Mixture of Toluene + Phenol, 3-methyl- + Water

Excel

Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

Phenol, 3-methyl-

Name
Phenol, 3-methyl-
InChI
InChI=1S/C7H8O/c1-6-3-2-4-7(8)5-6/h2-5,8H,1H3
InChI Key
RLSSMJSEOOYNOY-UHFFFAOYSA-N
Formula
C7H8O
SMILES
Cc1cccc(O)c1
Mol. Weight (g/mol)
108.14
CAS
108-39-4

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
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Datasets

  1. Mole fraction (4)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. ρl - Mass density, kg/m3 (2)

Mole fraction of Phenol, 3-methyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Toluene (1) - Liquid mixture 1 Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 1
298.15 0.0000 0.5184
298.15 0.1358 0.5087
298.15 0.1776 0.4952
298.15 0.2195 0.4835
298.15 0.2867 0.4565
298.15 0.3295 0.4375
298.15 0.4116 0.3983
298.15 0.5338 0.3300
298.15 0.5791 0.3022
298.15 0.6960 0.2252
323.15 0.0000 0.4742
323.15 0.0724 0.4826
323.15 0.1182 0.4801
323.15 0.1615 0.4696
323.15 0.1774 0.4692
323.15 0.2037 0.4668
323.15 0.2133 0.4547
323.15 0.2756 0.4362
323.15 0.3409 0.4118
323.15 0.4912 0.3408
323.15 0.5216 0.3241
323.15 0.5891 0.2847
323.15 0.7168 0.2009
323.15 0.7527 0.1692
323.15 0.7735 0.1672

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

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Toluene (1) - Gas Mole fraction of Phenol, 3-methyl- (2) - Gas Mole fraction of Toluene (1) - Liquid Mole fraction of Phenol, 3-methyl- (2) - Liquid
333.15 17.05 0.4075 0.0090 0.1559 0.6719
333.15 19.87 0.2005 0.0093 0.0914 0.6257
333.15 21.20 0.1335 0.0082 0.0456 0.5749
333.15 23.85 0.2006 0.0079 0.0571 0.5202
333.15 24.54 0.2277 0.0060 0.1394 0.5444
333.15 25.74 0.2692 0.0083 0.0933 0.5120
333.15 25.85 0.2011 0.0058 0.0608 0.4372
363.15 70.07 0.3382 0.0194 0.1595 0.6066
363.15 72.38 0.2036 0.0147 0.0950 0.5798
363.15 82.94 0.1594 0.0109 0.0530 0.4458
363.15 85.15 0.2084 0.0100 0.1225 0.4960
363.15 93.59 0.1992 0.0108 0.0990 0.4100

Mole fraction of Phenol, 3-methyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed Measured
Temperature, K - Liquid mixture 1 Mole fraction of Toluene (1) - Liquid mixture 1 Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 1
298.15 0.0000 0.5184
298.15 0.1358 0.5087
298.15 0.1776 0.4952
298.15 0.2195 0.4835
298.15 0.2867 0.4565
298.15 0.3295 0.4375
298.15 0.4116 0.3983
298.15 0.5338 0.3300
298.15 0.5791 0.3022
298.15 0.6960 0.2252
323.15 0.0000 0.4742
323.15 0.0724 0.4826
323.15 0.1182 0.4801
323.15 0.1615 0.4696
323.15 0.1774 0.4692
323.15 0.2037 0.4668
323.15 0.2133 0.4547
323.15 0.2756 0.4362
323.15 0.3409 0.4118
323.15 0.4912 0.3408
323.15 0.5216 0.3241
323.15 0.5891 0.2847
323.15 0.7168 0.2009
323.15 0.7527 0.1692
323.15 0.7735 0.1672

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

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mole fraction of Toluene (1) - Gas Mole fraction of Phenol, 3-methyl- (2) - Gas Mole fraction of Toluene (1) - Liquid Mole fraction of Phenol, 3-methyl- (2) - Liquid
333.15 17.05 0.4075 0.0090 0.1559 0.6719
333.15 19.87 0.2005 0.0093 0.0914 0.6257
333.15 21.20 0.1335 0.0082 0.0456 0.5749
333.15 23.85 0.2006 0.0079 0.0571 0.5202
333.15 24.54 0.2277 0.0060 0.1394 0.5444
333.15 25.74 0.2692 0.0083 0.0933 0.5120
333.15 25.85 0.2011 0.0058 0.0608 0.4372
363.15 70.07 0.3382 0.0194 0.1595 0.6066
363.15 72.38 0.2036 0.0147 0.0950 0.5798
363.15 82.94 0.1594 0.0109 0.0530 0.4458
363.15 85.15 0.2084 0.0100 0.1225 0.4960
363.15 93.59 0.1992 0.0108 0.0990 0.4100

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Mole fraction of Phenol, 3-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
333.15 0.0601 0.5339 23.94
333.15 0.0622 0.7417 14.65
333.15 0.0819 0.6733 18.47
363.15 0.0383 0.5224 74.19
363.15 0.0404 0.4936 77.59
363.15 0.0489 0.4833 79.19
363.15 0.0645 0.4386 89.66
363.15 0.0820 0.5526 75.99
363.15 0.0902 0.5993 69.60
363.15 0.0958 0.6616 57.10

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Mole fraction of Phenol, 3-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
333.15 0.0601 0.5339 23.94
333.15 0.0622 0.7417 14.65
333.15 0.0819 0.6733 18.47
363.15 0.0383 0.5224 74.19
363.15 0.0404 0.4936 77.59
363.15 0.0489 0.4833 79.19
363.15 0.0645 0.4386 89.66
363.15 0.0820 0.5526 75.99
363.15 0.0902 0.5993 69.60
363.15 0.0958 0.6616 57.10

Mass density, kg/m3 [ref]

Operational conditions:

Fixed Measured
Mole fraction of Toluene (1) - Liquid Mole fraction of Phenol, 3-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 0.5470 1020.94
0.0000 0.5754 1021.37
0.0000 0.6312 1022.09
0.0000 0.6558 1022.4
0.0000 0.7040 1022.95
0.0000 0.7933 1023.97
0.0000 0.8839 1024.94
0.0000 1.0000 1025.95
0.0349 0.5553 1013.01
0.0416 0.7603 1015.97
0.0518 0.8381 1015.71
0.0563 0.9437 1016.89
0.0655 0.6129 1008.16
0.0663 0.6573 1009.17
0.0677 0.5100 1004.48
0.0712 0.5863 1006.26
0.0807 0.8125 1010.57
0.0853 0.9147 1012.17
0.0895 0.7223 1006.9
0.0977 0.5191 998.62
0.1022 0.4911 996.49
0.1135 0.6241 999.64
0.1190 0.5778 996.92
0.1423 0.7581 999.76
0.1443 0.5402 990.75
0.1465 0.6771 996.24
0.1619 0.8381 999.57
0.1759 0.4742 981.74
0.1812 0.4479 979.21
0.2097 0.6985 987.94
0.2139 0.4962 976.76
0.2160 0.5142 977.55
0.2203 0.5489 978.85
0.2242 0.5461 978.02
0.2245 0.4462 971.81
0.2381 0.4167 967.56
0.2482 0.4746 970.05
0.2521 0.7479 984.6
0.2560 0.5902 976.19
0.2597 0.4855 969.19
0.2788 0.4553 964.39
0.2816 0.3930 959.09
0.2894 0.5637 970.22
0.2989 0.6196 972.36
0.3042 0.4003 956.41
0.3053 0.6947 975.73
0.3302 0.4393 956.24
0.3477 0.5175 959.94
0.3572 0.4057 949.99
0.3608 0.3678 946.12
0.3613 0.4496 953.14
0.3743 0.4103 948.39
0.3776 0.3405 941.46
0.3799 0.6201 963.22
0.3847 0.5438 957.6
0.3865 0.4319 948.68
0.4119 0.3217 935.52
0.4224 0.4582 947.05
0.4251 0.3308 935.16
0.4364 0.4982 948.83
0.4461 0.3496 934.71
0.4494 0.5506 951.45
0.4591 0.3548 933.9
0.4834 0.3637 932.26
0.4837 0.2971 925.38
0.4852 0.4084 936.46
0.4929 0.2774 922.3
0.5158 0.3175 924.6
0.5205 0.4795 939.49
0.5261 0.4189 933.73
0.5313 0.2959 920.74
0.5394 0.2520 915.12
0.5414 0.3008 920.58
0.5541 0.3139 920.83
0.5656 0.3446 923.17
0.5695 0.2477 912.16
0.5781 0.3729 924.98
0.5917 0.2577 911.54
0.6225 0.2172 904.32
0.6246 0.2054 902.74
0.6281 0.2618 909.31
0.6286 0.2947 913.02
0.6317 0.3256 916.12
0.6349 0.2305 904.97
0.6510 0.2457 905.73
0.6639 0.1838 897.28
0.6652 0.2196 901.71
0.7046 0.2611 904.23
0.7198 0.2802 905.42
0.7382 0.1652 890.32
0.7425 0.1689 890.66
0.7616 0.1678 889.55
0.7672 0.1340 884.73
0.7683 0.1838 891.21
0.7702 0.2031 893.58
0.8129 0.1871 889.49
0.8330 0.1176 879.53
0.8406 0.0872 874.54
0.8411 0.1042 876.88
0.8470 0.0881 874.79
0.8588 0.0891 874.04
0.8663 0.0731 871.76
0.8723 0.1277 879.32
0.8846 0.1020 875.4
0.9119 0.0507 867.07
0.9221 0.0492 866.5
0.9373 0.0442 865.34
0.9407 0.0389 864.5
0.9534 0.0466 865.4
0.9700 0.0265 862.1
1.0000 0.0000 857.47

Mass density, kg/m3 [ref]

Operational conditions:

Fixed Measured
Mole fraction of Toluene (1) - Liquid Mole fraction of Phenol, 3-methyl- (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 0.5470 1020.94
0.0000 0.5754 1021.37
0.0000 0.6312 1022.09
0.0000 0.6558 1022.4
0.0000 0.7040 1022.95
0.0000 0.7933 1023.97
0.0000 0.8839 1024.94
0.0000 1.0000 1025.95
0.0349 0.5553 1013.01
0.0416 0.7603 1015.97
0.0518 0.8381 1015.71
0.0563 0.9437 1016.89
0.0655 0.6129 1008.16
0.0663 0.6573 1009.17
0.0677 0.5100 1004.48
0.0712 0.5863 1006.26
0.0807 0.8125 1010.57
0.0853 0.9147 1012.17
0.0895 0.7223 1006.9
0.0977 0.5191 998.62
0.1022 0.4911 996.49
0.1135 0.6241 999.64
0.1190 0.5778 996.92
0.1423 0.7581 999.76
0.1443 0.5402 990.75
0.1465 0.6771 996.24
0.1619 0.8381 999.57
0.1759 0.4742 981.74
0.1812 0.4479 979.21
0.2097 0.6985 987.94
0.2139 0.4962 976.76
0.2160 0.5142 977.55
0.2203 0.5489 978.85
0.2242 0.5461 978.02
0.2245 0.4462 971.81
0.2381 0.4167 967.56
0.2482 0.4746 970.05
0.2521 0.7479 984.6
0.2560 0.5902 976.19
0.2597 0.4855 969.19
0.2788 0.4553 964.39
0.2816 0.3930 959.09
0.2894 0.5637 970.22
0.2989 0.6196 972.36
0.3042 0.4003 956.41
0.3053 0.6947 975.73
0.3302 0.4393 956.24
0.3477 0.5175 959.94
0.3572 0.4057 949.99
0.3608 0.3678 946.12
0.3613 0.4496 953.14
0.3743 0.4103 948.39
0.3776 0.3405 941.46
0.3799 0.6201 963.22
0.3847 0.5438 957.6
0.3865 0.4319 948.68
0.4119 0.3217 935.52
0.4224 0.4582 947.05
0.4251 0.3308 935.16
0.4364 0.4982 948.83
0.4461 0.3496 934.71
0.4494 0.5506 951.45
0.4591 0.3548 933.9
0.4834 0.3637 932.26
0.4837 0.2971 925.38
0.4852 0.4084 936.46
0.4929 0.2774 922.3
0.5158 0.3175 924.6
0.5205 0.4795 939.49
0.5261 0.4189 933.73
0.5313 0.2959 920.74
0.5394 0.2520 915.12
0.5414 0.3008 920.58
0.5541 0.3139 920.83
0.5656 0.3446 923.17
0.5695 0.2477 912.16
0.5781 0.3729 924.98
0.5917 0.2577 911.54
0.6225 0.2172 904.32
0.6246 0.2054 902.74
0.6281 0.2618 909.31
0.6286 0.2947 913.02
0.6317 0.3256 916.12
0.6349 0.2305 904.97
0.6510 0.2457 905.73
0.6639 0.1838 897.28
0.6652 0.2196 901.71
0.7046 0.2611 904.23
0.7198 0.2802 905.42
0.7382 0.1652 890.32
0.7425 0.1689 890.66
0.7616 0.1678 889.55
0.7672 0.1340 884.73
0.7683 0.1838 891.21
0.7702 0.2031 893.58
0.8129 0.1871 889.49
0.8330 0.1176 879.53
0.8406 0.0872 874.54
0.8411 0.1042 876.88
0.8470 0.0881 874.79
0.8588 0.0891 874.04
0.8663 0.0731 871.76
0.8723 0.1277 879.32
0.8846 0.1020 875.4
0.9119 0.0507 867.07
0.9221 0.0492 866.5
0.9373 0.0442 865.34
0.9407 0.0389 864.5
0.9534 0.0466 865.4
0.9700 0.0265 862.1
1.0000 0.0000 857.47

Sources