Operational conditions:
| Mole fraction of Phenol, 2-methyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1954 | -1.112 |
| 0.4127 | -1.6207 |
| 0.6007 | -1.6522 |
| 0.8013 | -0.9436 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0000 | 1037.02 |
| 303.15 | 0.1387 | 1015.95 |
| 303.15 | 0.2617 | 994.82 |
| 303.15 | 0.3713 | 973.68 |
| 303.15 | 0.4698 | 952.47 |
| 303.15 | 0.5586 | 931.22 |
| 303.15 | 0.6392 | 909.96 |
| 303.15 | 0.7127 | 888.59 |
| 303.15 | 0.7799 | 867.19 |
| 303.15 | 0.8417 | 845.72 |
| 303.15 | 0.8986 | 824.22 |
| 303.15 | 0.9510 | 802.69 |
| 303.15 | 1.0000 | 781.08 |
| 308.15 | 0.0000 | 1032.58 |
| 308.15 | 0.1387 | 1011.54 |
| 308.15 | 0.2617 | 990.39 |
| 308.15 | 0.3713 | 969.21 |
| 308.15 | 0.4698 | 947.97 |
| 308.15 | 0.5586 | 926.73 |
| 308.15 | 0.6392 | 905.45 |
| 308.15 | 0.7127 | 884.08 |
| 308.15 | 0.7799 | 862.71 |
| 308.15 | 0.8417 | 841.26 |
| 308.15 | 0.8986 | 819.77 |
| 308.15 | 0.9510 | 798.22 |
| 308.15 | 1.0000 | 776.59 |
| 313.15 | 0.0000 | 1028.19 |
| 313.15 | 0.1387 | 1007.18 |
| 313.15 | 0.2617 | 986.02 |
| 313.15 | 0.3713 | 964.81 |
| 313.15 | 0.4698 | 943.57 |
| 313.15 | 0.5586 | 922.33 |
| 313.15 | 0.6392 | 901.08 |
| 313.15 | 0.7127 | 879.74 |
| 313.15 | 0.7799 | 858.37 |
| 313.15 | 0.8417 | 836.92 |
| 313.15 | 0.8986 | 815.43 |
| 313.15 | 0.9510 | 793.89 |
| 313.15 | 1.0000 | 772.23 |
| 318.15 | 0.0000 | 1023.82 |
| 318.15 | 0.1387 | 1002.83 |
| 318.15 | 0.2617 | 981.62 |
| 318.15 | 0.3713 | 960.38 |
| 318.15 | 0.4698 | 939.1 |
| 318.15 | 0.5586 | 917.85 |
| 318.15 | 0.6392 | 896.59 |
| 318.15 | 0.7127 | 875.23 |
| 318.15 | 0.7799 | 853.88 |
| 318.15 | 0.8417 | 832.43 |
| 318.15 | 0.8986 | 810.91 |
| 318.15 | 0.9510 | 789.33 |
| 318.15 | 1.0000 | 767.61 |
Operational conditions:
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 0.0000 | 1488.12 |
| 303.15 | 0.1387 | 1435.4 |
| 303.15 | 0.2617 | 1391.2 |
| 303.15 | 0.3713 | 1351.2 |
| 303.15 | 0.4698 | 1314.2 |
| 303.15 | 0.5586 | 1280.2 |
| 303.15 | 0.6392 | 1249.3 |
| 303.15 | 0.7127 | 1221.5 |
| 303.15 | 0.7799 | 1196.9 |
| 303.15 | 0.8417 | 1175.2 |
| 303.15 | 0.8986 | 1156.5 |
| 303.15 | 0.9510 | 1140.6 |
| 303.15 | 1.0000 | 1127.01 |
| 313.15 | 0.0000 | 1453.02 |
| 313.15 | 0.1387 | 1401.2 |
| 313.15 | 0.2617 | 1355.4 |
| 313.15 | 0.3713 | 1314.6 |
| 313.15 | 0.4698 | 1277.9 |
| 313.15 | 0.5586 | 1245.0 |
| 313.15 | 0.6392 | 1215.3 |
| 313.15 | 0.7127 | 1188.6 |
| 313.15 | 0.7799 | 1164.8 |
| 313.15 | 0.8417 | 1143.6 |
| 313.15 | 0.8986 | 1124.8 |
| 313.15 | 0.9510 | 1108.4 |
| 313.15 | 1.0000 | 1094.03 |
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Mole fraction of Phenol, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
| 9.00 | 0.0970 | 302.23 |
| 9.00 | 0.2060 | 305.46 |
| 9.00 | 0.3040 | 308.67 |
| 9.00 | 0.3900 | 312.21 |
| 9.00 | 0.5070 | 319.01 |
| 9.00 | 0.5970 | 326.79 |
| 9.00 | 0.6990 | 333.07 |
| 9.00 | 0.7910 | 342.80 |
| 9.00 | 0.8980 | 359.99 |
| 15.00 | 0.0970 | 311.87 |
| 15.00 | 0.2060 | 315.32 |
| 15.00 | 0.3040 | 319.29 |
| 15.00 | 0.3900 | 322.19 |
| 15.00 | 0.5070 | 329.86 |
| 15.00 | 0.5970 | 336.50 |
| 15.00 | 0.6990 | 344.12 |
| 15.00 | 0.7910 | 354.31 |
| 15.00 | 0.8980 | 373.10 |
| 35.10 | 0.0970 | 329.36 |
| 35.10 | 0.2060 | 333.25 |
| 35.10 | 0.3040 | 337.22 |
| 35.10 | 0.3900 | 340.16 |
| 35.10 | 0.5070 | 348.90 |
| 35.10 | 0.5970 | 356.03 |
| 35.10 | 0.6990 | 363.84 |
| 35.10 | 0.7910 | 375.90 |
| 55.10 | 0.0970 | 339.54 |
| 55.10 | 0.2060 | 343.48 |
| 55.10 | 0.3040 | 347.87 |
| 55.10 | 0.3900 | 350.35 |
| 55.10 | 0.5070 | 360.29 |
| 55.10 | 0.5970 | 367.82 |
| 55.10 | 0.6990 | 376.33 |
| 55.10 | 0.7910 | 389.39 |
| 75.00 | 0.0970 | 346.85 |
| 75.00 | 0.2060 | 351.09 |
| 75.00 | 0.3040 | 355.53 |
| 75.00 | 0.3900 | 357.50 |
| 75.00 | 0.5070 | 368.40 |
| 75.00 | 0.5970 | 376.10 |
| 75.00 | 0.6990 | 385.84 |
| 85.10 | 0.0970 | 349.95 |
| 85.10 | 0.2060 | 354.17 |
| 85.10 | 0.3040 | 358.80 |
| 85.10 | 0.3900 | 360.75 |
| 85.10 | 0.5070 | 371.88 |
| 85.10 | 0.5970 | 379.52 |
| 85.10 | 0.6990 | 389.62 |
| 99.10 | 0.0970 | 353.75 |
| 97.70 | 0.2060 | 357.95 |
| 99.70 | 0.3040 | 363.05 |
| 99.90 | 0.3900 | 364.60 |
| 99.10 | 0.5070 | 374.97 |
| 98.50 | 0.5970 | 384.56 |
| 99.40 | 0.6990 | 394.11 |
Operational condition: Pressure, kPa = 95.76 (Liquid)
| Mole fraction of Ethanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 461.85 |
| 0.0512 | 434.85 |
| 0.1002 | 419.35 |
| 0.1505 | 408.15 |
| 0.1926 | 400.85 |
| 0.3003 | 387.15 |
| 0.4005 | 378.05 |
| 0.5003 | 370.85 |
| 0.6096 | 364.55 |
| 0.7002 | 360.15 |
| 0.8226 | 355.35 |
| 0.9003 | 352.85 |
| 0.9511 | 351.35 |
| 1.0000 | 350.05 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.