Mixture of Phenol, 2-methoxy- + Ethanol

Datasets

1. Activity coefficient
2. Excess molar enthalpy (molar enthalpy
3. T_boil - Boiling temperature at pressure P, K

Activity coefficient of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Activity coefficient of Ethanol (2) - Liquid
298.15	0.1046	1.771
298.15	0.1074	1.755
298.15	0.0974	1.797
298.15	0.1594	1.651
298.15	0.1758	1.617
298.15	0.1854	1.583
298.15	0.2961	1.412
298.15	0.3105	1.394
298.15	0.2387	1.5
298.15	0.4457	1.267
298.15	0.3734	1.335
298.15	0.3887	1.322
298.15	0.4918	1.223
298.15	0.5145	1.202
298.15	0.5214	1.202
298.15	0.6117	1.15
298.15	0.6220	1.146
298.15	0.6456	1.129
298.15	0.7254	1.136
298.15	0.7153	1.16
298.15	0.7149	1.157
298.15	0.8118	1.058
298.15	0.8229	1.077
298.15	0.8203	1.057
298.15	0.9081	0.9810
298.15	0.9103	1.046
298.15	0.9088	1.056
308.15	0.1035	1.691
308.15	0.1046	1.678
308.15	0.1019	1.685
308.15	0.1925	1.523
308.15	0.2082	1.482
308.15	0.2066	1.496
308.15	0.3118	1.344
308.15	0.2940	1.37
308.15	0.4052	1.248
308.15	0.4055	1.253
308.15	0.4145	1.237
308.15	0.5073	1.183
308.15	0.5038	1.18
308.15	0.5160	1.174
308.15	0.6137	1.118
308.15	0.6115	1.121
308.15	0.6057	1.125
308.15	0.7138	1.066
308.15	0.7129	1.078
308.15	0.8092	1.039
308.15	0.8110	1.036
308.15	0.8078	1.038
308.15	0.9048	1.008
308.15	0.9030	1.01
308.15	0.9013	1.007
318.15	0.1037	1.745
318.15	0.1056	1.704
318.15	0.1063	1.701
318.15	0.1841	1.567
318.15	0.1852	1.553
318.15	0.2106	1.525
318.15	0.3131	1.354
318.15	0.2995	1.378
318.15	0.2709	1.428
318.15	0.4169	1.266
318.15	0.4246	1.26
318.15	0.4235	1.263
318.15	0.5108	1.226
318.15	0.5152	1.218
318.15	0.5096	1.225
318.15	0.6111	1.156
318.15	0.6073	1.16
318.15	0.6066	1.163
318.15	0.7125	1.106
318.15	0.7048	1.105
318.15	0.7154	1.103
318.15	0.8081	1.061
318.15	0.8018	1.065
318.15	0.8015	1.041
318.15	0.8975	1.031
318.15	0.8885	1.028

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Phenol, 2-methoxy- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0168	-0.0300
0.1988	-0.3795
0.3994	-0.5491
0.6080	-0.5053
0.7783	-0.2378

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Phenol, 2-methoxy- (1) - Liquid	Boiling temperature at pressure P, K - Liquid
9.00	0.1090	300.25
9.00	0.2190	303.33
9.00	0.3220	304.88
9.00	0.4000	307.11
9.00	0.4910	309.40
9.00	0.5920	312.76
9.00	0.7010	316.55
9.00	0.7730	320.29
9.00	0.8890	332.80
16.40	0.1090	313.11
16.40	0.2190	315.03
16.40	0.3220	317.28
16.40	0.4000	319.36
16.40	0.4910	321.93
16.40	0.5920	325.08
16.40	0.7010	329.79
16.40	0.7730	333.56
16.40	0.8890	347.75
33.30	0.1090	328.13
33.30	0.2190	329.87
33.30	0.3220	332.29
33.30	0.4000	334.17
33.30	0.4910	337.32
33.30	0.5920	340.83
33.30	0.7010	346.20
33.30	0.7730	350.90
33.30	0.8890	368.35
50.00	0.1090	337.36
50.00	0.2190	339.06
50.00	0.3220	341.49
50.00	0.4000	343.46
50.00	0.4910	346.85
50.00	0.5920	350.46
50.00	0.7010	356.72
50.00	0.7730	362.19
50.00	0.8890	381.56
70.00	0.1090	345.35
70.00	0.2190	347.10
70.00	0.3220	349.65
70.00	0.4000	351.60
70.00	0.4910	355.68
70.00	0.5920	359.53
70.00	0.7010	366.51
70.00	0.7730	372.24
70.00	0.8890	394.05
83.20	0.1090	349.63
83.20	0.2190	351.45
83.20	0.3220	354.00
83.20	0.4000	355.80
83.20	0.4910	360.20
83.20	0.5920	364.10
83.20	0.7010	371.89
83.20	0.7730	377.68
83.20	0.8890	400.47
99.60	0.1090	354.12
96.10	0.2190	354.92
99.20	0.3220	358.70
97.70	0.4000	359.87
99.00	0.4910	365.43
97.10	0.5920	368.80
99.70	0.7010	377.89
99.00	0.7730	383.82
96.50	0.8890	409.48

Sources

• Phase equilibria of phenolic compounds in water or ethanol
• Guaiacol and its mixtures: new data and predictive models Part 2: Gibbs energy of solvation

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