Datasets
-
Activity coefficient (2)
-
Mass fraction (54)
-
Excess molar enthalpy (molar enthalpy (2)
-
ρl - Mass density, kg/m3 (2)
Activity coefficient of Methyl Isobutyl Ketone (1)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Methyl Isobutyl Ketone (1) - Liquid |
| 278.15 |
239.0 |
| 288.15 |
277.0 |
| 288.15 |
287.0 |
| 298.15 |
327.0 |
| 308.15 |
370.0 |
| 318.15 |
405.0 |
| 328.15 |
410.0 |
Activity coefficient of Methyl Isobutyl Ketone (1)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Methyl Isobutyl Ketone (1) - Liquid |
| 278.15 |
239.0 |
| 288.15 |
277.0 |
| 288.15 |
287.0 |
| 298.15 |
327.0 |
| 308.15 |
370.0 |
| 318.15 |
405.0 |
| 328.15 |
410.0 |
Mass fraction of Water (2)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid mixture 1)
- Pressure, kPa = 101 (Liquid mixture 1)
| Mass fraction of Water (2) - Liquid mixture 1 |
| 0.0190 |
| 0.9810 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
100.00 |
0.9877 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
100.00 |
0.0194 |
Mole fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 333.15 |
0.0023 |
| 343.15 |
0.0022 |
| 353.15 |
0.0019 |
Mole fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 333.15 |
0.8109 |
| 343.15 |
0.7410 |
| 353.15 |
0.6924 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 293.20 |
0.0915 |
| 293.20 |
0.9953 |
| 313.20 |
0.1380 |
| 313.20 |
0.9966 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 401.00 |
0.0190 |
| 303.10 |
0.0160 |
| 302.80 |
0.0160 |
| 322.40 |
0.0140 |
| 401.00 |
0.0180 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 401.00 |
0.9410 |
| 303.10 |
0.9810 |
| 302.80 |
0.9810 |
| 322.40 |
0.9750 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid mixture 1)
- Pressure, kPa = 101.3 (Liquid mixture 1)
| Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 0.0155 |
| 0.9785 |
Mole fraction of Methyl Isobutyl Ketone (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 101.00 |
293.15 |
0.9009 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.20 |
101.30 |
0.0209 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.20 |
101.30 |
0.9815 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 303.15 |
0.0192 |
| 328.15 |
0.0251 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 303.15 |
0.9826 |
| 328.15 |
0.9857 |
| 328.15 |
0.9856 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0237 |
| 318.15 |
0.0275 |
| 338.15 |
0.0334 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0162 |
| 318.15 |
0.0152 |
| 338.15 |
0.0137 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.15 |
0.0178 |
| 313.15 |
0.0145 |
| 323.15 |
0.0136 |
| 333.15 |
0.0127 |
| 343.15 |
0.0121 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0245 |
| 313.15 |
0.0256 |
| 323.15 |
0.0278 |
| 333.15 |
0.0295 |
| 343.15 |
0.0321 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0171 |
| 313.15 |
0.0148 |
| 323.15 |
0.0136 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0194 |
| 313.15 |
0.0244 |
| 323.15 |
0.0278 |
Henry's Law constant (molality scale), kPa*kg/mol of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Methyl Isobutyl Ketone (1) - Liquid |
| 274.15 |
0.8336 |
| 294.65 |
8.0847 |
| 294.65 |
8.2695 |
| 296.15 |
9.335 |
| 310.15 |
37.243 |
| 320.15 |
72.455 |
| 331.15 |
163.71 |
| 333.15 |
236.27 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0181 |
| 318.15 |
0.0146 |
| 308.15 |
0.0159 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.15 |
0.9802 |
| 318.15 |
0.9766 |
| 308.15 |
0.9780 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.15 |
0.9802 |
| 308.15 |
0.9762 |
| 318.15 |
0.9722 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0190 |
| 308.15 |
0.0169 |
| 318.15 |
0.0152 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 292.25 |
0.0184 |
| 312.65 |
0.0142 |
| 323.25 |
0.0138 |
| 343.35 |
0.0123 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 292.25 |
0.0237 |
| 312.65 |
0.0246 |
| 323.25 |
0.0267 |
| 343.35 |
0.0312 |
Mass fraction of Water (2)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid mixture 1)
- Pressure, kPa = 101 (Liquid mixture 1)
| Mass fraction of Water (2) - Liquid mixture 1 |
| 0.0190 |
| 0.9810 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
100.00 |
0.9877 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
100.00 |
0.0194 |
Mole fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 333.15 |
0.0023 |
| 343.15 |
0.0022 |
| 353.15 |
0.0019 |
Mole fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 333.15 |
0.8109 |
| 343.15 |
0.7410 |
| 353.15 |
0.6924 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 293.20 |
0.0915 |
| 293.20 |
0.9953 |
| 313.20 |
0.1380 |
| 313.20 |
0.9966 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 401.00 |
0.0190 |
| 303.10 |
0.0160 |
| 302.80 |
0.0160 |
| 322.40 |
0.0140 |
| 401.00 |
0.0180 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 401.00 |
0.9410 |
| 303.10 |
0.9810 |
| 302.80 |
0.9810 |
| 322.40 |
0.9750 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid mixture 1)
- Pressure, kPa = 101.3 (Liquid mixture 1)
| Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 0.0155 |
| 0.9785 |
Mole fraction of Methyl Isobutyl Ketone (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 101.00 |
293.15 |
0.9009 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.20 |
101.30 |
0.0209 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.20 |
101.30 |
0.9815 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 303.15 |
0.0192 |
| 328.15 |
0.0251 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 303.15 |
0.9826 |
| 328.15 |
0.9857 |
| 328.15 |
0.9856 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0237 |
| 318.15 |
0.0275 |
| 338.15 |
0.0334 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0162 |
| 318.15 |
0.0152 |
| 338.15 |
0.0137 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.15 |
0.0178 |
| 313.15 |
0.0145 |
| 323.15 |
0.0136 |
| 333.15 |
0.0127 |
| 343.15 |
0.0121 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0245 |
| 313.15 |
0.0256 |
| 323.15 |
0.0278 |
| 333.15 |
0.0295 |
| 343.15 |
0.0321 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0171 |
| 313.15 |
0.0148 |
| 323.15 |
0.0136 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.0194 |
| 313.15 |
0.0244 |
| 323.15 |
0.0278 |
Henry's Law constant (molality scale), kPa*kg/mol of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Methyl Isobutyl Ketone (1) - Liquid |
| 274.15 |
0.8336 |
| 294.65 |
8.0847 |
| 294.65 |
8.2695 |
| 296.15 |
9.335 |
| 310.15 |
37.243 |
| 320.15 |
72.455 |
| 331.15 |
163.71 |
| 333.15 |
236.27 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0181 |
| 318.15 |
0.0146 |
| 308.15 |
0.0159 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.15 |
0.9802 |
| 318.15 |
0.9766 |
| 308.15 |
0.9780 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 298.15 |
0.9802 |
| 308.15 |
0.9762 |
| 318.15 |
0.9722 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 2 |
| 298.15 |
0.0190 |
| 308.15 |
0.0169 |
| 318.15 |
0.0152 |
Mass fraction of Methyl Isobutyl Ketone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Methyl Isobutyl Ketone (1) - Liquid mixture 1 |
| 292.25 |
0.0184 |
| 312.65 |
0.0142 |
| 323.25 |
0.0138 |
| 343.35 |
0.0123 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 292.25 |
0.0237 |
| 312.65 |
0.0246 |
| 323.25 |
0.0267 |
| 343.35 |
0.0312 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0020 |
288.15 |
-0.0247 |
| 0.0020 |
288.15 |
-0.0247 |
| 0.0017 |
288.15 |
-0.0213 |
| 0.0017 |
288.15 |
-0.0214 |
| 0.0014 |
288.15 |
-0.0178 |
| 0.0014 |
288.15 |
-0.0180 |
| 0.0011 |
288.15 |
-0.0144 |
| 0.0011 |
288.15 |
-0.0143 |
| 0.0006 |
288.15 |
-0.0073 |
| 0.0006 |
288.15 |
-0.0072 |
| 0.0020 |
298.15 |
-0.0192 |
| 0.0020 |
298.15 |
-0.0191 |
| 0.0017 |
298.15 |
-0.0165 |
| 0.0017 |
298.15 |
-0.0166 |
| 0.0014 |
298.15 |
-0.0138 |
| 0.0014 |
298.15 |
-0.0140 |
| 0.0011 |
298.15 |
-0.0113 |
| 0.0011 |
298.15 |
-0.0113 |
| 0.0009 |
298.15 |
-0.0084 |
| 0.0009 |
298.15 |
-0.0085 |
| 0.0006 |
298.15 |
-0.0056 |
| 0.0006 |
298.15 |
-0.0056 |
| 0.0020 |
308.15 |
-0.0138 |
| 0.0020 |
308.15 |
-0.0138 |
| 0.0017 |
308.15 |
-0.0119 |
| 0.0017 |
308.15 |
-0.0120 |
| 0.0014 |
308.15 |
-0.0100 |
| 0.0014 |
308.15 |
-0.0100 |
| 0.0011 |
308.15 |
-0.0081 |
| 0.0011 |
308.15 |
-0.0080 |
| 0.0009 |
308.15 |
-0.0062 |
| 0.0009 |
308.15 |
-0.0062 |
| 0.0006 |
308.15 |
-0.0040 |
| 0.0006 |
318.15 |
-0.0041 |
| 0.0020 |
318.15 |
-0.0084 |
| 0.0020 |
318.15 |
-0.0086 |
| 0.0017 |
318.15 |
-0.0074 |
| 0.0017 |
318.15 |
-0.0075 |
| 0.0014 |
318.15 |
-0.0062 |
| 0.0014 |
318.15 |
-0.0062 |
| 0.0011 |
318.15 |
-0.0051 |
| 0.0011 |
318.15 |
-0.0051 |
| 0.0009 |
318.15 |
-0.0039 |
| 0.0009 |
318.15 |
-0.0038 |
| 0.0006 |
318.15 |
-0.0027 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Temperature, K - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0020 |
288.15 |
-0.0247 |
| 0.0020 |
288.15 |
-0.0247 |
| 0.0017 |
288.15 |
-0.0213 |
| 0.0017 |
288.15 |
-0.0214 |
| 0.0014 |
288.15 |
-0.0178 |
| 0.0014 |
288.15 |
-0.0180 |
| 0.0011 |
288.15 |
-0.0144 |
| 0.0011 |
288.15 |
-0.0143 |
| 0.0006 |
288.15 |
-0.0073 |
| 0.0006 |
288.15 |
-0.0072 |
| 0.0020 |
298.15 |
-0.0192 |
| 0.0020 |
298.15 |
-0.0191 |
| 0.0017 |
298.15 |
-0.0165 |
| 0.0017 |
298.15 |
-0.0166 |
| 0.0014 |
298.15 |
-0.0138 |
| 0.0014 |
298.15 |
-0.0140 |
| 0.0011 |
298.15 |
-0.0113 |
| 0.0011 |
298.15 |
-0.0113 |
| 0.0009 |
298.15 |
-0.0084 |
| 0.0009 |
298.15 |
-0.0085 |
| 0.0006 |
298.15 |
-0.0056 |
| 0.0006 |
298.15 |
-0.0056 |
| 0.0020 |
308.15 |
-0.0138 |
| 0.0020 |
308.15 |
-0.0138 |
| 0.0017 |
308.15 |
-0.0119 |
| 0.0017 |
308.15 |
-0.0120 |
| 0.0014 |
308.15 |
-0.0100 |
| 0.0014 |
308.15 |
-0.0100 |
| 0.0011 |
308.15 |
-0.0081 |
| 0.0011 |
308.15 |
-0.0080 |
| 0.0009 |
308.15 |
-0.0062 |
| 0.0009 |
308.15 |
-0.0062 |
| 0.0006 |
308.15 |
-0.0040 |
| 0.0006 |
318.15 |
-0.0041 |
| 0.0020 |
318.15 |
-0.0084 |
| 0.0020 |
318.15 |
-0.0086 |
| 0.0017 |
318.15 |
-0.0074 |
| 0.0017 |
318.15 |
-0.0075 |
| 0.0014 |
318.15 |
-0.0062 |
| 0.0014 |
318.15 |
-0.0062 |
| 0.0011 |
318.15 |
-0.0051 |
| 0.0011 |
318.15 |
-0.0051 |
| 0.0009 |
318.15 |
-0.0039 |
| 0.0009 |
318.15 |
-0.0038 |
| 0.0006 |
318.15 |
-0.0027 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0020 |
288.15 |
997.567 |
| 0.0020 |
288.15 |
997.592 |
| 0.0017 |
288.15 |
997.788 |
| 0.0017 |
288.15 |
997.779 |
| 0.0014 |
288.15 |
998.001 |
| 0.0014 |
288.15 |
997.995 |
| 0.0011 |
288.15 |
998.21 |
| 0.0011 |
288.15 |
998.224 |
| 0.0009 |
288.15 |
998.405 |
| 0.0009 |
288.15 |
998.422 |
| 0.0006 |
288.15 |
998.655 |
| 0.0006 |
288.15 |
998.669 |
| 0.0020 |
298.15 |
995.417 |
| 0.0020 |
298.15 |
995.402 |
| 0.0017 |
298.15 |
995.624 |
| 0.0017 |
298.15 |
995.64 |
| 0.0014 |
298.15 |
995.875 |
| 0.0014 |
298.15 |
995.871 |
| 0.0011 |
298.15 |
996.114 |
| 0.0011 |
298.15 |
996.078 |
| 0.0009 |
298.15 |
996.345 |
| 0.0009 |
298.15 |
996.319 |
| 0.0006 |
298.15 |
996.572 |
| 0.0006 |
298.15 |
996.58 |
| 0.0020 |
308.15 |
992.3 |
| 0.0020 |
308.15 |
992.285 |
| 0.0017 |
308.15 |
992.542 |
| 0.0017 |
308.15 |
992.525 |
| 0.0014 |
308.15 |
992.791 |
| 0.0014 |
308.15 |
992.795 |
| 0.0011 |
308.15 |
993.03 |
| 0.0011 |
308.15 |
993.053 |
| 0.0009 |
308.15 |
993.283 |
| 0.0009 |
308.15 |
993.282 |
| 0.0006 |
308.15 |
993.534 |
| 0.0006 |
308.15 |
993.533 |
| 0.0020 |
318.15 |
988.379 |
| 0.0020 |
318.15 |
988.402 |
| 0.0017 |
318.15 |
988.636 |
| 0.0017 |
318.15 |
988.633 |
| 0.0014 |
318.15 |
988.91 |
| 0.0014 |
318.15 |
988.905 |
| 0.0011 |
318.15 |
989.147 |
| 0.0011 |
318.15 |
989.156 |
| 0.0009 |
318.15 |
989.411 |
| 0.0009 |
318.15 |
989.421 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
| Fixed |
Measured |
| Mole fraction of Methyl Isobutyl Ketone (1) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0020 |
288.15 |
997.567 |
| 0.0020 |
288.15 |
997.592 |
| 0.0017 |
288.15 |
997.788 |
| 0.0017 |
288.15 |
997.779 |
| 0.0014 |
288.15 |
998.001 |
| 0.0014 |
288.15 |
997.995 |
| 0.0011 |
288.15 |
998.21 |
| 0.0011 |
288.15 |
998.224 |
| 0.0009 |
288.15 |
998.405 |
| 0.0009 |
288.15 |
998.422 |
| 0.0006 |
288.15 |
998.655 |
| 0.0006 |
288.15 |
998.669 |
| 0.0020 |
298.15 |
995.417 |
| 0.0020 |
298.15 |
995.402 |
| 0.0017 |
298.15 |
995.624 |
| 0.0017 |
298.15 |
995.64 |
| 0.0014 |
298.15 |
995.875 |
| 0.0014 |
298.15 |
995.871 |
| 0.0011 |
298.15 |
996.114 |
| 0.0011 |
298.15 |
996.078 |
| 0.0009 |
298.15 |
996.345 |
| 0.0009 |
298.15 |
996.319 |
| 0.0006 |
298.15 |
996.572 |
| 0.0006 |
298.15 |
996.58 |
| 0.0020 |
308.15 |
992.3 |
| 0.0020 |
308.15 |
992.285 |
| 0.0017 |
308.15 |
992.542 |
| 0.0017 |
308.15 |
992.525 |
| 0.0014 |
308.15 |
992.791 |
| 0.0014 |
308.15 |
992.795 |
| 0.0011 |
308.15 |
993.03 |
| 0.0011 |
308.15 |
993.053 |
| 0.0009 |
308.15 |
993.283 |
| 0.0009 |
308.15 |
993.282 |
| 0.0006 |
308.15 |
993.534 |
| 0.0006 |
308.15 |
993.533 |
| 0.0020 |
318.15 |
988.379 |
| 0.0020 |
318.15 |
988.402 |
| 0.0017 |
318.15 |
988.636 |
| 0.0017 |
318.15 |
988.633 |
| 0.0014 |
318.15 |
988.91 |
| 0.0014 |
318.15 |
988.905 |
| 0.0011 |
318.15 |
989.147 |
| 0.0011 |
318.15 |
989.156 |
| 0.0009 |
318.15 |
989.411 |
| 0.0009 |
318.15 |
989.421 |
Sources
-
Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
-
Salt influence on MIBK/water liquid-liquid equilibrium: Measuring and modeling with ePC-SAFT and COSMO-RS
-
Liquid-liquid equilibrium for ternary systems, methyl isobutyl ketone +(catechol, resorcinol and hydroquinone) + water at 333.15 K, 343.15 K and 353.15 K
-
Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
-
Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
-
Influence of Salt on the Solubility and Tie-Line Data for Water + Formic Acid + Methyl Isobutyl Ketone at T = 298.15 K
-
Liquid-Liquid Equilibria of Ionic Liquids-Water-Acetic Acid Mixtures
-
Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
-
Measurement and Thermodynamic Modeling of Ternary (Liquid + Liquid) Equilibrium for Extraction of N,N-Dimethylacetamide from Aqueous Solution with Different Solvents
-
Liquid-Liquid Equilibrium of Water + 2-Methoxyphenol + Methyl Isobutyl Ketone and Water + 1,2-Benzenediol + Methyl Isobutyl Ketone at 303.15 K and 328.15 K
-
Liquid-Liquid Equilibrium for the Ternary Systems (Methyl Isobutyl Ketone + Quinoline or Isoquinoline + Water) at 298.15, 318.15, and 338.15 K
-
Experiments and COSMO-SAC Modeling of Methyl Isobutyl Ketone + Dimethylphenols + Water Mixtures
-
Air-Water Partitioning of C5 and C6 Alkanones: Measurement, Critical Compilation, Correlation, and Recommended Data
-
Liquid-Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + Water + Hydroquinone
-
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
-
Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + m-Benzenediol + Water
-
Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + 1,2-Benzenediol + Water
-
Liquid Liquid Equilibria for the Ternary System Water + Methyl Isobutyl Ketone + tert-Butyl Alcohol at Several Temperatures