.43
101.30	0.3000	358.12
101.30	0.4000	355.90
101.30	0.4999	355.45
101.30	0.6000	353.98
101.30	0.7000	353.46
101.30	0.8000	352.65
101.30	0.9000	351.90
101.30	1.0000	351.44

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Ethanol (2) - Liquid	y1[mol/mol] of Ethanol (2) - Vapour
411.55	0.0000	0.0000
389.45	0.0300	0.6500
370.75	0.0850	0.8150
363.55	0.1450	0.8400
360.25	0.1800	0.8700
357.15	0.3350	0.8900
355.55	0.4450	0.8950
354.25	0.6200	0.9100
353.35	0.7250	0.9100
352.85	0.7880	0.9150
352.65	0.8250	0.9250
352.25	0.8600	0.9300
352.05	0.8900	0.9350
351.95	0.9300	0.9500
351.85	0.9500	0.9620
351.75	0.9650	0.9700
351.55	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Ethanol (2) - Liquid	y1[mol/mol] of Ethanol (2) - Vapour
411.52	0.0000	0.0000
373.82	0.0570	0.6710
365.04	0.1200	0.7700
359.44	0.2110	0.8250
357.26	0.3060	0.8410
353.52	0.6680	0.8810
352.67	0.7800	0.8980
352.08	0.8610	0.9190
351.72	0.9140	0.9400
351.59	0.9420	0.9550
351.49	0.9680	0.9730
351.46	0.9860	0.9870
351.45	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

P [kPa] - VLE	x1[mol/mol] of Ethanol (2) - Liquid
4.446	0.0036
4.954	0.0054
5.464	0.0074
5.926	0.0092
7.125	0.0143
7.614	0.0166
8.518	0.0210
10.061	0.0299
11.284	0.0386
12.28	0.0474
13.527	0.0615
14.459	0.0754
15.164	0.0886
15.74	0.1017
16.216	0.1144
16.944	0.1387
17.5	0.1620
17.932	0.1838
18.428	0.2147
18.904	0.2522
19.262	0.2863
19.542	0.3174

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol, Methylcyclohexane and p-Xylene
• Ebulliometric Determination and Prediction of Vapor Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate

Note: These property values are available through the Cheméo API. A free account gives you an access key.