Datasets
-
η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Toluene (1) - Liquid |
Viscosity, Pa*s - Liquid |
308.15 |
0.0000 |
0.0006 |
308.15 |
0.0424 |
0.0006 |
308.15 |
0.1280 |
0.0006 |
308.15 |
0.2164 |
0.0005 |
308.15 |
0.2928 |
0.0005 |
308.15 |
0.3930 |
0.0005 |
308.15 |
0.4922 |
0.0005 |
308.15 |
0.5716 |
0.0005 |
308.15 |
0.7107 |
0.0005 |
308.15 |
0.8425 |
0.0005 |
308.15 |
1.0000 |
0.0005 |
313.15 |
0.0000 |
0.0005 |
313.15 |
0.0424 |
0.0005 |
313.15 |
0.1280 |
0.0005 |
313.15 |
0.2164 |
0.0005 |
313.15 |
0.2928 |
0.0005 |
313.15 |
0.3930 |
0.0005 |
313.15 |
0.4922 |
0.0005 |
313.15 |
0.5716 |
0.0005 |
313.15 |
0.7107 |
0.0005 |
313.15 |
0.8425 |
0.0005 |
313.15 |
1.0000 |
0.0005 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Toluene (1) - Liquid |
Viscosity, Pa*s - Liquid |
308.15 |
0.0000 |
0.0006 |
308.15 |
0.0424 |
0.0006 |
308.15 |
0.1280 |
0.0006 |
308.15 |
0.2164 |
0.0005 |
308.15 |
0.2928 |
0.0005 |
308.15 |
0.3930 |
0.0005 |
308.15 |
0.4922 |
0.0005 |
308.15 |
0.5716 |
0.0005 |
308.15 |
0.7107 |
0.0005 |
308.15 |
0.8425 |
0.0005 |
308.15 |
1.0000 |
0.0005 |
313.15 |
0.0000 |
0.0005 |
313.15 |
0.0424 |
0.0005 |
313.15 |
0.1280 |
0.0005 |
313.15 |
0.2164 |
0.0005 |
313.15 |
0.2928 |
0.0005 |
313.15 |
0.3930 |
0.0005 |
313.15 |
0.4922 |
0.0005 |
313.15 |
0.5716 |
0.0005 |
313.15 |
0.7107 |
0.0005 |
313.15 |
0.8425 |
0.0005 |
313.15 |
1.0000 |
0.0005 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Toluene (1) - Liquid |
Mass density, kg/m3 - Liquid |
308.15 |
0.0000 |
853.7 |
308.15 |
0.0424 |
853.7 |
308.15 |
0.1280 |
853.7 |
308.15 |
0.2164 |
853.6 |
308.15 |
0.2928 |
853.6 |
308.15 |
0.3930 |
853.5 |
308.15 |
0.4922 |
853.4 |
308.15 |
0.5716 |
853.4 |
308.15 |
0.7107 |
853.2 |
308.15 |
0.8425 |
853.0 |
308.15 |
1.0000 |
852.8 |
318.15 |
0.0000 |
849.5 |
318.15 |
0.0424 |
849.5 |
318.15 |
0.1280 |
849.4 |
318.15 |
0.2164 |
849.3 |
318.15 |
0.2928 |
849.3 |
318.15 |
0.3930 |
849.2 |
318.15 |
0.4922 |
849.1 |
318.15 |
0.5716 |
849.0 |
318.15 |
0.7107 |
848.8 |
318.15 |
0.8425 |
848.6 |
318.15 |
1.0000 |
848.3 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Toluene (1) - Liquid |
Mass density, kg/m3 - Liquid |
308.15 |
0.0000 |
853.7 |
308.15 |
0.0424 |
853.7 |
308.15 |
0.1280 |
853.7 |
308.15 |
0.2164 |
853.6 |
308.15 |
0.2928 |
853.6 |
308.15 |
0.3930 |
853.5 |
308.15 |
0.4922 |
853.4 |
308.15 |
0.5716 |
853.4 |
308.15 |
0.7107 |
853.2 |
308.15 |
0.8425 |
853.0 |
308.15 |
1.0000 |
852.8 |
318.15 |
0.0000 |
849.5 |
318.15 |
0.0424 |
849.5 |
318.15 |
0.1280 |
849.4 |
318.15 |
0.2164 |
849.3 |
318.15 |
0.2928 |
849.3 |
318.15 |
0.3930 |
849.2 |
318.15 |
0.4922 |
849.1 |
318.15 |
0.5716 |
849.0 |
318.15 |
0.7107 |
848.8 |
318.15 |
0.8425 |
848.6 |
318.15 |
1.0000 |
848.3 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Toluene (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
26.66 |
0.0000 |
365.86 |
26.66 |
0.1880 |
360.27 |
26.66 |
0.3160 |
357.03 |
26.66 |
0.3230 |
356.78 |
26.66 |
0.3790 |
355.73 |
26.66 |
0.4340 |
353.90 |
26.66 |
0.4470 |
353.73 |
26.66 |
0.5130 |
352.10 |
26.66 |
0.6060 |
350.23 |
26.66 |
0.7020 |
348.12 |
26.66 |
0.7730 |
346.68 |
26.66 |
0.8720 |
344.99 |
26.66 |
1.0000 |
342.65 |
53.33 |
0.0000 |
386.94 |
53.33 |
0.1880 |
381.34 |
53.33 |
0.3160 |
377.91 |
53.33 |
0.3230 |
377.68 |
53.33 |
0.3790 |
376.48 |
53.33 |
0.4340 |
374.66 |
53.33 |
0.4470 |
374.36 |
53.33 |
0.5130 |
372.72 |
53.33 |
0.6060 |
370.67 |
53.33 |
0.7020 |
368.52 |
53.33 |
0.7730 |
366.97 |
53.33 |
0.8720 |
365.13 |
53.33 |
1.0000 |
362.63 |
79.99 |
0.0000 |
400.70 |
79.99 |
0.1880 |
395.07 |
79.99 |
0.3160 |
391.40 |
79.99 |
0.3230 |
391.30 |
79.99 |
0.3790 |
389.97 |
79.99 |
0.4340 |
388.23 |
79.99 |
0.4470 |
387.90 |
79.99 |
0.5130 |
386.16 |
79.99 |
0.6060 |
384.07 |
79.99 |
0.7020 |
381.78 |
79.99 |
0.7730 |
380.16 |
79.99 |
0.8720 |
378.23 |
79.99 |
1.0000 |
375.66 |
101.32 |
0.0000 |
409.31 |
101.32 |
0.1880 |
403.63 |
101.32 |
0.3160 |
399.88 |
101.32 |
0.3230 |
399.80 |
101.32 |
0.3790 |
398.43 |
101.32 |
0.4340 |
396.67 |
101.32 |
0.4470 |
396.30 |
101.32 |
0.5130 |
394.47 |
101.32 |
0.6060 |
392.38 |
101.32 |
0.7020 |
389.83 |
101.32 |
0.7730 |
388.37 |
101.32 |
0.8720 |
386.37 |
101.32 |
1.0000 |
383.76 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Mole fraction of Toluene (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
26.66 |
0.0000 |
365.86 |
26.66 |
0.1880 |
360.27 |
26.66 |
0.3160 |
357.03 |
26.66 |
0.3230 |
356.78 |
26.66 |
0.3790 |
355.73 |
26.66 |
0.4340 |
353.90 |
26.66 |
0.4470 |
353.73 |
26.66 |
0.5130 |
352.10 |
26.66 |
0.6060 |
350.23 |
26.66 |
0.7020 |
348.12 |
26.66 |
0.7730 |
346.68 |
26.66 |
0.8720 |
344.99 |
26.66 |
1.0000 |
342.65 |
53.33 |
0.0000 |
386.94 |
53.33 |
0.1880 |
381.34 |
53.33 |
0.3160 |
377.91 |
53.33 |
0.3230 |
377.68 |
53.33 |
0.3790 |
376.48 |
53.33 |
0.4340 |
374.66 |
53.33 |
0.4470 |
374.36 |
53.33 |
0.5130 |
372.72 |
53.33 |
0.6060 |
370.67 |
53.33 |
0.7020 |
368.52 |
53.33 |
0.7730 |
366.97 |
53.33 |
0.8720 |
365.13 |
53.33 |
1.0000 |
362.63 |
79.99 |
0.0000 |
400.70 |
79.99 |
0.1880 |
395.07 |
79.99 |
0.3160 |
391.40 |
79.99 |
0.3230 |
391.30 |
79.99 |
0.3790 |
389.97 |
79.99 |
0.4340 |
388.23 |
79.99 |
0.4470 |
387.90 |
79.99 |
0.5130 |
386.16 |
79.99 |
0.6060 |
384.07 |
79.99 |
0.7020 |
381.78 |
79.99 |
0.7730 |
380.16 |
79.99 |
0.8720 |
378.23 |
79.99 |
1.0000 |
375.66 |
101.32 |
0.0000 |
409.31 |
101.32 |
0.1880 |
403.63 |
101.32 |
0.3160 |
399.88 |
101.32 |
0.3230 |
399.80 |
101.32 |
0.3790 |
398.43 |
101.32 |
0.4340 |
396.67 |
101.32 |
0.4470 |
396.30 |
101.32 |
0.5130 |
394.47 |
101.32 |
0.6060 |
392.38 |
101.32 |
0.7020 |
389.83 |
101.32 |
0.7730 |
388.37 |
101.32 |
0.8720 |
386.37 |
101.32 |
1.0000 |
383.76 |
Sources