Operational conditions:
| Mole fraction of LACTIC ACID, ETHYL ESTER (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0510 | -0.0368 |
| 0.1040 | -0.0696 |
| 0.2090 | -0.1250 |
| 0.3270 | -0.1510 |
| 0.4370 | -0.1580 |
| 0.5690 | -0.1490 |
| 0.6210 | -0.1310 |
| 0.7630 | -0.0833 |
| 0.8300 | -0.0562 |
| 0.9050 | -0.0281 |
| 0.9580 | -0.0110 |
Operational conditions:
| Mole fraction of LACTIC ACID, ETHYL ESTER (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 786.53 |
| 0.0432 | 816.63 |
| 0.0935 | 846.09 |
| 0.1911 | 890.78 |
| 0.2979 | 926.51 |
| 0.3976 | 951.94 |
| 0.5018 | 972.85 |
| 0.5789 | 985.46 |
| 0.6950 | 1000.96 |
| 0.8045 | 1012.66 |
| 0.9018 | 1021.2 |
| 0.9622 | 1025.79 |
| 1.0000 | 1028.45 |
Operational conditions:
| Mole fraction of LACTIC ACID, ETHYL ESTER (1) - Liquid | Speed of sound, m/s - Liquid |
|---|---|
| 0.0000 | 1103.95 |
| 0.0432 | 1125.5 |
| 0.0935 | 1149.11 |
| 0.1911 | 1187.02 |
| 0.2979 | 1215.43 |
| 0.3976 | 1234.51 |
| 0.5018 | 1250.53 |
| 0.5789 | 1258.98 |
| 0.6950 | 1270.32 |
| 0.8045 | 1275.92 |
| 0.9018 | 1278.25 |
| 0.9622 | 1278.96 |
| 1.0000 | 1279.34 |
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Mole fraction of Methyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
| 40.00 | 0.0000 | 396.91 |
| 40.00 | 0.1055 | 372.42 |
| 40.00 | 0.2097 | 355.98 |
| 40.00 | 0.3128 | 344.84 |
| 40.00 | 0.4147 | 336.70 |
| 40.00 | 0.5138 | 331.33 |
| 40.00 | 0.6145 | 327.05 |
| 40.00 | 0.7125 | 323.14 |
| 40.00 | 0.8095 | 320.18 |
| 40.00 | 0.9054 | 317.57 |
| 40.00 | 1.0000 | 315.49 |
| 53.33 | 0.0000 | 405.49 |
| 53.33 | 0.1055 | 380.91 |
| 53.33 | 0.2097 | 364.10 |
| 53.33 | 0.3128 | 353.04 |
| 53.33 | 0.4147 | 344.04 |
| 53.33 | 0.5138 | 339.30 |
| 53.33 | 0.6145 | 333.90 |
| 53.33 | 0.7125 | 330.00 |
| 53.33 | 0.8095 | 327.13 |
| 53.33 | 0.9054 | 324.37 |
| 53.33 | 1.0000 | 321.98 |
| 66.66 | 0.0000 | 412.44 |
| 66.66 | 0.1055 | 387.65 |
| 66.66 | 0.2097 | 370.86 |
| 66.66 | 0.3128 | 361.01 |
| 66.66 | 0.4147 | 349.97 |
| 66.66 | 0.5138 | 344.07 |
| 66.66 | 0.6145 | 339.52 |
| 66.66 | 0.7125 | 335.59 |
| 66.66 | 0.8095 | 332.67 |
| 66.66 | 0.9054 | 330.09 |
| 66.66 | 1.0000 | 327.23 |
| 79.99 | 0.0000 | 418.34 |
| 79.99 | 0.1055 | 394.50 |
| 79.99 | 0.2097 | 374.40 |
| 79.99 | 0.3128 | 366.29 |
| 79.99 | 0.4147 | 355.27 |
| 79.99 | 0.5138 | 349.14 |
| 79.99 | 0.6145 | 344.31 |
| 79.99 | 0.7125 | 340.35 |
| 79.99 | 0.8095 | 337.56 |
| 79.99 | 0.9054 | 334.95 |
| 79.99 | 1.0000 | 331.66 |
| 93.32 | 0.0000 | 423.47 |
| 93.32 | 0.1055 | 401.49 |
| 93.32 | 0.2097 | 379.00 |
| 93.32 | 0.3128 | 371.03 |
| 93.32 | 0.4147 | 359.94 |
| 93.32 | 0.5138 | 353.53 |
| 93.32 | 0.6145 | 348.49 |
| 93.32 | 0.7125 | 344.59 |
| 93.32 | 0.8095 | 341.76 |
| 93.32 | 0.9054 | 339.40 |
| 93.32 | 1.0000 | 335.51 |
| 101.30 | 0.0000 | 426.10 |
| 101.30 | 0.1055 | 405.09 |
| 101.30 | 0.2097 | 382.88 |
| 101.30 | 0.3128 | 373.81 |
| 101.30 | 0.4147 | 362.22 |
| 101.30 | 0.5138 | 356.01 |
| 101.30 | 0.6145 | 350.82 |
| 101.30 | 0.7125 | 346.88 |
| 101.30 | 0.8095 | 344.04 |
| 101.30 | 0.9054 | 341.63 |
| 101.30 | 1.0000 | 337.60 |
| 40.00 | 0.7700 | 321.36 |
| 53.33 | 0.7700 | 327.99 |
| 66.66 | 0.7700 | 333.33 |
| 79.99 | 0.7700 | 338.00 |
| 93.32 | 0.7700 | 342.17 |
| 101.30 | 0.7700 | 344.55 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Methyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.9500 | 339.52 |
| 0.8800 | 342.02 |
Note: These property values are available through the Cheméo API. A free account gives you an access key.