Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 1-Butanol (1) - Liquid | Mole fraction of 1-Butanol (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0175 | 0.1033 |
| 0.0712 | 0.3410 |
| 0.1487 | 0.5475 |
| 0.2029 | 0.6444 |
| 0.2636 | 0.7220 |
| 0.3376 | 0.7983 |
| 0.3773 | 0.8334 |
| 0.4049 | 0.8410 |
| 0.4556 | 0.8830 |
| 0.4941 | 0.8947 |
| 0.5113 | 0.8994 |
| 0.5357 | 0.9065 |
| 0.5835 | 0.9290 |
| 0.5940 | 0.9316 |
| 0.6699 | 0.9505 |
| 0.6887 | 0.9589 |
| 0.7218 | 0.9671 |
| 0.7534 | 0.9683 |
| 0.8587 | 0.9800 |
| 0.9106 | 0.9880 |
| 0.9238 | 0.9895 |
| 0.9398 | 0.9913 |
| 0.9536 | 0.9924 |
| 0.9667 | 0.9938 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 1-Butanol (1) - Liquid | Mole fraction of 1-Butanol (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0175 | 0.1033 |
| 0.0712 | 0.3410 |
| 0.1487 | 0.5475 |
| 0.2029 | 0.6444 |
| 0.2636 | 0.7220 |
| 0.3376 | 0.7983 |
| 0.3773 | 0.8334 |
| 0.4049 | 0.8410 |
| 0.4556 | 0.8830 |
| 0.4941 | 0.8947 |
| 0.5113 | 0.8994 |
| 0.5357 | 0.9065 |
| 0.5835 | 0.9290 |
| 0.5940 | 0.9316 |
| 0.6699 | 0.9505 |
| 0.6887 | 0.9589 |
| 0.7218 | 0.9671 |
| 0.7534 | 0.9683 |
| 0.8587 | 0.9800 |
| 0.9106 | 0.9880 |
| 0.9238 | 0.9895 |
| 0.9398 | 0.9913 |
| 0.9536 | 0.9924 |
| 0.9667 | 0.9938 |
| 1.0000 | 1.0000 |
Operational conditions:
| Mole fraction of 1-Butanol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 982.178 |
| 0.0989 | 971.809 |
| 0.1806 | 962.459 |
| 0.2599 | 952.704 |
| 0.3973 | 933.863 |
| 0.5154 | 915.521 |
| 0.5669 | 906.818 |
| 0.6645 | 888.883 |
| 0.7069 | 880.503 |
| 0.7854 | 863.836 |
| 0.8546 | 847.901 |
| 0.9174 | 832.199 |
| 0.9728 | 817.297 |
| 1.0000 | 809.572 |
Operational conditions:
| Mole fraction of 1-Butanol (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 982.178 |
| 0.0989 | 971.809 |
| 0.1806 | 962.459 |
| 0.2599 | 952.704 |
| 0.3973 | 933.863 |
| 0.5154 | 915.521 |
| 0.5669 | 906.818 |
| 0.6645 | 888.883 |
| 0.7069 | 880.503 |
| 0.7854 | 863.836 |
| 0.8546 | 847.901 |
| 0.9174 | 832.199 |
| 0.9728 | 817.297 |
| 1.0000 | 809.572 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 1-Butanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 460.75 |
| 0.0175 | 457.75 |
| 0.0712 | 448.89 |
| 0.1487 | 437.50 |
| 0.2029 | 431.27 |
| 0.2636 | 425.10 |
| 0.3376 | 419.40 |
| 0.3773 | 415.77 |
| 0.4049 | 414.45 |
| 0.4556 | 411.10 |
| 0.4941 | 409.19 |
| 0.5113 | 408.21 |
| 0.5357 | 407.10 |
| 0.5835 | 404.73 |
| 0.5940 | 404.17 |
| 0.6699 | 400.95 |
| 0.6887 | 400.00 |
| 0.7218 | 398.67 |
| 0.7534 | 397.60 |
| 0.8587 | 394.27 |
| 0.9106 | 392.77 |
| 0.9238 | 392.34 |
| 0.9398 | 391.99 |
| 0.9536 | 391.59 |
| 0.9667 | 391.35 |
| 1.0000 | 390.88 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 1-Butanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 460.75 |
| 0.0175 | 457.75 |
| 0.0712 | 448.89 |
| 0.1487 | 437.50 |
| 0.2029 | 431.27 |
| 0.2636 | 425.10 |
| 0.3376 | 419.40 |
| 0.3773 | 415.77 |
| 0.4049 | 414.45 |
| 0.4556 | 411.10 |
| 0.4941 | 409.19 |
| 0.5113 | 408.21 |
| 0.5357 | 407.10 |
| 0.5835 | 404.73 |
| 0.5940 | 404.17 |
| 0.6699 | 400.95 |
| 0.6887 | 400.00 |
| 0.7218 | 398.67 |
| 0.7534 | 397.60 |
| 0.8587 | 394.27 |
| 0.9106 | 392.77 |
| 0.9238 | 392.34 |
| 0.9398 | 391.99 |
| 0.9536 | 391.59 |
| 0.9667 | 391.35 |
| 1.0000 | 390.88 |