Operational conditions:
| Mole fraction of p-Xylene (2) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0004 |
| 0.0429 | 0.0004 |
| 0.1074 | 0.0004 |
| 0.2235 | 0.0004 |
| 0.3501 | 0.0005 |
| 0.4895 | 0.0005 |
| 0.6419 | 0.0005 |
| 0.8117 | 0.0006 |
| 0.9213 | 0.0006 |
| 1.0000 | 0.0006 |
Operational conditions:
| Mole fraction of p-Xylene (2) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0004 |
| 0.0429 | 0.0004 |
| 0.1074 | 0.0004 |
| 0.2235 | 0.0004 |
| 0.3501 | 0.0005 |
| 0.4895 | 0.0005 |
| 0.6419 | 0.0005 |
| 0.8117 | 0.0006 |
| 0.9213 | 0.0006 |
| 1.0000 | 0.0006 |
Operational conditions:
| Mole fraction of p-Xylene (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 799.6 |
| 0.0429 | 806.0 |
| 0.1074 | 813.8 |
| 0.2235 | 823.5 |
| 0.3501 | 830.4 |
| 0.4895 | 836.6 |
| 0.6419 | 842.9 |
| 0.8117 | 849.6 |
| 0.9213 | 853.2 |
| 1.0000 | 856.1 |
Operational conditions:
| Mole fraction of p-Xylene (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 799.6 |
| 0.0429 | 806.0 |
| 0.1074 | 813.8 |
| 0.2235 | 823.5 |
| 0.3501 | 830.4 |
| 0.4895 | 836.6 |
| 0.6419 | 842.9 |
| 0.8117 | 849.6 |
| 0.9213 | 853.2 |
| 1.0000 | 856.1 |
Operational conditions:
| Mole fraction of p-Xylene (2) - Liquid | Speed of sound, m/s - Liquid |
|---|---|
| 0.0000 | 1195.0 |
| 0.0429 | 1218.0 |
| 0.1074 | 1237.0 |
| 0.2235 | 1257.0 |
| 0.3501 | 1272.0 |
| 0.4895 | 1289.0 |
| 0.6419 | 1299.0 |
| 0.8117 | 1308.0 |
| 0.9213 | 1313.0 |
| 1.0000 | 1316.0 |
Operational conditions:
| Mole fraction of p-Xylene (2) - Liquid | Speed of sound, m/s - Liquid |
|---|---|
| 0.0000 | 1195.0 |
| 0.0429 | 1218.0 |
| 0.1074 | 1237.0 |
| 0.2235 | 1257.0 |
| 0.3501 | 1272.0 |
| 0.4895 | 1289.0 |
| 0.6419 | 1299.0 |
| 0.8117 | 1308.0 |
| 0.9213 | 1313.0 |
| 1.0000 | 1316.0 |
Operational condition: Temperature, K = 298.15 (Liquid)
| Mole fraction of 2-Butanone (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0999 | 0.0276 |
| 0.2007 | 0.0273 |
| 0.3001 | 0.0270 |
| 0.4020 | 0.0266 |
| 0.5001 | 0.0263 |
| 0.6006 | 0.0259 |
| 0.7009 | 0.0255 |
| 0.8009 | 0.0251 |
| 0.8999 | 0.0247 |
Operational condition: Temperature, K = 298.15 (Liquid)
| Mole fraction of 2-Butanone (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 0.0999 | 0.0276 |
| 0.2007 | 0.0273 |
| 0.3001 | 0.0270 |
| 0.4020 | 0.0266 |
| 0.5001 | 0.0263 |
| 0.6006 | 0.0259 |
| 0.7009 | 0.0255 |
| 0.8009 | 0.0251 |
| 0.8999 | 0.0247 |
Operational conditions:
| Mole fraction of 2-Butanone (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0502 | -3.3000e-08 |
| 0.1002 | -6.5000e-08 |
| 0.1505 | -9.0000e-08 |
| 0.1996 | -1.1300e-07 |
| 0.2499 | -1.3500e-07 |
| 0.2991 | -1.5700e-07 |
| 0.3502 | -1.7000e-07 |
| 0.4003 | -1.8300e-07 |
| 0.4504 | -1.9200e-07 |
| 0.4998 | -1.9500e-07 |
| 0.5505 | -1.9100e-07 |
| 0.5999 | -1.8800e-07 |
| 0.6598 | -1.7700e-07 |
| 0.7002 | -1.7200e-07 |
| 0.7504 | -1.5400e-07 |
| 0.7997 | -1.3900e-07 |
| 0.8506 | -1.0800e-07 |
| 0.8993 | -8.0000e-08 |
| 0.9481 | -4.8000e-08 |
Operational conditions:
| Mole fraction of 2-Butanone (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0502 | -3.3000e-08 |
| 0.1002 | -6.5000e-08 |
| 0.1505 | -9.0000e-08 |
| 0.1996 | -1.1300e-07 |
| 0.2499 | -1.3500e-07 |
| 0.2991 | -1.5700e-07 |
| 0.3502 | -1.7000e-07 |
| 0.4003 | -1.8300e-07 |
| 0.4504 | -1.9200e-07 |
| 0.4998 | -1.9500e-07 |
| 0.5505 | -1.9100e-07 |
| 0.5999 | -1.8800e-07 |
| 0.6598 | -1.7700e-07 |
| 0.7002 | -1.7200e-07 |
| 0.7504 | -1.5400e-07 |
| 0.7997 | -1.3900e-07 |
| 0.8506 | -1.0800e-07 |
| 0.8993 | -8.0000e-08 |
| 0.9481 | -4.8000e-08 |