Datasets
-
Mole fraction (12)
-
ρl - Mass density, kg/m3 (2)
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mole fraction of Toluene (2) - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
| 298.15 |
0.0000 |
0.5093 |
| 298.15 |
0.0375 |
0.5160 |
| 298.15 |
0.0992 |
0.5158 |
| 298.15 |
0.1003 |
0.5216 |
| 298.15 |
0.1166 |
0.5197 |
| 298.15 |
0.1177 |
0.5247 |
| 298.15 |
0.1718 |
0.5072 |
| 298.15 |
0.1728 |
0.5100 |
| 298.15 |
0.2114 |
0.4972 |
| 298.15 |
0.2121 |
0.4988 |
| 298.15 |
0.2694 |
0.4686 |
| 298.15 |
0.2721 |
0.4732 |
| 298.15 |
0.3105 |
0.4534 |
| 298.15 |
0.3245 |
0.4486 |
| 298.15 |
0.3273 |
0.4524 |
| 298.15 |
0.3731 |
0.4293 |
| 298.15 |
0.3732 |
0.4294 |
| 298.15 |
0.4604 |
0.3847 |
| 298.15 |
0.5984 |
0.3021 |
| 298.15 |
0.6010 |
0.3034 |
| 298.15 |
0.6748 |
0.2468 |
| 298.15 |
0.6794 |
0.2484 |
| 298.15 |
0.9964 |
0.0000 |
| 323.15 |
0.0000 |
0.4917 |
| 323.15 |
0.0459 |
0.5004 |
| 323.15 |
0.0996 |
0.4967 |
| 323.15 |
0.2034 |
0.4784 |
| 323.15 |
0.3007 |
0.4432 |
| 323.15 |
0.3252 |
0.4345 |
| 323.15 |
0.9933 |
0.0000 |
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 |
24.14 |
0.0113 |
| 333.15 |
25.81 |
0.0137 |
| 333.15 |
26.18 |
0.0095 |
| 363.15 |
80.31 |
0.0167 |
| 363.15 |
87.35 |
0.0145 |
| 363.15 |
89.13 |
0.0150 |
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 |
24.14 |
0.5056 |
| 333.15 |
25.81 |
0.5076 |
| 333.15 |
26.18 |
0.5070 |
| 363.15 |
80.31 |
0.5016 |
| 363.15 |
87.35 |
0.5023 |
| 363.15 |
89.13 |
0.5022 |
Mole fraction of Toluene (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (2) - Liquid mixture 1 |
| 333.15 |
24.14 |
0.0498 |
| 333.15 |
25.81 |
0.0822 |
| 333.15 |
26.18 |
0.0913 |
| 363.15 |
80.31 |
0.0412 |
| 363.15 |
87.35 |
0.0969 |
| 363.15 |
89.13 |
0.1093 |
Mole fraction of Toluene (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Toluene (2) - Gas |
| 333.15 |
24.14 |
0.1502 |
| 333.15 |
25.81 |
0.1998 |
| 333.15 |
26.18 |
0.2064 |
| 363.15 |
80.31 |
0.0997 |
| 363.15 |
87.35 |
0.1771 |
| 363.15 |
89.13 |
0.2021 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Toluene (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Gas |
Mole fraction of Toluene (2) - Gas |
| 333.15 |
8.00 |
0.1549 |
0.7998 |
0.0523 |
0.6044 |
| 333.15 |
10.05 |
0.1335 |
0.7814 |
0.0392 |
0.4301 |
| 333.15 |
15.51 |
0.1548 |
0.7044 |
0.0216 |
0.3609 |
| 333.15 |
21.81 |
0.1433 |
0.6058 |
0.0127 |
0.2761 |
| 333.15 |
23.50 |
0.1326 |
0.5734 |
0.0114 |
0.2636 |
| 333.15 |
23.72 |
0.0635 |
0.5268 |
0.0112 |
0.1623 |
| 333.15 |
24.54 |
0.1210 |
0.5486 |
0.0097 |
0.2327 |
| 333.15 |
24.76 |
0.1382 |
0.5489 |
0.0104 |
0.2653 |
| 333.15 |
27.26 |
0.3221 |
0.4922 |
0.0073 |
0.3903 |
| 333.15 |
27.84 |
0.2179 |
0.4990 |
0.0074 |
0.3180 |
| 333.15 |
29.25 |
0.3217 |
0.4698 |
0.0067 |
0.3860 |
| 333.15 |
30.01 |
0.4339 |
0.4135 |
0.0056 |
0.4240 |
| 363.15 |
29.50 |
0.1385 |
0.7902 |
0.0677 |
0.4227 |
| 363.15 |
40.65 |
0.1541 |
0.7358 |
0.0431 |
0.3359 |
| 363.15 |
49.61 |
0.1546 |
0.6962 |
0.0353 |
0.3035 |
| 363.15 |
70.47 |
0.1394 |
0.5983 |
0.0208 |
0.2337 |
| 363.15 |
75.79 |
0.1325 |
0.5616 |
0.0176 |
0.2199 |
| 363.15 |
75.99 |
0.0516 |
0.5213 |
0.0174 |
0.1170 |
| 363.15 |
78.63 |
0.1104 |
0.5391 |
0.0164 |
0.1946 |
| 363.15 |
80.07 |
0.1360 |
0.5348 |
0.0159 |
0.2156 |
| 363.15 |
84.29 |
0.3473 |
0.4762 |
0.0119 |
0.3698 |
| 363.15 |
87.69 |
0.2245 |
0.4978 |
0.0130 |
0.2861 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Mole fraction of Toluene (2) - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
| 298.15 |
0.0000 |
0.5093 |
| 298.15 |
0.0375 |
0.5160 |
| 298.15 |
0.0992 |
0.5158 |
| 298.15 |
0.1003 |
0.5216 |
| 298.15 |
0.1166 |
0.5197 |
| 298.15 |
0.1177 |
0.5247 |
| 298.15 |
0.1718 |
0.5072 |
| 298.15 |
0.1728 |
0.5100 |
| 298.15 |
0.2114 |
0.4972 |
| 298.15 |
0.2121 |
0.4988 |
| 298.15 |
0.2694 |
0.4686 |
| 298.15 |
0.2721 |
0.4732 |
| 298.15 |
0.3105 |
0.4534 |
| 298.15 |
0.3245 |
0.4486 |
| 298.15 |
0.3273 |
0.4524 |
| 298.15 |
0.3731 |
0.4293 |
| 298.15 |
0.3732 |
0.4294 |
| 298.15 |
0.4604 |
0.3847 |
| 298.15 |
0.5984 |
0.3021 |
| 298.15 |
0.6010 |
0.3034 |
| 298.15 |
0.6748 |
0.2468 |
| 298.15 |
0.6794 |
0.2484 |
| 298.15 |
0.9964 |
0.0000 |
| 323.15 |
0.0000 |
0.4917 |
| 323.15 |
0.0459 |
0.5004 |
| 323.15 |
0.0996 |
0.4967 |
| 323.15 |
0.2034 |
0.4784 |
| 323.15 |
0.3007 |
0.4432 |
| 323.15 |
0.3252 |
0.4345 |
| 323.15 |
0.9933 |
0.0000 |
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 |
24.14 |
0.0113 |
| 333.15 |
25.81 |
0.0137 |
| 333.15 |
26.18 |
0.0095 |
| 363.15 |
80.31 |
0.0167 |
| 363.15 |
87.35 |
0.0145 |
| 363.15 |
89.13 |
0.0150 |
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 |
24.14 |
0.5056 |
| 333.15 |
25.81 |
0.5076 |
| 333.15 |
26.18 |
0.5070 |
| 363.15 |
80.31 |
0.5016 |
| 363.15 |
87.35 |
0.5023 |
| 363.15 |
89.13 |
0.5022 |
Mole fraction of Toluene (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Toluene (2) - Liquid mixture 1 |
| 333.15 |
24.14 |
0.0498 |
| 333.15 |
25.81 |
0.0822 |
| 333.15 |
26.18 |
0.0913 |
| 363.15 |
80.31 |
0.0412 |
| 363.15 |
87.35 |
0.0969 |
| 363.15 |
89.13 |
0.1093 |
Mole fraction of Toluene (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Toluene (2) - Gas |
| 333.15 |
24.14 |
0.1502 |
| 333.15 |
25.81 |
0.1998 |
| 333.15 |
26.18 |
0.2064 |
| 363.15 |
80.31 |
0.0997 |
| 363.15 |
87.35 |
0.1771 |
| 363.15 |
89.13 |
0.2021 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Toluene (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Gas |
Mole fraction of Toluene (2) - Gas |
| 333.15 |
8.00 |
0.1549 |
0.7998 |
0.0523 |
0.6044 |
| 333.15 |
10.05 |
0.1335 |
0.7814 |
0.0392 |
0.4301 |
| 333.15 |
15.51 |
0.1548 |
0.7044 |
0.0216 |
0.3609 |
| 333.15 |
21.81 |
0.1433 |
0.6058 |
0.0127 |
0.2761 |
| 333.15 |
23.50 |
0.1326 |
0.5734 |
0.0114 |
0.2636 |
| 333.15 |
23.72 |
0.0635 |
0.5268 |
0.0112 |
0.1623 |
| 333.15 |
24.54 |
0.1210 |
0.5486 |
0.0097 |
0.2327 |
| 333.15 |
24.76 |
0.1382 |
0.5489 |
0.0104 |
0.2653 |
| 333.15 |
27.26 |
0.3221 |
0.4922 |
0.0073 |
0.3903 |
| 333.15 |
27.84 |
0.2179 |
0.4990 |
0.0074 |
0.3180 |
| 333.15 |
29.25 |
0.3217 |
0.4698 |
0.0067 |
0.3860 |
| 333.15 |
30.01 |
0.4339 |
0.4135 |
0.0056 |
0.4240 |
| 363.15 |
29.50 |
0.1385 |
0.7902 |
0.0677 |
0.4227 |
| 363.15 |
40.65 |
0.1541 |
0.7358 |
0.0431 |
0.3359 |
| 363.15 |
49.61 |
0.1546 |
0.6962 |
0.0353 |
0.3035 |
| 363.15 |
70.47 |
0.1394 |
0.5983 |
0.0208 |
0.2337 |
| 363.15 |
75.79 |
0.1325 |
0.5616 |
0.0176 |
0.2199 |
| 363.15 |
75.99 |
0.0516 |
0.5213 |
0.0174 |
0.1170 |
| 363.15 |
78.63 |
0.1104 |
0.5391 |
0.0164 |
0.1946 |
| 363.15 |
80.07 |
0.1360 |
0.5348 |
0.0159 |
0.2156 |
| 363.15 |
84.29 |
0.3473 |
0.4762 |
0.0119 |
0.3698 |
| 363.15 |
87.69 |
0.2245 |
0.4978 |
0.0130 |
0.2861 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Fixed |
Measured |
| Mole fraction of Toluene (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
0.5953 |
1033.22 |
| 0.0000 |
0.6750 |
1034.33 |
| 0.0000 |
0.8012 |
1035.55 |
| 0.0000 |
0.8909 |
1036.26 |
| 0.0000 |
1.0000 |
1036.94 |
| 0.0222 |
0.5821 |
1027.5 |
| 0.0529 |
0.9471 |
1027.55 |
| 0.0549 |
0.6380 |
1021.49 |
| 0.0560 |
0.7564 |
1023.89 |
| 0.0562 |
0.8408 |
1025.41 |
| 0.0570 |
0.5614 |
1018.81 |
| 0.0819 |
0.8179 |
1020.45 |
| 0.0849 |
0.9151 |
1021.91 |
| 0.0852 |
0.7329 |
1017.91 |
| 0.1005 |
0.5355 |
1008.27 |
| 0.1135 |
0.5277 |
1005.16 |
| 0.1136 |
0.5984 |
1008.25 |
| 0.1296 |
0.6973 |
1008.91 |
| 0.1409 |
0.8591 |
1011.86 |
| 0.1438 |
0.5097 |
998.12 |
| 0.1480 |
0.7590 |
1007.86 |
| 0.1547 |
0.5706 |
999.23 |
| 0.1927 |
0.6468 |
996.27 |
| 0.1966 |
0.5423 |
990.34 |
| 0.2030 |
0.7970 |
1000.75 |
| 0.2110 |
0.7029 |
995.9 |
| 0.2450 |
0.5097 |
980.26 |
| 0.2485 |
0.6021 |
985.33 |
| 0.2680 |
0.6521 |
985.22 |
| 0.2749 |
0.7251 |
987.89 |
| 0.2989 |
0.4733 |
969.46 |
| 0.3096 |
0.5532 |
973.61 |
| 0.3254 |
0.6010 |
974.52 |
| 0.3410 |
0.6590 |
975.95 |
| 0.3729 |
0.5024 |
961.68 |
| 0.3913 |
0.4109 |
951.76 |
| 0.3927 |
0.5410 |
962.15 |
| 0.4123 |
0.4708 |
954.37 |
| 0.4343 |
0.5657 |
959.13 |
| 0.4371 |
0.5015 |
954.06 |
| 0.4707 |
0.3573 |
937.24 |
| 0.4899 |
0.4087 |
940.32 |
| 0.5187 |
0.4813 |
943.88 |
| 0.5269 |
0.4215 |
937.83 |
| 0.5631 |
0.3500 |
927.44 |
| 0.5857 |
0.2797 |
917.49 |
| 0.5864 |
0.3685 |
927.29 |
| 0.6073 |
0.3927 |
927.88 |
| 0.6275 |
0.2985 |
916.34 |
| 0.6564 |
0.3061 |
914.99 |
| 0.6800 |
0.2564 |
907.46 |
| 0.6873 |
0.3127 |
913.43 |
| 0.7024 |
0.2009 |
898.84 |
| 0.7104 |
0.2580 |
905.59 |
| 0.7547 |
0.2453 |
901.26 |
| 0.7831 |
0.1738 |
890.56 |
| 0.7852 |
0.2148 |
895.73 |
| 0.7867 |
0.1900 |
892.53 |
| 0.8147 |
0.1251 |
882.26 |
| 0.8290 |
0.1370 |
883.25 |
| 0.8381 |
0.1619 |
886.24 |
| 0.8414 |
0.1413 |
883.26 |
| 0.8481 |
0.1519 |
884.43 |
| 0.8681 |
0.1057 |
877.13 |
| 0.8915 |
0.0732 |
871.5 |
| 0.9068 |
0.0932 |
873.9 |
| 0.9287 |
0.0636 |
868.87 |
| 0.9323 |
0.0542 |
867.33 |
| 0.9346 |
0.0654 |
869.01 |
| 0.9395 |
0.0360 |
864.23 |
| 0.9513 |
0.0329 |
863.56 |
| 0.9628 |
0.0298 |
862.79 |
| 0.9737 |
0.0263 |
862.08 |
| 0.9774 |
0.0181 |
860.67 |
| 1.0000 |
0.0000 |
857.47 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Fixed |
Measured |
| Mole fraction of Toluene (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0000 |
0.5953 |
1033.22 |
| 0.0000 |
0.6750 |
1034.33 |
| 0.0000 |
0.8012 |
1035.55 |
| 0.0000 |
0.8909 |
1036.26 |
| 0.0000 |
1.0000 |
1036.94 |
| 0.0222 |
0.5821 |
1027.5 |
| 0.0529 |
0.9471 |
1027.55 |
| 0.0549 |
0.6380 |
1021.49 |
| 0.0560 |
0.7564 |
1023.89 |
| 0.0562 |
0.8408 |
1025.41 |
| 0.0570 |
0.5614 |
1018.81 |
| 0.0819 |
0.8179 |
1020.45 |
| 0.0849 |
0.9151 |
1021.91 |
| 0.0852 |
0.7329 |
1017.91 |
| 0.1005 |
0.5355 |
1008.27 |
| 0.1135 |
0.5277 |
1005.16 |
| 0.1136 |
0.5984 |
1008.25 |
| 0.1296 |
0.6973 |
1008.91 |
| 0.1409 |
0.8591 |
1011.86 |
| 0.1438 |
0.5097 |
998.12 |
| 0.1480 |
0.7590 |
1007.86 |
| 0.1547 |
0.5706 |
999.23 |
| 0.1927 |
0.6468 |
996.27 |
| 0.1966 |
0.5423 |
990.34 |
| 0.2030 |
0.7970 |
1000.75 |
| 0.2110 |
0.7029 |
995.9 |
| 0.2450 |
0.5097 |
980.26 |
| 0.2485 |
0.6021 |
985.33 |
| 0.2680 |
0.6521 |
985.22 |
| 0.2749 |
0.7251 |
987.89 |
| 0.2989 |
0.4733 |
969.46 |
| 0.3096 |
0.5532 |
973.61 |
| 0.3254 |
0.6010 |
974.52 |
| 0.3410 |
0.6590 |
975.95 |
| 0.3729 |
0.5024 |
961.68 |
| 0.3913 |
0.4109 |
951.76 |
| 0.3927 |
0.5410 |
962.15 |
| 0.4123 |
0.4708 |
954.37 |
| 0.4343 |
0.5657 |
959.13 |
| 0.4371 |
0.5015 |
954.06 |
| 0.4707 |
0.3573 |
937.24 |
| 0.4899 |
0.4087 |
940.32 |
| 0.5187 |
0.4813 |
943.88 |
| 0.5269 |
0.4215 |
937.83 |
| 0.5631 |
0.3500 |
927.44 |
| 0.5857 |
0.2797 |
917.49 |
| 0.5864 |
0.3685 |
927.29 |
| 0.6073 |
0.3927 |
927.88 |
| 0.6275 |
0.2985 |
916.34 |
| 0.6564 |
0.3061 |
914.99 |
| 0.6800 |
0.2564 |
907.46 |
| 0.6873 |
0.3127 |
913.43 |
| 0.7024 |
0.2009 |
898.84 |
| 0.7104 |
0.2580 |
905.59 |
| 0.7547 |
0.2453 |
901.26 |
| 0.7831 |
0.1738 |
890.56 |
| 0.7852 |
0.2148 |
895.73 |
| 0.7867 |
0.1900 |
892.53 |
| 0.8147 |
0.1251 |
882.26 |
| 0.8290 |
0.1370 |
883.25 |
| 0.8381 |
0.1619 |
886.24 |
| 0.8414 |
0.1413 |
883.26 |
| 0.8481 |
0.1519 |
884.43 |
| 0.8681 |
0.1057 |
877.13 |
| 0.8915 |
0.0732 |
871.5 |
| 0.9068 |
0.0932 |
873.9 |
| 0.9287 |
0.0636 |
868.87 |
| 0.9323 |
0.0542 |
867.33 |
| 0.9346 |
0.0654 |
869.01 |
| 0.9395 |
0.0360 |
864.23 |
| 0.9513 |
0.0329 |
863.56 |
| 0.9628 |
0.0298 |
862.79 |
| 0.9737 |
0.0263 |
862.08 |
| 0.9774 |
0.0181 |
860.67 |
| 1.0000 |
0.0000 |
857.47 |
Sources
