Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Methyl valerate (1) - Liquid | Mole fraction of Methyl valerate (1) - Gas |
|---|---|
| 0.0204 | 0.0114 |
| 0.0300 | 0.0168 |
| 0.0515 | 0.0289 |
| 0.0755 | 0.0425 |
| 0.1056 | 0.0595 |
| 0.1315 | 0.0739 |
| 0.1600 | 0.0901 |
| 0.1947 | 0.1097 |
| 0.2162 | 0.1221 |
| 0.2512 | 0.1421 |
| 0.2833 | 0.1609 |
| 0.3239 | 0.1827 |
| 0.3739 | 0.2127 |
| 0.4034 | 0.2279 |
| 0.4403 | 0.2479 |
| 0.4604 | 0.2597 |
| 0.4874 | 0.2787 |
| 0.5103 | 0.2936 |
| 0.5417 | 0.3170 |
| 0.5694 | 0.3386 |
| 0.6009 | 0.3654 |
| 0.6363 | 0.3928 |
| 0.6654 | 0.4199 |
| 0.6842 | 0.4391 |
| 0.7177 | 0.4721 |
| 0.7432 | 0.5002 |
| 0.7643 | 0.5254 |
| 0.7912 | 0.5580 |
| 0.8152 | 0.5917 |
| 0.8402 | 0.6307 |
| 0.8596 | 0.6667 |
| 0.8800 | 0.7050 |
| 0.9000 | 0.7500 |
| 0.9158 | 0.7892 |
| 0.9303 | 0.8255 |
| 0.9437 | 0.8542 |
| 0.9555 | 0.8836 |
| 0.9662 | 0.9129 |
| 0.9809 | 0.9505 |
| 0.9894 | 0.9729 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Methyl valerate (1) - Liquid | Mole fraction of Methyl valerate (1) - Gas |
|---|---|
| 0.0204 | 0.0114 |
| 0.0300 | 0.0168 |
| 0.0515 | 0.0289 |
| 0.0755 | 0.0425 |
| 0.1056 | 0.0595 |
| 0.1315 | 0.0739 |
| 0.1600 | 0.0901 |
| 0.1947 | 0.1097 |
| 0.2162 | 0.1221 |
| 0.2512 | 0.1421 |
| 0.2833 | 0.1609 |
| 0.3239 | 0.1827 |
| 0.3739 | 0.2127 |
| 0.4034 | 0.2279 |
| 0.4403 | 0.2479 |
| 0.4604 | 0.2597 |
| 0.4874 | 0.2787 |
| 0.5103 | 0.2936 |
| 0.5417 | 0.3170 |
| 0.5694 | 0.3386 |
| 0.6009 | 0.3654 |
| 0.6363 | 0.3928 |
| 0.6654 | 0.4199 |
| 0.6842 | 0.4391 |
| 0.7177 | 0.4721 |
| 0.7432 | 0.5002 |
| 0.7643 | 0.5254 |
| 0.7912 | 0.5580 |
| 0.8152 | 0.5917 |
| 0.8402 | 0.6307 |
| 0.8596 | 0.6667 |
| 0.8800 | 0.7050 |
| 0.9000 | 0.7500 |
| 0.9158 | 0.7892 |
| 0.9303 | 0.8255 |
| 0.9437 | 0.8542 |
| 0.9555 | 0.8836 |
| 0.9662 | 0.9129 |
| 0.9809 | 0.9505 |
| 0.9894 | 0.9729 |
Operational conditions:
| Mole fraction of Methyl valerate (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0172 | 682.12 |
| 0.0613 | 689.72 |
| 0.1404 | 703.9 |
| 0.2074 | 716.09 |
| 0.2867 | 731.09 |
| 0.3552 | 744.33 |
| 0.4135 | 755.77 |
| 0.4931 | 771.88 |
| 0.5619 | 786.14 |
| 0.6310 | 800.74 |
| 0.7038 | 816.52 |
| 0.7607 | 828.99 |
| 0.8392 | 846.84 |
| 0.9149 | 864.2 |
| 0.9531 | 873.23 |
| 0.9836 | 880.67 |
Operational conditions:
| Mole fraction of Methyl valerate (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0172 | 682.12 |
| 0.0613 | 689.72 |
| 0.1404 | 703.9 |
| 0.2074 | 716.09 |
| 0.2867 | 731.09 |
| 0.3552 | 744.33 |
| 0.4135 | 755.77 |
| 0.4931 | 771.88 |
| 0.5619 | 786.14 |
| 0.6310 | 800.74 |
| 0.7038 | 816.52 |
| 0.7607 | 828.99 |
| 0.8392 | 846.84 |
| 0.9149 | 864.2 |
| 0.9531 | 873.23 |
| 0.9836 | 880.67 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Methyl valerate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0204 | 371.48 |
| 0.0300 | 371.61 |
| 0.0515 | 371.80 |
| 0.0755 | 371.97 |
| 0.1056 | 372.21 |
| 0.1315 | 372.50 |
| 0.1600 | 372.81 |
| 0.1947 | 373.17 |
| 0.2162 | 373.48 |
| 0.2512 | 373.95 |
| 0.2833 | 374.42 |
| 0.3239 | 375.00 |
| 0.3739 | 375.90 |
| 0.4034 | 376.32 |
| 0.4403 | 376.92 |
| 0.4604 | 377.35 |
| 0.4874 | 377.95 |
| 0.5103 | 378.45 |
| 0.5417 | 379.20 |
| 0.5694 | 379.95 |
| 0.6009 | 380.85 |
| 0.6363 | 381.80 |
| 0.6654 | 382.70 |
| 0.6842 | 383.35 |
| 0.7177 | 384.37 |
| 0.7432 | 385.40 |
| 0.7643 | 386.20 |
| 0.7912 | 387.42 |
| 0.8152 | 388.50 |
| 0.8402 | 389.65 |
| 0.8596 | 390.65 |
| 0.8800 | 391.75 |
| 0.9000 | 393.20 |
| 0.9158 | 394.40 |
| 0.9303 | 395.35 |
| 0.9437 | 396.15 |
| 0.9555 | 396.90 |
| 0.9662 | 397.68 |
| 0.9809 | 398.91 |
| 0.9894 | 399.54 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Methyl valerate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0204 | 371.48 |
| 0.0300 | 371.61 |
| 0.0515 | 371.80 |
| 0.0755 | 371.97 |
| 0.1056 | 372.21 |
| 0.1315 | 372.50 |
| 0.1600 | 372.81 |
| 0.1947 | 373.17 |
| 0.2162 | 373.48 |
| 0.2512 | 373.95 |
| 0.2833 | 374.42 |
| 0.3239 | 375.00 |
| 0.3739 | 375.90 |
| 0.4034 | 376.32 |
| 0.4403 | 376.92 |
| 0.4604 | 377.35 |
| 0.4874 | 377.95 |
| 0.5103 | 378.45 |
| 0.5417 | 379.20 |
| 0.5694 | 379.95 |
| 0.6009 | 380.85 |
| 0.6363 | 381.80 |
| 0.6654 | 382.70 |
| 0.6842 | 383.35 |
| 0.7177 | 384.37 |
| 0.7432 | 385.40 |
| 0.7643 | 386.20 |
| 0.7912 | 387.42 |
| 0.8152 | 388.50 |
| 0.8402 | 389.65 |
| 0.8596 | 390.65 |
| 0.8800 | 391.75 |
| 0.9000 | 393.20 |
| 0.9158 | 394.40 |
| 0.9303 | 395.35 |
| 0.9437 | 396.15 |
| 0.9555 | 396.90 |
| 0.9662 | 397.68 |
| 0.9809 | 398.91 |
| 0.9894 | 399.54 |