Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 | Mole fraction of Toluene (1) - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 2 | Mole fraction of Toluene (1) - Liquid mixture 2 |
298.15 | 0.7643 | 0.2021 | 0.0300 | 0.0762 |
298.15 | 0.6402 | 0.3071 | 0.0385 | 0.1430 |
298.15 | 0.5715 | 0.3613 | 0.0458 | 0.1897 |
298.15 | 0.4445 | 0.4494 | 0.0674 | 0.2941 |
298.15 | 0.4065 | 0.4714 | 0.0770 | 0.3287 |
298.15 | 0.3565 | 0.4957 | 0.0927 | 0.3753 |
298.15 | 0.3063 | 0.5130 | 0.1134 | 0.4213 |
313.15 | 0.7643 | 0.2000 | 0.0319 | 0.0782 |
313.15 | 0.6401 | 0.3050 | 0.0404 | 0.1453 |
313.15 | 0.5710 | 0.3593 | 0.0475 | 0.1920 |
313.15 | 0.4277 | 0.4568 | 0.0724 | 0.3089 |
313.15 | 0.4044 | 0.4698 | 0.0783 | 0.3300 |
313.15 | 0.3455 | 0.4973 | 0.0970 | 0.3838 |
313.15 | 0.3027 | 0.5111 | 0.1150 | 0.4221 |
333.15 | 0.7641 | 0.1975 | 0.0346 | 0.0814 |
333.15 | 0.5671 | 0.3592 | 0.0513 | 0.1935 |
333.15 | 0.4403 | 0.4457 | 0.0717 | 0.2978 |
333.15 | 0.4243 | 0.4546 | 0.0748 | 0.3113 |
333.15 | 0.4077 | 0.4610 | 0.0815 | 0.3324 |
333.15 | 0.3406 | 0.4950 | 0.1010 | 0.3852 |
333.15 | 0.2963 | 0.5076 | 0.1190 | 0.4248 |
353.15 | 0.7628 | 0.1951 | 0.0375 | 0.0830 |
353.15 | 0.6380 | 0.2996 | 0.0462 | 0.1513 |
353.15 | 0.5685 | 0.3534 | 0.0535 | 0.1979 |
353.15 | 0.4361 | 0.4431 | 0.0755 | 0.3011 |
353.15 | 0.3960 | 0.4651 | 0.0854 | 0.3349 |
353.15 | 0.3347 | 0.4912 | 0.1057 | 0.3882 |
353.15 | 0.2881 | 0.5034 | 0.1264 | 0.4286 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 1 | Mole fraction of Toluene (1) - Liquid mixture 1 | Mole fraction of Heptane (2) - Liquid mixture 2 | Mole fraction of Toluene (1) - Liquid mixture 2 |
298.15 | 0.7643 | 0.2021 | 0.0300 | 0.0762 |
298.15 | 0.6402 | 0.3071 | 0.0385 | 0.1430 |
298.15 | 0.5715 | 0.3613 | 0.0458 | 0.1897 |
298.15 | 0.4445 | 0.4494 | 0.0674 | 0.2941 |
298.15 | 0.4065 | 0.4714 | 0.0770 | 0.3287 |
298.15 | 0.3565 | 0.4957 | 0.0927 | 0.3753 |
298.15 | 0.3063 | 0.5130 | 0.1134 | 0.4213 |
313.15 | 0.7643 | 0.2000 | 0.0319 | 0.0782 |
313.15 | 0.6401 | 0.3050 | 0.0404 | 0.1453 |
313.15 | 0.5710 | 0.3593 | 0.0475 | 0.1920 |
313.15 | 0.4277 | 0.4568 | 0.0724 | 0.3089 |
313.15 | 0.4044 | 0.4698 | 0.0783 | 0.3300 |
313.15 | 0.3455 | 0.4973 | 0.0970 | 0.3838 |
313.15 | 0.3027 | 0.5111 | 0.1150 | 0.4221 |
333.15 | 0.7641 | 0.1975 | 0.0346 | 0.0814 |
333.15 | 0.5671 | 0.3592 | 0.0513 | 0.1935 |
333.15 | 0.4403 | 0.4457 | 0.0717 | 0.2978 |
333.15 | 0.4243 | 0.4546 | 0.0748 | 0.3113 |
333.15 | 0.4077 | 0.4610 | 0.0815 | 0.3324 |
333.15 | 0.3406 | 0.4950 | 0.1010 | 0.3852 |
333.15 | 0.2963 | 0.5076 | 0.1190 | 0.4248 |
353.15 | 0.7628 | 0.1951 | 0.0375 | 0.0830 |
353.15 | 0.6380 | 0.2996 | 0.0462 | 0.1513 |
353.15 | 0.5685 | 0.3534 | 0.0535 | 0.1979 |
353.15 | 0.4361 | 0.4431 | 0.0755 | 0.3011 |
353.15 | 0.3960 | 0.4651 | 0.0854 | 0.3349 |
353.15 | 0.3347 | 0.4912 | 0.1057 | 0.3882 |
353.15 | 0.2881 | 0.5034 | 0.1264 | 0.4286 |