Mixture of Methyl Isobutyl Ketone + 1-Propanol
Datasets
-
Mole fraction (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of 1-Propanol (2)
[ref]
Fixed |
Measured |
Mole fraction of 1-Propanol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of 1-Propanol (2) - Gas |
0.0000 |
338.15 |
0.0000 |
0.1140 |
338.15 |
0.2290 |
0.2020 |
338.15 |
0.3590 |
0.3040 |
338.15 |
0.4440 |
0.3750 |
338.15 |
0.4990 |
0.4450 |
338.15 |
0.5560 |
0.4990 |
338.15 |
0.5870 |
0.6350 |
338.15 |
0.6770 |
0.7070 |
338.15 |
0.7270 |
0.7920 |
338.15 |
0.7880 |
0.8390 |
338.15 |
0.8270 |
0.8880 |
338.15 |
0.8720 |
0.9530 |
338.15 |
0.9420 |
1.0000 |
338.15 |
1.0000 |
0.0000 |
353.15 |
0.0000 |
0.1100 |
353.15 |
0.2300 |
0.2090 |
353.15 |
0.3620 |
0.3000 |
353.15 |
0.4550 |
0.3770 |
353.15 |
0.5230 |
0.4420 |
353.15 |
0.5680 |
0.4950 |
353.15 |
0.6070 |
0.6450 |
353.15 |
0.6960 |
0.7290 |
353.15 |
0.7470 |
0.7960 |
353.15 |
0.8080 |
0.8430 |
353.15 |
0.8450 |
0.8860 |
353.15 |
0.8850 |
0.9360 |
353.15 |
0.9310 |
1.0000 |
353.15 |
1.0000 |
0.0000 |
368.15 |
0.0000 |
0.1110 |
368.15 |
0.2200 |
0.2060 |
368.15 |
0.3650 |
0.3000 |
368.15 |
0.4640 |
0.3750 |
368.15 |
0.5270 |
0.4420 |
368.15 |
0.5770 |
0.4970 |
368.15 |
0.6170 |
0.7390 |
368.15 |
0.7690 |
0.8110 |
368.15 |
0.8210 |
0.8500 |
368.15 |
0.8580 |
0.8920 |
368.15 |
0.8970 |
0.9370 |
368.15 |
0.9390 |
1.0000 |
368.15 |
1.0000 |
Mole fraction of 1-Propanol (2)
[ref]
Fixed |
Measured |
Mole fraction of 1-Propanol (2) - Liquid |
Temperature, K - Liquid |
Mole fraction of 1-Propanol (2) - Gas |
0.0000 |
338.15 |
0.0000 |
0.1140 |
338.15 |
0.2290 |
0.2020 |
338.15 |
0.3590 |
0.3040 |
338.15 |
0.4440 |
0.3750 |
338.15 |
0.4990 |
0.4450 |
338.15 |
0.5560 |
0.4990 |
338.15 |
0.5870 |
0.6350 |
338.15 |
0.6770 |
0.7070 |
338.15 |
0.7270 |
0.7920 |
338.15 |
0.7880 |
0.8390 |
338.15 |
0.8270 |
0.8880 |
338.15 |
0.8720 |
0.9530 |
338.15 |
0.9420 |
1.0000 |
338.15 |
1.0000 |
0.0000 |
353.15 |
0.0000 |
0.1100 |
353.15 |
0.2300 |
0.2090 |
353.15 |
0.3620 |
0.3000 |
353.15 |
0.4550 |
0.3770 |
353.15 |
0.5230 |
0.4420 |
353.15 |
0.5680 |
0.4950 |
353.15 |
0.6070 |
0.6450 |
353.15 |
0.6960 |
0.7290 |
353.15 |
0.7470 |
0.7960 |
353.15 |
0.8080 |
0.8430 |
353.15 |
0.8450 |
0.8860 |
353.15 |
0.8850 |
0.9360 |
353.15 |
0.9310 |
1.0000 |
353.15 |
1.0000 |
0.0000 |
368.15 |
0.0000 |
0.1110 |
368.15 |
0.2200 |
0.2060 |
368.15 |
0.3650 |
0.3000 |
368.15 |
0.4640 |
0.3750 |
368.15 |
0.5270 |
0.4420 |
368.15 |
0.5770 |
0.4970 |
368.15 |
0.6170 |
0.7390 |
368.15 |
0.7690 |
0.8110 |
368.15 |
0.8210 |
0.8500 |
368.15 |
0.8580 |
0.8920 |
368.15 |
0.8970 |
0.9370 |
368.15 |
0.9390 |
1.0000 |
368.15 |
1.0000 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0797 |
0.3906 |
0.1587 |
0.6867 |
0.2384 |
0.9203 |
0.3192 |
1.0949 |
0.3901 |
1.2133 |
0.4948 |
1.297 |
0.5955 |
1.2865 |
0.6981 |
1.1769 |
0.8004 |
0.9423 |
0.9012 |
0.5634 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0797 |
0.3906 |
0.1587 |
0.6867 |
0.2384 |
0.9203 |
0.3192 |
1.0949 |
0.3901 |
1.2133 |
0.4948 |
1.297 |
0.5955 |
1.2865 |
0.6981 |
1.1769 |
0.8004 |
0.9423 |
0.9012 |
0.5634 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of 1-Propanol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
338.15 |
17.57 |
0.1140 |
338.15 |
21.32 |
0.2020 |
338.15 |
23.11 |
0.3040 |
338.15 |
24.53 |
0.3750 |
338.15 |
25.16 |
0.4450 |
338.15 |
25.81 |
0.4990 |
338.15 |
26.09 |
0.6350 |
338.15 |
26.61 |
0.7070 |
338.15 |
26.95 |
0.7920 |
338.15 |
26.98 |
0.8390 |
338.15 |
26.94 |
0.8880 |
338.15 |
26.84 |
0.9530 |
338.15 |
26.46 |
1.0000 |
338.15 |
25.92 |
0.0000 |
353.15 |
31.41 |
0.1100 |
353.15 |
37.91 |
0.2090 |
353.15 |
41.61 |
0.3000 |
353.15 |
44.45 |
0.3770 |
353.15 |
46.03 |
0.4420 |
353.15 |
47.29 |
0.4950 |
353.15 |
48.18 |
0.6450 |
353.15 |
49.76 |
0.7290 |
353.15 |
50.66 |
0.7960 |
353.15 |
51.26 |
0.8430 |
353.15 |
51.66 |
0.8860 |
353.15 |
51.64 |
0.9360 |
353.15 |
51.54 |
1.0000 |
353.15 |
51.00 |
0.0000 |
368.15 |
54.04 |
0.1110 |
368.15 |
63.68 |
0.2060 |
368.15 |
70.25 |
0.3000 |
368.15 |
76.25 |
0.3750 |
368.15 |
79.52 |
0.4420 |
368.15 |
82.17 |
0.4970 |
368.15 |
84.15 |
0.7390 |
368.15 |
89.97 |
0.8110 |
368.15 |
91.80 |
0.8500 |
368.15 |
92.57 |
0.8920 |
368.15 |
93.43 |
0.9370 |
368.15 |
93.90 |
1.0000 |
368.15 |
93.92 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of 1-Propanol (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
338.15 |
17.57 |
0.1140 |
338.15 |
21.32 |
0.2020 |
338.15 |
23.11 |
0.3040 |
338.15 |
24.53 |
0.3750 |
338.15 |
25.16 |
0.4450 |
338.15 |
25.81 |
0.4990 |
338.15 |
26.09 |
0.6350 |
338.15 |
26.61 |
0.7070 |
338.15 |
26.95 |
0.7920 |
338.15 |
26.98 |
0.8390 |
338.15 |
26.94 |
0.8880 |
338.15 |
26.84 |
0.9530 |
338.15 |
26.46 |
1.0000 |
338.15 |
25.92 |
0.0000 |
353.15 |
31.41 |
0.1100 |
353.15 |
37.91 |
0.2090 |
353.15 |
41.61 |
0.3000 |
353.15 |
44.45 |
0.3770 |
353.15 |
46.03 |
0.4420 |
353.15 |
47.29 |
0.4950 |
353.15 |
48.18 |
0.6450 |
353.15 |
49.76 |
0.7290 |
353.15 |
50.66 |
0.7960 |
353.15 |
51.26 |
0.8430 |
353.15 |
51.66 |
0.8860 |
353.15 |
51.64 |
0.9360 |
353.15 |
51.54 |
1.0000 |
353.15 |
51.00 |
0.0000 |
368.15 |
54.04 |
0.1110 |
368.15 |
63.68 |
0.2060 |
368.15 |
70.25 |
0.3000 |
368.15 |
76.25 |
0.3750 |
368.15 |
79.52 |
0.4420 |
368.15 |
82.17 |
0.4970 |
368.15 |
84.15 |
0.7390 |
368.15 |
89.97 |
0.8110 |
368.15 |
91.80 |
0.8500 |
368.15 |
92.57 |
0.8920 |
368.15 |
93.43 |
0.9370 |
368.15 |
93.90 |
1.0000 |
368.15 |
93.92 |
Sources