Datasets
-
Mole fraction (6)
-
η - Viscosity, Pa*s (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (2)
-
Tboil - Boiling temperature at pressure P, K (6)
-
Vapor Liquid Equilibrium at Constant Pressure
-
Vapor Liquid Equilibrium at Constant Temperature (2)
Mole fraction of Acetone (2)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Mole fraction of Acetone (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0440 |
0.1290 |
| 0.0850 |
0.2320 |
| 0.1320 |
0.3250 |
| 0.1750 |
0.4030 |
| 0.2270 |
0.4630 |
| 0.2760 |
0.5170 |
| 0.3280 |
0.5710 |
| 0.3800 |
0.6090 |
| 0.4330 |
0.6510 |
| 0.4810 |
0.6850 |
| 0.5380 |
0.7190 |
| 0.5860 |
0.7490 |
| 0.6390 |
0.7770 |
| 0.6880 |
0.8030 |
| 0.7450 |
0.8350 |
| 0.7960 |
0.8670 |
| 0.8490 |
0.8980 |
| 0.9010 |
0.9290 |
| 0.9510 |
0.9650 |
| 1.0000 |
1.0000 |
Mole fraction of Acetone (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Acetone (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Acetone (2) - Gas |
| 0.0000 |
351.55 |
0.0000 |
| 0.0714 |
348.20 |
0.2086 |
| 0.1480 |
345.35 |
0.3438 |
| 0.2107 |
343.25 |
0.4312 |
| 0.3242 |
339.90 |
0.5504 |
| 0.3928 |
338.35 |
0.6107 |
| 0.5016 |
336.05 |
0.6872 |
| 0.6343 |
333.80 |
0.7699 |
| 0.7779 |
331.80 |
0.8571 |
| 0.8977 |
330.30 |
0.9346 |
| 1.0000 |
329.35 |
1.0000 |
Mole fraction of Acetone (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Mole fraction of Acetone (2) - Gas |
| 1.0000 |
1.0000 |
| 0.8910 |
0.9330 |
| 0.7430 |
0.8420 |
| 0.6590 |
0.7900 |
| 0.5640 |
0.7350 |
| 0.4950 |
0.6800 |
| 0.4020 |
0.6240 |
| 0.3260 |
0.5600 |
| 0.2400 |
0.4740 |
| 0.1660 |
0.3910 |
| 0.1100 |
0.2910 |
| 0.0760 |
0.2270 |
| 0.0000 |
0.0000 |
Mole fraction of Acetone (2)
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Mole fraction of Acetone (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0440 |
0.1290 |
| 0.0850 |
0.2320 |
| 0.1320 |
0.3250 |
| 0.1750 |
0.4030 |
| 0.2270 |
0.4630 |
| 0.2760 |
0.5170 |
| 0.3280 |
0.5710 |
| 0.3800 |
0.6090 |
| 0.4330 |
0.6510 |
| 0.4810 |
0.6850 |
| 0.5380 |
0.7190 |
| 0.5860 |
0.7490 |
| 0.6390 |
0.7770 |
| 0.6880 |
0.8030 |
| 0.7450 |
0.8350 |
| 0.7960 |
0.8670 |
| 0.8490 |
0.8980 |
| 0.9010 |
0.9290 |
| 0.9510 |
0.9650 |
| 1.0000 |
1.0000 |
Mole fraction of Acetone (2)
[ref]
| Fixed |
Measured |
| Mole fraction of Acetone (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of Acetone (2) - Gas |
| 0.0000 |
351.55 |
0.0000 |
| 0.0714 |
348.20 |
0.2086 |
| 0.1480 |
345.35 |
0.3438 |
| 0.2107 |
343.25 |
0.4312 |
| 0.3242 |
339.90 |
0.5504 |
| 0.3928 |
338.35 |
0.6107 |
| 0.5016 |
336.05 |
0.6872 |
| 0.6343 |
333.80 |
0.7699 |
| 0.7779 |
331.80 |
0.8571 |
| 0.8977 |
330.30 |
0.9346 |
| 1.0000 |
329.35 |
1.0000 |
Mole fraction of Acetone (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Mole fraction of Acetone (2) - Gas |
| 1.0000 |
1.0000 |
| 0.8910 |
0.9330 |
| 0.7430 |
0.8420 |
| 0.6590 |
0.7900 |
| 0.5640 |
0.7350 |
| 0.4950 |
0.6800 |
| 0.4020 |
0.6240 |
| 0.3260 |
0.5600 |
| 0.2400 |
0.4740 |
| 0.1660 |
0.3910 |
| 0.1100 |
0.2910 |
| 0.0760 |
0.2270 |
| 0.0000 |
0.0000 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Viscosity, Pa*s - Liquid |
| 288.15 |
0.0000 |
0.0013 |
| 288.15 |
0.0500 |
0.0011 |
| 288.15 |
0.1000 |
0.0010 |
| 288.15 |
0.1500 |
0.0009 |
| 288.15 |
0.2000 |
0.0008 |
| 288.15 |
0.2500 |
0.0007 |
| 288.15 |
0.3000 |
0.0006 |
| 288.15 |
0.3500 |
0.0006 |
| 288.15 |
0.4000 |
0.0006 |
| 288.15 |
0.4500 |
0.0005 |
| 288.15 |
0.4999 |
0.0005 |
| 288.15 |
0.5500 |
0.0005 |
| 288.15 |
0.6000 |
0.0004 |
| 288.15 |
0.6500 |
0.0004 |
| 288.15 |
0.7000 |
0.0004 |
| 288.15 |
0.7500 |
0.0004 |
| 288.15 |
0.8000 |
0.0004 |
| 288.15 |
0.8501 |
0.0004 |
| 288.15 |
0.9000 |
0.0004 |
| 288.15 |
0.9500 |
0.0003 |
| 288.15 |
1.0000 |
0.0003 |
| 298.15 |
0.0000 |
0.0011 |
| 298.15 |
0.0500 |
0.0009 |
| 298.15 |
0.1000 |
0.0008 |
| 298.15 |
0.1500 |
0.0007 |
| 298.15 |
0.2000 |
0.0007 |
| 298.15 |
0.2500 |
0.0006 |
| 298.15 |
0.3000 |
0.0006 |
| 298.15 |
0.3500 |
0.0005 |
| 298.15 |
0.4000 |
0.0005 |
| 298.15 |
0.4500 |
0.0005 |
| 298.15 |
0.4999 |
0.0004 |
| 298.15 |
0.5500 |
0.0004 |
| 298.15 |
0.6000 |
0.0004 |
| 298.15 |
0.6500 |
0.0004 |
| 298.15 |
0.7000 |
0.0004 |
| 298.15 |
0.7500 |
0.0003 |
| 298.15 |
0.8000 |
0.0003 |
| 298.15 |
0.8501 |
0.0003 |
| 298.15 |
0.9000 |
0.0003 |
| 298.15 |
0.9500 |
0.0003 |
| 298.15 |
1.0000 |
0.0003 |
| 308.15 |
0.0000 |
0.0009 |
| 308.15 |
0.0500 |
0.0008 |
| 308.15 |
0.1000 |
0.0007 |
| 308.15 |
0.1500 |
0.0006 |
| 308.15 |
0.2000 |
0.0006 |
| 308.15 |
0.2500 |
0.0005 |
| 308.15 |
0.3000 |
0.0005 |
| 308.15 |
0.3500 |
0.0005 |
| 308.15 |
0.4000 |
0.0004 |
| 308.15 |
0.4500 |
0.0004 |
| 308.15 |
0.4999 |
0.0004 |
| 308.15 |
0.5500 |
0.0004 |
| 308.15 |
0.6000 |
0.0003 |
| 308.15 |
0.6500 |
0.0003 |
| 308.15 |
0.7000 |
0.0003 |
| 308.15 |
0.7500 |
0.0003 |
| 308.15 |
0.8000 |
0.0003 |
| 308.15 |
0.8501 |
0.0003 |
| 308.15 |
0.9000 |
0.0003 |
| 308.15 |
0.9500 |
0.0003 |
| 308.15 |
1.0000 |
0.0003 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Viscosity, Pa*s - Liquid |
| 288.15 |
0.0000 |
0.0013 |
| 288.15 |
0.0500 |
0.0011 |
| 288.15 |
0.1000 |
0.0010 |
| 288.15 |
0.1500 |
0.0009 |
| 288.15 |
0.2000 |
0.0008 |
| 288.15 |
0.2500 |
0.0007 |
| 288.15 |
0.3000 |
0.0006 |
| 288.15 |
0.3500 |
0.0006 |
| 288.15 |
0.4000 |
0.0006 |
| 288.15 |
0.4500 |
0.0005 |
| 288.15 |
0.4999 |
0.0005 |
| 288.15 |
0.5500 |
0.0005 |
| 288.15 |
0.6000 |
0.0004 |
| 288.15 |
0.6500 |
0.0004 |
| 288.15 |
0.7000 |
0.0004 |
| 288.15 |
0.7500 |
0.0004 |
| 288.15 |
0.8000 |
0.0004 |
| 288.15 |
0.8501 |
0.0004 |
| 288.15 |
0.9000 |
0.0004 |
| 288.15 |
0.9500 |
0.0003 |
| 288.15 |
1.0000 |
0.0003 |
| 298.15 |
0.0000 |
0.0011 |
| 298.15 |
0.0500 |
0.0009 |
| 298.15 |
0.1000 |
0.0008 |
| 298.15 |
0.1500 |
0.0007 |
| 298.15 |
0.2000 |
0.0007 |
| 298.15 |
0.2500 |
0.0006 |
| 298.15 |
0.3000 |
0.0006 |
| 298.15 |
0.3500 |
0.0005 |
| 298.15 |
0.4000 |
0.0005 |
| 298.15 |
0.4500 |
0.0005 |
| 298.15 |
0.4999 |
0.0004 |
| 298.15 |
0.5500 |
0.0004 |
| 298.15 |
0.6000 |
0.0004 |
| 298.15 |
0.6500 |
0.0004 |
| 298.15 |
0.7000 |
0.0004 |
| 298.15 |
0.7500 |
0.0003 |
| 298.15 |
0.8000 |
0.0003 |
| 298.15 |
0.8501 |
0.0003 |
| 298.15 |
0.9000 |
0.0003 |
| 298.15 |
0.9500 |
0.0003 |
| 298.15 |
1.0000 |
0.0003 |
| 308.15 |
0.0000 |
0.0009 |
| 308.15 |
0.0500 |
0.0008 |
| 308.15 |
0.1000 |
0.0007 |
| 308.15 |
0.1500 |
0.0006 |
| 308.15 |
0.2000 |
0.0006 |
| 308.15 |
0.2500 |
0.0005 |
| 308.15 |
0.3000 |
0.0005 |
| 308.15 |
0.3500 |
0.0005 |
| 308.15 |
0.4000 |
0.0004 |
| 308.15 |
0.4500 |
0.0004 |
| 308.15 |
0.4999 |
0.0004 |
| 308.15 |
0.5500 |
0.0004 |
| 308.15 |
0.6000 |
0.0003 |
| 308.15 |
0.6500 |
0.0003 |
| 308.15 |
0.7000 |
0.0003 |
| 308.15 |
0.7500 |
0.0003 |
| 308.15 |
0.8000 |
0.0003 |
| 308.15 |
0.8501 |
0.0003 |
| 308.15 |
0.9000 |
0.0003 |
| 308.15 |
0.9500 |
0.0003 |
| 308.15 |
1.0000 |
0.0003 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 323.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0500 |
0.2550 |
| 0.1020 |
0.4830 |
| 0.1500 |
0.6520 |
| 0.2000 |
0.8050 |
| 0.2520 |
0.9280 |
| 0.3000 |
1.018 |
| 0.3520 |
1.085 |
| 0.4000 |
1.124 |
| 0.4520 |
1.144 |
| 0.5010 |
1.139 |
| 0.5510 |
1.109 |
| 0.6000 |
1.066 |
| 0.6500 |
1.005 |
| 0.7020 |
0.9190 |
| 0.7520 |
0.8180 |
| 0.8000 |
0.7010 |
| 0.8500 |
0.5600 |
| 0.9010 |
0.3920 |
| 0.9500 |
0.2110 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 323.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0500 |
0.2550 |
| 0.1020 |
0.4830 |
| 0.1500 |
0.6520 |
| 0.2000 |
0.8050 |
| 0.2520 |
0.9280 |
| 0.3000 |
1.018 |
| 0.3520 |
1.085 |
| 0.4000 |
1.124 |
| 0.4520 |
1.144 |
| 0.5010 |
1.139 |
| 0.5510 |
1.109 |
| 0.6000 |
1.066 |
| 0.6500 |
1.005 |
| 0.7020 |
0.9190 |
| 0.7520 |
0.8180 |
| 0.8000 |
0.7010 |
| 0.8500 |
0.5600 |
| 0.9010 |
0.3920 |
| 0.9500 |
0.2110 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Refractive index (Na D-line) - Liquid |
| 288.15 |
0.0000 |
1.3634 |
| 288.15 |
0.0500 |
1.3635 |
| 288.15 |
0.1000 |
1.3636 |
| 288.15 |
0.1500 |
1.3637 |
| 288.15 |
0.2000 |
1.3636 |
| 288.15 |
0.2500 |
1.3636 |
| 288.15 |
0.3000 |
1.3635 |
| 288.15 |
0.3500 |
1.3634 |
| 288.15 |
0.4000 |
1.3633 |
| 288.15 |
0.4500 |
1.3632 |
| 288.15 |
0.4999 |
1.3631 |
| 288.15 |
0.5500 |
1.363 |
| 288.15 |
0.6000 |
1.3629 |
| 288.15 |
0.6500 |
1.3627 |
| 288.15 |
0.7000 |
1.3626 |
| 288.15 |
0.7500 |
1.3625 |
| 288.15 |
0.8000 |
1.3623 |
| 288.15 |
0.8501 |
1.3621 |
| 288.15 |
0.9000 |
1.362 |
| 288.15 |
0.9500 |
1.3618 |
| 288.15 |
1.0000 |
1.3615 |
| 298.15 |
0.0000 |
1.3592 |
| 298.15 |
0.0500 |
1.3592 |
| 298.15 |
0.1000 |
1.3592 |
| 298.15 |
0.1500 |
1.3591 |
| 298.15 |
0.2000 |
1.359 |
| 298.15 |
0.2500 |
1.3589 |
| 298.15 |
0.3000 |
1.3587 |
| 298.15 |
0.3500 |
1.3586 |
| 298.15 |
0.4000 |
1.3584 |
| 298.15 |
0.4500 |
1.3583 |
| 298.15 |
0.4999 |
1.3581 |
| 298.15 |
0.5500 |
1.3579 |
| 298.15 |
0.6000 |
1.3577 |
| 298.15 |
0.6500 |
1.3575 |
| 298.15 |
0.7000 |
1.3573 |
| 298.15 |
0.7500 |
1.3571 |
| 298.15 |
0.8000 |
1.3569 |
| 298.15 |
0.8501 |
1.3567 |
| 298.15 |
0.9000 |
1.3565 |
| 298.15 |
0.9500 |
1.3563 |
| 298.15 |
1.0000 |
1.356 |
| 308.15 |
0.0000 |
1.355 |
| 308.15 |
0.0500 |
1.3549 |
| 308.15 |
0.1000 |
1.3547 |
| 308.15 |
0.1500 |
1.3545 |
| 308.15 |
0.2000 |
1.3543 |
| 308.15 |
0.2500 |
1.3541 |
| 308.15 |
0.3000 |
1.3539 |
| 308.15 |
0.3500 |
1.3537 |
| 308.15 |
0.4000 |
1.3535 |
| 308.15 |
0.4500 |
1.3532 |
| 308.15 |
0.4999 |
1.353 |
| 308.15 |
0.5500 |
1.3528 |
| 308.15 |
0.6000 |
1.3525 |
| 308.15 |
0.6500 |
1.3523 |
| 308.15 |
0.7000 |
1.352 |
| 308.15 |
0.7500 |
1.3518 |
| 308.15 |
0.8000 |
1.3515 |
| 308.15 |
0.8501 |
1.3513 |
| 308.15 |
0.9000 |
1.351 |
| 308.15 |
0.9500 |
1.3508 |
| 308.15 |
1.0000 |
1.3506 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Refractive index (Na D-line) - Liquid |
| 288.15 |
0.0000 |
1.3634 |
| 288.15 |
0.0500 |
1.3635 |
| 288.15 |
0.1000 |
1.3636 |
| 288.15 |
0.1500 |
1.3637 |
| 288.15 |
0.2000 |
1.3636 |
| 288.15 |
0.2500 |
1.3636 |
| 288.15 |
0.3000 |
1.3635 |
| 288.15 |
0.3500 |
1.3634 |
| 288.15 |
0.4000 |
1.3633 |
| 288.15 |
0.4500 |
1.3632 |
| 288.15 |
0.4999 |
1.3631 |
| 288.15 |
0.5500 |
1.363 |
| 288.15 |
0.6000 |
1.3629 |
| 288.15 |
0.6500 |
1.3627 |
| 288.15 |
0.7000 |
1.3626 |
| 288.15 |
0.7500 |
1.3625 |
| 288.15 |
0.8000 |
1.3623 |
| 288.15 |
0.8501 |
1.3621 |
| 288.15 |
0.9000 |
1.362 |
| 288.15 |
0.9500 |
1.3618 |
| 288.15 |
1.0000 |
1.3615 |
| 298.15 |
0.0000 |
1.3592 |
| 298.15 |
0.0500 |
1.3592 |
| 298.15 |
0.1000 |
1.3592 |
| 298.15 |
0.1500 |
1.3591 |
| 298.15 |
0.2000 |
1.359 |
| 298.15 |
0.2500 |
1.3589 |
| 298.15 |
0.3000 |
1.3587 |
| 298.15 |
0.3500 |
1.3586 |
| 298.15 |
0.4000 |
1.3584 |
| 298.15 |
0.4500 |
1.3583 |
| 298.15 |
0.4999 |
1.3581 |
| 298.15 |
0.5500 |
1.3579 |
| 298.15 |
0.6000 |
1.3577 |
| 298.15 |
0.6500 |
1.3575 |
| 298.15 |
0.7000 |
1.3573 |
| 298.15 |
0.7500 |
1.3571 |
| 298.15 |
0.8000 |
1.3569 |
| 298.15 |
0.8501 |
1.3567 |
| 298.15 |
0.9000 |
1.3565 |
| 298.15 |
0.9500 |
1.3563 |
| 298.15 |
1.0000 |
1.356 |
| 308.15 |
0.0000 |
1.355 |
| 308.15 |
0.0500 |
1.3549 |
| 308.15 |
0.1000 |
1.3547 |
| 308.15 |
0.1500 |
1.3545 |
| 308.15 |
0.2000 |
1.3543 |
| 308.15 |
0.2500 |
1.3541 |
| 308.15 |
0.3000 |
1.3539 |
| 308.15 |
0.3500 |
1.3537 |
| 308.15 |
0.4000 |
1.3535 |
| 308.15 |
0.4500 |
1.3532 |
| 308.15 |
0.4999 |
1.353 |
| 308.15 |
0.5500 |
1.3528 |
| 308.15 |
0.6000 |
1.3525 |
| 308.15 |
0.6500 |
1.3523 |
| 308.15 |
0.7000 |
1.352 |
| 308.15 |
0.7500 |
1.3518 |
| 308.15 |
0.8000 |
1.3515 |
| 308.15 |
0.8501 |
1.3513 |
| 308.15 |
0.9000 |
1.351 |
| 308.15 |
0.9500 |
1.3508 |
| 308.15 |
1.0000 |
1.3506 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.0000 |
793.74 |
| 288.15 |
0.0500 |
794.4 |
| 288.15 |
0.1000 |
794.86 |
| 288.15 |
0.1500 |
795.23 |
| 288.15 |
0.2000 |
795.5 |
| 288.15 |
0.2500 |
795.75 |
| 288.15 |
0.3000 |
795.99 |
| 288.15 |
0.3500 |
796.18 |
| 288.15 |
0.4000 |
796.34 |
| 288.15 |
0.4500 |
796.46 |
| 288.15 |
0.4999 |
796.57 |
| 288.15 |
0.5500 |
796.68 |
| 288.15 |
0.6000 |
796.77 |
| 288.15 |
0.6500 |
796.84 |
| 288.15 |
0.7000 |
796.86 |
| 288.15 |
0.7500 |
796.88 |
| 288.15 |
0.8000 |
796.91 |
| 288.15 |
0.8501 |
796.9 |
| 288.15 |
0.9000 |
796.92 |
| 288.15 |
0.9500 |
796.91 |
| 288.15 |
1.0000 |
796.87 |
| 298.15 |
0.0000 |
785.17 |
| 298.15 |
0.0500 |
785.59 |
| 298.15 |
0.1000 |
785.84 |
| 298.15 |
0.1500 |
786.0 |
| 298.15 |
0.2000 |
786.08 |
| 298.15 |
0.2500 |
786.16 |
| 298.15 |
0.3000 |
786.23 |
| 298.15 |
0.3500 |
786.24 |
| 298.15 |
0.4000 |
786.23 |
| 298.15 |
0.4500 |
786.21 |
| 298.15 |
0.4999 |
786.19 |
| 298.15 |
0.5500 |
786.17 |
| 298.15 |
0.6000 |
786.13 |
| 298.15 |
0.6500 |
786.07 |
| 298.15 |
0.7000 |
786.0 |
| 298.15 |
0.7500 |
785.9 |
| 298.15 |
0.8000 |
785.84 |
| 298.15 |
0.8501 |
785.73 |
| 298.15 |
0.9000 |
785.66 |
| 298.15 |
0.9500 |
785.57 |
| 298.15 |
1.0000 |
785.47 |
| 308.15 |
0.0000 |
776.49 |
| 308.15 |
0.0500 |
776.66 |
| 308.15 |
0.1000 |
776.66 |
| 308.15 |
0.1500 |
776.61 |
| 308.15 |
0.2000 |
776.53 |
| 308.15 |
0.2500 |
776.41 |
| 308.15 |
0.3000 |
776.28 |
| 308.15 |
0.3500 |
776.12 |
| 308.15 |
0.4000 |
775.96 |
| 308.15 |
0.4500 |
775.79 |
| 308.15 |
0.4999 |
775.63 |
| 308.15 |
0.5500 |
775.47 |
| 308.15 |
0.6000 |
775.3 |
| 308.15 |
0.6500 |
775.13 |
| 308.15 |
0.7000 |
774.96 |
| 308.15 |
0.7500 |
774.77 |
| 308.15 |
0.8000 |
774.59 |
| 308.15 |
0.8501 |
774.4 |
| 308.15 |
0.9000 |
774.23 |
| 308.15 |
0.9500 |
774.08 |
| 308.15 |
1.0000 |
773.91 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Acetone (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.0000 |
793.74 |
| 288.15 |
0.0500 |
794.4 |
| 288.15 |
0.1000 |
794.86 |
| 288.15 |
0.1500 |
795.23 |
| 288.15 |
0.2000 |
795.5 |
| 288.15 |
0.2500 |
795.75 |
| 288.15 |
0.3000 |
795.99 |
| 288.15 |
0.3500 |
796.18 |
| 288.15 |
0.4000 |
796.34 |
| 288.15 |
0.4500 |
796.46 |
| 288.15 |
0.4999 |
796.57 |
| 288.15 |
0.5500 |
796.68 |
| 288.15 |
0.6000 |
796.77 |
| 288.15 |
0.6500 |
796.84 |
| 288.15 |
0.7000 |
796.86 |
| 288.15 |
0.7500 |
796.88 |
| 288.15 |
0.8000 |
796.91 |
| 288.15 |
0.8501 |
796.9 |
| 288.15 |
0.9000 |
796.92 |
| 288.15 |
0.9500 |
796.91 |
| 288.15 |
1.0000 |
796.87 |
| 298.15 |
0.0000 |
785.17 |
| 298.15 |
0.0500 |
785.59 |
| 298.15 |
0.1000 |
785.84 |
| 298.15 |
0.1500 |
786.0 |
| 298.15 |
0.2000 |
786.08 |
| 298.15 |
0.2500 |
786.16 |
| 298.15 |
0.3000 |
786.23 |
| 298.15 |
0.3500 |
786.24 |
| 298.15 |
0.4000 |
786.23 |
| 298.15 |
0.4500 |
786.21 |
| 298.15 |
0.4999 |
786.19 |
| 298.15 |
0.5500 |
786.17 |
| 298.15 |
0.6000 |
786.13 |
| 298.15 |
0.6500 |
786.07 |
| 298.15 |
0.7000 |
786.0 |
| 298.15 |
0.7500 |
785.9 |
| 298.15 |
0.8000 |
785.84 |
| 298.15 |
0.8501 |
785.73 |
| 298.15 |
0.9000 |
785.66 |
| 298.15 |
0.9500 |
785.57 |
| 298.15 |
1.0000 |
785.47 |
| 308.15 |
0.0000 |
776.49 |
| 308.15 |
0.0500 |
776.66 |
| 308.15 |
0.1000 |
776.66 |
| 308.15 |
0.1500 |
776.61 |
| 308.15 |
0.2000 |
776.53 |
| 308.15 |
0.2500 |
776.41 |
| 308.15 |
0.3000 |
776.28 |
| 308.15 |
0.3500 |
776.12 |
| 308.15 |
0.4000 |
775.96 |
| 308.15 |
0.4500 |
775.79 |
| 308.15 |
0.4999 |
775.63 |
| 308.15 |
0.5500 |
775.47 |
| 308.15 |
0.6000 |
775.3 |
| 308.15 |
0.6500 |
775.13 |
| 308.15 |
0.7000 |
774.96 |
| 308.15 |
0.7500 |
774.77 |
| 308.15 |
0.8000 |
774.59 |
| 308.15 |
0.8501 |
774.4 |
| 308.15 |
0.9000 |
774.23 |
| 308.15 |
0.9500 |
774.08 |
| 308.15 |
1.0000 |
773.91 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
351.44 |
| 0.0440 |
348.91 |
| 0.0850 |
346.65 |
| 0.1320 |
344.53 |
| 0.1750 |
342.69 |
| 0.2270 |
341.17 |
| 0.2760 |
339.81 |
| 0.3280 |
338.39 |
| 0.3800 |
337.32 |
| 0.4330 |
336.24 |
| 0.4810 |
335.37 |
| 0.5380 |
334.51 |
| 0.5860 |
333.78 |
| 0.6390 |
333.06 |
| 0.6880 |
332.43 |
| 0.7450 |
331.81 |
| 0.7960 |
331.20 |
| 0.8490 |
330.66 |
| 0.9010 |
330.17 |
| 0.9510 |
329.69 |
| 1.0000 |
329.26 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
351.55 |
| 0.0714 |
348.20 |
| 0.1480 |
345.35 |
| 0.2107 |
343.25 |
| 0.3242 |
339.90 |
| 0.3928 |
338.35 |
| 0.5016 |
336.05 |
| 0.6343 |
333.80 |
| 0.7779 |
331.80 |
| 0.8977 |
330.30 |
| 1.0000 |
329.35 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 1.0000 |
329.37 |
| 0.8910 |
330.15 |
| 0.7430 |
331.71 |
| 0.6590 |
332.80 |
| 0.5640 |
334.09 |
| 0.4950 |
335.31 |
| 0.4020 |
336.88 |
| 0.3260 |
338.49 |
| 0.2400 |
340.68 |
| 0.1660 |
343.14 |
| 0.1100 |
345.41 |
| 0.0760 |
346.97 |
| 0.0000 |
351.45 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.32 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
351.44 |
| 0.0440 |
348.91 |
| 0.0850 |
346.65 |
| 0.1320 |
344.53 |
| 0.1750 |
342.69 |
| 0.2270 |
341.17 |
| 0.2760 |
339.81 |
| 0.3280 |
338.39 |
| 0.3800 |
337.32 |
| 0.4330 |
336.24 |
| 0.4810 |
335.37 |
| 0.5380 |
334.51 |
| 0.5860 |
333.78 |
| 0.6390 |
333.06 |
| 0.6880 |
332.43 |
| 0.7450 |
331.81 |
| 0.7960 |
331.20 |
| 0.8490 |
330.66 |
| 0.9010 |
330.17 |
| 0.9510 |
329.69 |
| 1.0000 |
329.26 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
351.55 |
| 0.0714 |
348.20 |
| 0.1480 |
345.35 |
| 0.2107 |
343.25 |
| 0.3242 |
339.90 |
| 0.3928 |
338.35 |
| 0.5016 |
336.05 |
| 0.6343 |
333.80 |
| 0.7779 |
331.80 |
| 0.8977 |
330.30 |
| 1.0000 |
329.35 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Acetone (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 1.0000 |
329.37 |
| 0.8910 |
330.15 |
| 0.7430 |
331.71 |
| 0.6590 |
332.80 |
| 0.5640 |
334.09 |
| 0.4950 |
335.31 |
| 0.4020 |
336.88 |
| 0.3260 |
338.49 |
| 0.2400 |
340.68 |
| 0.1660 |
343.14 |
| 0.1100 |
345.41 |
| 0.0760 |
346.97 |
| 0.0000 |
351.45 |
Vapor Liquid Equilibrium at Constant Pressure
[ref]
Operational condition: Pressure, kPa =
101.33 (VLE)
| Fixed |
Measured |
| T [K] - VLE |
x1[mol/mol] of Acetone (2) - Liquid |
y1[mol/mol] of Acetone (2) - Vapour |
| 351.45 |
0.0000 |
0.0000 |
| 349.55 |
0.0330 |
0.1110 |
| 347.15 |
0.0780 |
0.2160 |
| 343.95 |
0.1490 |
0.3450 |
| 342.25 |
0.1950 |
0.4100 |
| 338.75 |
0.3160 |
0.5340 |
| 336.55 |
0.4140 |
0.6140 |
| 334.45 |
0.5320 |
0.6970 |
| 332.15 |
0.6910 |
0.7960 |
| 330.45 |
0.8520 |
0.8960 |
| 329.25 |
1.0000 |
1.0000 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
305.15 (VLE)
| P [kPa] - VLE |
x1[mol/mol] of Acetone (2) - Liquid |
| 11.679 |
0.0000 |
| 14.999 |
0.0422 |
| 16.585 |
0.0673 |
| 19.358 |
0.1130 |
| 22.571 |
0.1787 |
| 24.811 |
0.2361 |
| 25.585 |
0.2665 |
| 27.384 |
0.3128 |
| 28.371 |
0.3470 |
| 31.037 |
0.4458 |
| 33.037 |
0.5372 |
| 35.37 |
0.6548 |
| 37.584 |
0.7721 |
| 38.89 |
0.8474 |
| 40.13 |
0.9252 |
| 41.317 |
1.0000 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
313.15 (VLE)
| P [kPa] - VLE |
x1[mol/mol] of Acetone (2) - Liquid |
| 17.892 |
0.0000 |
| 21.612 |
0.0389 |
| 22.012 |
0.0446 |
| 24.531 |
0.0765 |
| 29.211 |
0.1409 |
| 32.011 |
0.1883 |
| 36.037 |
0.2683 |
| 39.037 |
0.3406 |
| 42.463 |
0.4355 |
| 45.41 |
0.5315 |
| 48.796 |
0.6528 |
| 51.729 |
0.7727 |
| 53.716 |
0.8593 |
| 54.689 |
0.9038 |
| 56.649 |
1.0000 |
Sources
-
Dortmund Data Bank Vapor-Liquid Equilibrium Data
-
Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
-
Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
-
Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
-
Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
-
Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa