Mixture of Phenol, 2-methoxy- + Ethanol

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Phenol, 2-methoxy-

Name
Phenol, 2-methoxy-
InChI
InChI=1S/C7H8O2/c1-9-7-5-3-2-4-6(7)8/h2-5,8H,1H3
InChI Key
LHGVFZTZFXWLCP-UHFFFAOYSA-N
Formula
C7H8O2
SMILES
COc1ccccc1O
Mol. Weight (g/mol)
124.14
CAS
90-05-1

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5
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Datasets

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

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

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:

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

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

Operational conditions:

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

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