Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Mass fraction of Decane (2) - Liquid mixture 1 | Mass fraction of Toluene (1) - Liquid mixture 1 |
| 303.15 | 0.0070 | 0.0206 |
| 303.15 | 0.0305 | 0.1267 |
| 303.15 | 0.0893 | 0.2279 |
| 303.15 | 0.1408 | 0.3043 |
| 303.15 | 0.0751 | 0.1948 |
| 303.15 | 0.1846 | 0.3931 |
| 303.15 | 0.2675 | 0.4693 |
| 303.15 | 0.4418 | 0.4477 |
| 303.15 | 0.5800 | 0.3566 |
| 303.15 | 0.7298 | 0.2463 |
| 303.15 | 0.8501 | 0.1309 |
| 303.15 | 0.9455 | 0.0279 |
| 333.15 | 0.0112 | 0.1386 |
| 333.15 | 0.7833 | 0.1963 |
| 333.15 | 0.6694 | 0.2872 |
| 333.15 | 0.5647 | 0.3765 |
| 333.15 | 0.1953 | 0.4028 |
| 333.15 | 0.2850 | 0.4234 |
| 333.15 | 0.1917 | 0.4087 |
| 333.15 | 0.1323 | 0.3515 |
| 333.15 | 0.1882 | 0.4300 |
| 333.15 | 0.1066 | 0.3374 |
| 333.15 | 0.0454 | 0.2018 |
| 333.15 | 0.0856 | 0.2753 |
| 333.15 | 0.0092 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 1 | Mass fraction of Toluene (1) - Liquid mixture 2 | Mass fraction of Decane (2) - Liquid mixture 2 | Mass fraction of Toluene (1) - Liquid mixture 1 | Mass fraction of Decane (2) - Liquid mixture 1 |
| 303.15 | 0.0354 | 0.0077 | 0.1676 | 0.7982 |
| 303.15 | 0.0506 | 0.0162 | 0.2699 | 0.6744 |
| 303.15 | 0.0607 | 0.0218 | 0.3475 | 0.5829 |
| 303.15 | 0.0744 | 0.0292 | 0.4330 | 0.4838 |
| 303.15 | 0.0808 | 0.0326 | 0.4838 | 0.4259 |
| 333.15 | 0.0301 | 0.0222 | 0.1942 | 0.7786 |
| 333.15 | 0.0447 | 0.0195 | 0.2404 | 0.7257 |
| 333.15 | 0.0592 | 0.0172 | 0.2992 | 0.6584 |
| 333.15 | 0.0791 | 0.0148 | 0.3692 | 0.5784 |
| 333.15 | 0.0909 | 0.0138 | 0.4136 | 0.5278 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Mass fraction of Decane (2) - Liquid mixture 1 | Mass fraction of Toluene (1) - Liquid mixture 1 |
| 303.15 | 0.0070 | 0.0206 |
| 303.15 | 0.0305 | 0.1267 |
| 303.15 | 0.0893 | 0.2279 |
| 303.15 | 0.1408 | 0.3043 |
| 303.15 | 0.0751 | 0.1948 |
| 303.15 | 0.1846 | 0.3931 |
| 303.15 | 0.2675 | 0.4693 |
| 303.15 | 0.4418 | 0.4477 |
| 303.15 | 0.5800 | 0.3566 |
| 303.15 | 0.7298 | 0.2463 |
| 303.15 | 0.8501 | 0.1309 |
| 303.15 | 0.9455 | 0.0279 |
| 333.15 | 0.0112 | 0.1386 |
| 333.15 | 0.7833 | 0.1963 |
| 333.15 | 0.6694 | 0.2872 |
| 333.15 | 0.5647 | 0.3765 |
| 333.15 | 0.1953 | 0.4028 |
| 333.15 | 0.2850 | 0.4234 |
| 333.15 | 0.1917 | 0.4087 |
| 333.15 | 0.1323 | 0.3515 |
| 333.15 | 0.1882 | 0.4300 |
| 333.15 | 0.1066 | 0.3374 |
| 333.15 | 0.0454 | 0.2018 |
| 333.15 | 0.0856 | 0.2753 |
| 333.15 | 0.0092 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 1 | Mass fraction of Toluene (1) - Liquid mixture 2 | Mass fraction of Decane (2) - Liquid mixture 2 | Mass fraction of Toluene (1) - Liquid mixture 1 | Mass fraction of Decane (2) - Liquid mixture 1 |
| 303.15 | 0.0354 | 0.0077 | 0.1676 | 0.7982 |
| 303.15 | 0.0506 | 0.0162 | 0.2699 | 0.6744 |
| 303.15 | 0.0607 | 0.0218 | 0.3475 | 0.5829 |
| 303.15 | 0.0744 | 0.0292 | 0.4330 | 0.4838 |
| 303.15 | 0.0808 | 0.0326 | 0.4838 | 0.4259 |
| 333.15 | 0.0301 | 0.0222 | 0.1942 | 0.7786 |
| 333.15 | 0.0447 | 0.0195 | 0.2404 | 0.7257 |
| 333.15 | 0.0592 | 0.0172 | 0.2992 | 0.6584 |
| 333.15 | 0.0791 | 0.0148 | 0.3692 | 0.5784 |
| 333.15 | 0.0909 | 0.0138 | 0.4136 | 0.5278 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mass fraction of Decane (2) - Liquid | Mass fraction of Toluene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0070 | 0.0206 | 1100.44 |
| 303.15 | 0.0305 | 0.1267 | 1074.578 |
| 303.15 | 0.0893 | 0.2279 | 1072.891 |
| 303.15 | 0.1408 | 0.3043 | 1011.921 |
| 303.15 | 0.0751 | 0.1948 | 1065.057 |
| 303.15 | 0.1846 | 0.3931 | 867.165 |
| 303.15 | 0.2675 | 0.4693 | 800.938 |
| 303.15 | 0.4418 | 0.4477 | 783.812 |
| 303.15 | 0.5800 | 0.3566 | 766.984 |
| 303.15 | 0.7298 | 0.2463 | 750.984 |
| 303.15 | 0.8501 | 0.1309 | 737.565 |
| 303.15 | 0.9455 | 0.0279 | 725.737 |
| 333.15 | 0.0112 | 0.1386 | 714.27 |
| 333.15 | 0.7833 | 0.1963 | 720.99 |
| 333.15 | 0.6694 | 0.2872 | 732.598 |
| 333.15 | 0.5647 | 0.3765 | 744.407 |
| 333.15 | 0.1953 | 0.4028 | 757.69 |
| 333.15 | 0.2850 | 0.4234 | 769.354 |
| 333.15 | 0.1917 | 0.4087 | 779.227 |
| 333.15 | 0.1323 | 0.3515 | 794.267 |
| 333.15 | 0.1882 | 0.4300 | 864.175 |
| 333.15 | 0.1066 | 0.3374 | 1019.718 |
| 333.15 | 0.0454 | 0.2018 | 1046.286 |
| 333.15 | 0.0856 | 0.2753 | 1048.992 |
| 333.15 | 0.0092 | 0.0000 | 1084.783 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Mass fraction of Decane (2) - Liquid | Mass fraction of Toluene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0070 | 0.0206 | 1100.44 |
| 303.15 | 0.0305 | 0.1267 | 1074.578 |
| 303.15 | 0.0893 | 0.2279 | 1072.891 |
| 303.15 | 0.1408 | 0.3043 | 1011.921 |
| 303.15 | 0.0751 | 0.1948 | 1065.057 |
| 303.15 | 0.1846 | 0.3931 | 867.165 |
| 303.15 | 0.2675 | 0.4693 | 800.938 |
| 303.15 | 0.4418 | 0.4477 | 783.812 |
| 303.15 | 0.5800 | 0.3566 | 766.984 |
| 303.15 | 0.7298 | 0.2463 | 750.984 |
| 303.15 | 0.8501 | 0.1309 | 737.565 |
| 303.15 | 0.9455 | 0.0279 | 725.737 |
| 333.15 | 0.0112 | 0.1386 | 714.27 |
| 333.15 | 0.7833 | 0.1963 | 720.99 |
| 333.15 | 0.6694 | 0.2872 | 732.598 |
| 333.15 | 0.5647 | 0.3765 | 744.407 |
| 333.15 | 0.1953 | 0.4028 | 757.69 |
| 333.15 | 0.2850 | 0.4234 | 769.354 |
| 333.15 | 0.1917 | 0.4087 | 779.227 |
| 333.15 | 0.1323 | 0.3515 | 794.267 |
| 333.15 | 0.1882 | 0.4300 | 864.175 |
| 333.15 | 0.1066 | 0.3374 | 1019.718 |
| 333.15 | 0.0454 | 0.2018 | 1046.286 |
| 333.15 | 0.0856 | 0.2753 | 1048.992 |
| 333.15 | 0.0092 | 0.0000 | 1084.783 |