Mixture of Phenol, 2-methyl- + Octane + Water

Excel

Phenol, 2-methyl-

Name
Phenol, 2-methyl-
InChI
InChI=1S/C7H8O/c1-6-4-2-3-5-7(6)8/h2-5,8H,1H3
InChI Key
QWVGKYWNOKOFNN-UHFFFAOYSA-N
Formula
C7H8O
SMILES
Cc1ccccc1O
Mol. Weight (g/mol)
108.14
CAS
95-48-7

Octane

Name
Octane
InChI
InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3
InChI Key
TVMXDCGIABBOFY-UHFFFAOYSA-N
Formula
C8H18
SMILES
CCCCCCCC
Mol. Weight (g/mol)
114.23
CAS
111-65-9

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. Mole fraction (20)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. ρl - Mass density, kg/m3 (2)

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
289.15 0.0593
323.15 0.1562

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
289.15 0.5170
323.15 0.5187

Mole fraction of Octane (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Octane (2) - Liquid mixture 1
289.15 0.9110
323.15 0.7566

Mole fraction of Octane (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Octane (2) - Liquid mixture 2
289.15 0.0707
323.15 0.1109

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Octane (2) - Liquid mixture 1 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
298.15 0.0000 0.5093
298.15 0.0142 0.5290
298.15 0.0334 0.5400
298.15 0.0409 0.5530
298.15 0.0593 0.5410
298.15 0.0634 0.5420
298.15 0.0907 0.5390
298.15 0.1020 0.5550
298.15 0.1080 0.5570
298.15 0.1230 0.5700
298.15 0.1260 0.5730
298.15 0.1360 0.5780
298.15 0.1370 0.5820
298.15 0.1490 0.5820
298.15 0.1530 0.5840
298.15 0.2220 0.5900
298.15 0.2680 0.5560
298.15 0.3260 0.5230
298.15 0.3790 0.4860
298.15 0.3820 0.4930
298.15 0.4350 0.4490
298.15 0.4650 0.4390
298.15 0.6200 0.3090
298.15 0.7290 0.2250
323.15 0.0000 0.4917
323.15 0.0119 0.5092
323.15 0.1128 0.5279
323.15 0.1299 0.5179
323.15 0.1709 0.5126
323.15 0.2428 0.4928
323.15 0.2514 0.4878
323.15 0.2987 0.4666
323.15 0.4283 0.4011
323.15 0.5282 0.3400

Mole fraction of Phenol, 2-methyl- (1) [ref]

Fixed Measured
Temperature, K - Liquid mixture 1 Pressure, kPa - Liquid mixture 1 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
333.15 22.50 0.4903
333.15 24.87 0.5202
333.15 27.18 0.4212
333.15 27.90 0.4372
333.15 28.56 0.4308
333.15 28.98 0.4977
353.15 60.24 0.4636
353.15 63.25 0.3275
353.15 65.29 0.3617
353.15 66.21 0.3956
353.15 66.75 0.4834
353.15 67.53 0.4834

Mole fraction of Phenol, 2-methyl- (1) [ref]

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Mole fraction of Phenol, 2-methyl- (1) - Gas
333.15 22.50 0.0155
333.15 24.87 0.0161
333.15 27.18 0.0175
333.15 27.90 0.0169
333.15 28.56 0.0175
333.15 28.98 0.0159
353.15 60.24 0.0205
353.15 63.25 0.0199
353.15 65.29 0.0115
353.15 66.21 0.0187
353.15 66.75 0.0186
353.15 67.53 0.0180

Mole fraction of Octane (2) [ref]

Fixed Measured
Temperature, K - Liquid mixture 1 Pressure, kPa - Liquid mixture 1 Mole fraction of Octane (2) - Liquid mixture 1
333.15 22.50 0.0291
333.15 24.87 0.0357
333.15 27.18 0.0394
333.15 27.90 0.0545
333.15 28.56 0.0671
333.15 28.98 0.0929
353.15 60.24 0.0337
353.15 63.25 0.0385
353.15 65.29 0.0524
353.15 66.21 0.0661
353.15 66.75 0.0822
353.15 67.53 0.1000

Mole fraction of Octane (2) [ref]

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Mole fraction of Octane (2) - Gas
333.15 22.50 0.2338
333.15 24.87 0.2332
333.15 27.18 0.2613
333.15 27.90 0.2746
333.15 28.56 0.3065
333.15 28.98 0.2885
353.15 60.24 0.1992
353.15 63.25 0.2336
353.15 65.29 0.2560
353.15 66.21 0.2617
353.15 66.75 0.2635
353.15 67.53 0.2780

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Octane (2) - Gas Mole fraction of Phenol, 2-methyl- (1) - Gas Mole fraction of Octane (2) - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid
333.15 13.78 0.3763 0.0222 0.0671 0.7806
333.15 14.97 0.2171 0.0320 0.0393 0.7460
333.15 15.05 0.1958 0.0426 0.0341 0.7382
333.15 18.88 0.1572 0.0286 0.0324 0.7354
333.15 20.09 0.1546 0.0235 0.0225 0.6342
333.15 21.31 0.2305 0.0255 0.0330 0.6210
333.15 23.80 0.2078 0.0153 0.0344 0.5581
353.15 48.05 0.1591 0.0197 0.0291 0.6170
353.15 52.66 0.1805 0.0163 0.0330 0.5720
353.15 56.61 0.1874 0.0131 0.0338 0.5232

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
289.15 0.0593
323.15 0.1562

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
289.15 0.5170
323.15 0.5187

Mole fraction of Octane (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1 Mole fraction of Octane (2) - Liquid mixture 1
289.15 0.9110
323.15 0.7566

Mole fraction of Octane (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2 Mole fraction of Octane (2) - Liquid mixture 2
289.15 0.0707
323.15 0.1109

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Octane (2) - Liquid mixture 1 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
298.15 0.0000 0.5093
298.15 0.0142 0.5290
298.15 0.0334 0.5400
298.15 0.0409 0.5530
298.15 0.0593 0.5410
298.15 0.0634 0.5420
298.15 0.0907 0.5390
298.15 0.1020 0.5550
298.15 0.1080 0.5570
298.15 0.1230 0.5700
298.15 0.1260 0.5730
298.15 0.1360 0.5780
298.15 0.1370 0.5820
298.15 0.1490 0.5820
298.15 0.1530 0.5840
298.15 0.2220 0.5900
298.15 0.2680 0.5560
298.15 0.3260 0.5230
298.15 0.3790 0.4860
298.15 0.3820 0.4930
298.15 0.4350 0.4490
298.15 0.4650 0.4390
298.15 0.6200 0.3090
298.15 0.7290 0.2250
323.15 0.0000 0.4917
323.15 0.0119 0.5092
323.15 0.1128 0.5279
323.15 0.1299 0.5179
323.15 0.1709 0.5126
323.15 0.2428 0.4928
323.15 0.2514 0.4878
323.15 0.2987 0.4666
323.15 0.4283 0.4011
323.15 0.5282 0.3400

Mole fraction of Phenol, 2-methyl- (1) [ref]

Fixed Measured
Temperature, K - Liquid mixture 1 Pressure, kPa - Liquid mixture 1 Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
333.15 22.50 0.4903
333.15 24.87 0.5202
333.15 27.18 0.4212
333.15 27.90 0.4372
333.15 28.56 0.4308
333.15 28.98 0.4977
353.15 60.24 0.4636
353.15 63.25 0.3275
353.15 65.29 0.3617
353.15 66.21 0.3956
353.15 66.75 0.4834
353.15 67.53 0.4834

Mole fraction of Phenol, 2-methyl- (1) [ref]

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Mole fraction of Phenol, 2-methyl- (1) - Gas
333.15 22.50 0.0155
333.15 24.87 0.0161
333.15 27.18 0.0175
333.15 27.90 0.0169
333.15 28.56 0.0175
333.15 28.98 0.0159
353.15 60.24 0.0205
353.15 63.25 0.0199
353.15 65.29 0.0115
353.15 66.21 0.0187
353.15 66.75 0.0186
353.15 67.53 0.0180

Mole fraction of Octane (2) [ref]

Fixed Measured
Temperature, K - Liquid mixture 1 Pressure, kPa - Liquid mixture 1 Mole fraction of Octane (2) - Liquid mixture 1
333.15 22.50 0.0291
333.15 24.87 0.0357
333.15 27.18 0.0394
333.15 27.90 0.0545
333.15 28.56 0.0671
333.15 28.98 0.0929
353.15 60.24 0.0337
353.15 63.25 0.0385
353.15 65.29 0.0524
353.15 66.21 0.0661
353.15 66.75 0.0822
353.15 67.53 0.1000

Mole fraction of Octane (2) [ref]

Fixed Measured
Temperature, K - Gas Pressure, kPa - Gas Mole fraction of Octane (2) - Gas
333.15 22.50 0.2338
333.15 24.87 0.2332
333.15 27.18 0.2613
333.15 27.90 0.2746
333.15 28.56 0.3065
333.15 28.98 0.2885
353.15 60.24 0.1992
353.15 63.25 0.2336
353.15 65.29 0.2560
353.15 66.21 0.2617
353.15 66.75 0.2635
353.15 67.53 0.2780

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Octane (2) - Gas Mole fraction of Phenol, 2-methyl- (1) - Gas Mole fraction of Octane (2) - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid
333.15 13.78 0.3763 0.0222 0.0671 0.7806
333.15 14.97 0.2171 0.0320 0.0393 0.7460
333.15 15.05 0.1958 0.0426 0.0341 0.7382
333.15 18.88 0.1572 0.0286 0.0324 0.7354
333.15 20.09 0.1546 0.0235 0.0225 0.6342
333.15 21.31 0.2305 0.0255 0.0330 0.6210
333.15 23.80 0.2078 0.0153 0.0344 0.5581
353.15 48.05 0.1591 0.0197 0.0291 0.6170
353.15 52.66 0.1805 0.0163 0.0330 0.5720
353.15 56.61 0.1874 0.0131 0.0338 0.5232

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 353.15 (Liquid)

Fixed Measured
Mole fraction of Octane (2) - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0161 0.7187 38.91
0.0170 0.6699 42.74

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 353.15 (Liquid)

Fixed Measured
Mole fraction of Octane (2) - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0161 0.7187 38.91
0.0170 0.6699 42.74

Mass density, kg/m3 [ref]

Operational conditions:

Fixed Measured
Mole fraction of Octane (2) - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 0.8184 1035.9
0.0000 0.8443 1036.16
0.0000 0.8903 1036.47
0.0000 0.9409 1036.95
0.0000 1.0000 1036.94
0.0424 0.8084 1011.69
0.0500 0.8939 1010.32
0.0518 0.8442 1007.87
0.0621 0.7675 999.87
0.0741 0.8712 998.07
0.0779 0.9221 998.31
0.0788 0.7778 991.93
0.1358 0.7693 964.99
0.1372 0.7061 959.96
0.1580 0.7108 951.38
0.1603 0.7901 956.44
0.1634 0.8366 958.43
0.1819 0.6695 938.15
0.1955 0.7162 936.96
0.2128 0.6646 925.62
0.2270 0.7273 926.72
0.2381 0.6783 917.98
0.2569 0.7431 918.23
0.2618 0.6041 902.27
0.2758 0.6447 902.28
0.2898 0.6682 900.46
0.2990 0.7010 901.26
0.3165 0.5593 879.7
0.3212 0.5731 880.01
0.3399 0.6211 880.83
0.3533 0.5758 871.64
0.3600 0.6400 877.71
0.3779 0.5091 856.4
0.3924 0.5130 853.33
0.4206 0.4741 841.23
0.4226 0.5433 850.56
0.4277 0.5723 853.18
0.4328 0.5050 843.04
0.4565 0.4588 831.2
0.4642 0.5041 836.2
0.4784 0.4269 821.81
0.4797 0.5203 835.08
0.4986 0.4233 817.45
0.5188 0.4284 814.49
0.5668 0.3657 796.64
0.5694 0.3524 794.07
0.5787 0.4213 803.61
0.5821 0.3720 795.24
0.5968 0.3404 787.93
0.5996 0.3768 793.48
0.6279 0.3045 777.63
0.6512 0.3106 775.12
0.6607 0.3393 779.19
0.6913 0.2607 762.39
0.6933 0.2886 767.12
0.7003 0.2453 758.56
0.7217 0.2477 756.84
0.7559 0.2297 750.39
0.7569 0.2052 745.94
0.7664 0.2336 750.13
0.8006 0.1776 737.32
0.8032 0.1968 740.51
0.8410 0.1301 725.73
0.8670 0.1252 723.22
0.9112 0.0750 711.44
0.9143 0.0857 713.35
0.9159 0.0791 712.02
0.9384 0.0504 705.5
0.9693 0.0273 700.33
1.0000 0.0000 694.52

Mass density, kg/m3 [ref]

Operational conditions:

Fixed Measured
Mole fraction of Octane (2) - Liquid Mole fraction of Phenol, 2-methyl- (1) - Liquid Mass density, kg/m3 - Liquid
0.0000 0.8184 1035.9
0.0000 0.8443 1036.16
0.0000 0.8903 1036.47
0.0000 0.9409 1036.95
0.0000 1.0000 1036.94
0.0424 0.8084 1011.69
0.0500 0.8939 1010.32
0.0518 0.8442 1007.87
0.0621 0.7675 999.87
0.0741 0.8712 998.07
0.0779 0.9221 998.31
0.0788 0.7778 991.93
0.1358 0.7693 964.99
0.1372 0.7061 959.96
0.1580 0.7108 951.38
0.1603 0.7901 956.44
0.1634 0.8366 958.43
0.1819 0.6695 938.15
0.1955 0.7162 936.96
0.2128 0.6646 925.62
0.2270 0.7273 926.72
0.2381 0.6783 917.98
0.2569 0.7431 918.23
0.2618 0.6041 902.27
0.2758 0.6447 902.28
0.2898 0.6682 900.46
0.2990 0.7010 901.26
0.3165 0.5593 879.7
0.3212 0.5731 880.01
0.3399 0.6211 880.83
0.3533 0.5758 871.64
0.3600 0.6400 877.71
0.3779 0.5091 856.4
0.3924 0.5130 853.33
0.4206 0.4741 841.23
0.4226 0.5433 850.56
0.4277 0.5723 853.18
0.4328 0.5050 843.04
0.4565 0.4588 831.2
0.4642 0.5041 836.2
0.4784 0.4269 821.81
0.4797 0.5203 835.08
0.4986 0.4233 817.45
0.5188 0.4284 814.49
0.5668 0.3657 796.64
0.5694 0.3524 794.07
0.5787 0.4213 803.61
0.5821 0.3720 795.24
0.5968 0.3404 787.93
0.5996 0.3768 793.48
0.6279 0.3045 777.63
0.6512 0.3106 775.12
0.6607 0.3393 779.19
0.6913 0.2607 762.39
0.6933 0.2886 767.12
0.7003 0.2453 758.56
0.7217 0.2477 756.84
0.7559 0.2297 750.39
0.7569 0.2052 745.94
0.7664 0.2336 750.13
0.8006 0.1776 737.32
0.8032 0.1968 740.51
0.8410 0.1301 725.73
0.8670 0.1252 723.22
0.9112 0.0750 711.44
0.9143 0.0857 713.35
0.9159 0.0791 712.02
0.9384 0.0504 705.5
0.9693 0.0273 700.33
1.0000 0.0000 694.52

Sources