Datasets
-
Activity coefficient (4)
-
Mole fraction (44)
-
Interfacial tension, N/m (2)
-
ρl - Mass density, kg/m3 (4)
Activity coefficient of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Propane, 2-methoxy-2-methyl- (1) - Liquid |
| 288.15 |
127.0 |
| 298.15 |
139.0 |
| 308.15 |
180.0 |
| 318.15 |
234.0 |
Activity coefficient of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Propane, 2-methoxy-2-methyl- (1) - Liquid |
| 303.25 |
153.0 |
| 313.25 |
195.0 |
| 323.25 |
235.0 |
| 333.25 |
278.0 |
Activity coefficient of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Propane, 2-methoxy-2-methyl- (1) - Liquid |
| 288.15 |
127.0 |
| 298.15 |
139.0 |
| 308.15 |
180.0 |
| 318.15 |
234.0 |
Activity coefficient of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of Propane, 2-methoxy-2-methyl- (1) - Liquid |
| 303.25 |
153.0 |
| 313.25 |
195.0 |
| 323.25 |
235.0 |
| 333.25 |
278.0 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 275.50 |
0.0125 |
| 283.15 |
0.0119 |
| 298.15 |
0.0089 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 275.50 |
0.0570 |
| 283.15 |
0.0656 |
| 298.15 |
0.0686 |
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 |
0.0636 |
| 293.20 |
0.9879 |
| 313.20 |
0.0654 |
| 313.20 |
0.9863 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
101.30 |
0.0574 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
101.30 |
0.9933 |
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 2 |
| 298.20 |
0.9595 |
| 308.20 |
0.9633 |
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 |
| 298.20 |
0.0141 |
| 308.20 |
0.0178 |
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 |
| 308.20 |
101.30 |
0.0144 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 308.20 |
101.30 |
0.0367 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 298.30 |
0.9860 |
| 298.30 |
0.9870 |
| 298.30 |
0.9860 |
| 307.90 |
0.9860 |
| 307.90 |
0.9860 |
| 307.80 |
0.9840 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 298.30 |
0.0410 |
| 298.30 |
0.0410 |
| 298.30 |
0.0420 |
| 307.90 |
0.0320 |
| 307.90 |
0.0310 |
| 307.80 |
0.0320 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 293.15 |
0.9434 |
| 313.15 |
0.9534 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 293.15 |
0.0110 |
| 313.15 |
0.0069 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 313.15 |
101.00 |
0.9538 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 313.15 |
101.00 |
0.0160 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 293.00 |
101.30 |
0.9704 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 293.00 |
101.30 |
0.0133 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 288.15 |
0.9217 |
| 288.15 |
0.9098 |
| 298.15 |
0.9259 |
| 298.15 |
0.9329 |
| 308.15 |
0.9180 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 288.15 |
0.0120 |
| 288.15 |
0.0156 |
| 298.15 |
0.0078 |
| 298.15 |
0.0087 |
| 308.15 |
0.0072 |
Henry's Law constant (molality scale), kPa*kg/mol of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Propane, 2-methoxy-2-methyl- (1) - Liquid |
| 274.15 |
5.5001 |
| 294.65 |
52.116 |
| 294.65 |
41.029 |
| 296.15 |
58.013 |
| 310.15 |
59.031 |
| 320.15 |
367.63 |
| 331.15 |
1653.4 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 298.15 |
0.9875 |
| 313.15 |
0.9853 |
| 323.15 |
0.9842 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 298.15 |
0.0329 |
| 313.15 |
0.0250 |
| 323.15 |
0.0190 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 275.50 |
0.0125 |
| 283.15 |
0.0119 |
| 298.15 |
0.0089 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 275.50 |
0.0570 |
| 283.15 |
0.0656 |
| 298.15 |
0.0686 |
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 |
0.0636 |
| 293.20 |
0.9879 |
| 313.20 |
0.0654 |
| 313.20 |
0.9863 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
101.30 |
0.0574 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
101.30 |
0.9933 |
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 2 |
| 298.20 |
0.9595 |
| 308.20 |
0.9633 |
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 |
| 298.20 |
0.0141 |
| 308.20 |
0.0178 |
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 |
| 308.20 |
101.30 |
0.0144 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 308.20 |
101.30 |
0.0367 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 298.30 |
0.9860 |
| 298.30 |
0.9870 |
| 298.30 |
0.9860 |
| 307.90 |
0.9860 |
| 307.90 |
0.9860 |
| 307.80 |
0.9840 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 298.30 |
0.0410 |
| 298.30 |
0.0410 |
| 298.30 |
0.0420 |
| 307.90 |
0.0320 |
| 307.90 |
0.0310 |
| 307.80 |
0.0320 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 293.15 |
0.9434 |
| 313.15 |
0.9534 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 293.15 |
0.0110 |
| 313.15 |
0.0069 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 313.15 |
101.00 |
0.9538 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 313.15 |
101.00 |
0.0160 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 293.00 |
101.30 |
0.9704 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 293.00 |
101.30 |
0.0133 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 288.15 |
0.9217 |
| 288.15 |
0.9098 |
| 298.15 |
0.9259 |
| 298.15 |
0.9329 |
| 308.15 |
0.9180 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 288.15 |
0.0120 |
| 288.15 |
0.0156 |
| 298.15 |
0.0078 |
| 298.15 |
0.0087 |
| 308.15 |
0.0072 |
Henry's Law constant (molality scale), kPa*kg/mol of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of Propane, 2-methoxy-2-methyl- (1) - Liquid |
| 274.15 |
5.5001 |
| 294.65 |
52.116 |
| 294.65 |
41.029 |
| 296.15 |
58.013 |
| 310.15 |
59.031 |
| 320.15 |
367.63 |
| 331.15 |
1653.4 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
| 298.15 |
0.9875 |
| 313.15 |
0.9853 |
| 323.15 |
0.9842 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
| 298.15 |
0.0329 |
| 313.15 |
0.0250 |
| 323.15 |
0.0190 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 278.15 |
0.0078 |
| 288.15 |
0.0088 |
| 298.15 |
0.0098 |
| 308.15 |
0.0108 |
| 318.15 |
0.0117 |
Interfacial tension, N/m
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
| 278.15 |
0.0078 |
| 288.15 |
0.0088 |
| 298.15 |
0.0098 |
| 308.15 |
0.0108 |
| 318.15 |
0.0117 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
| 278.15 |
990.93 |
| 288.15 |
990.41 |
| 298.15 |
990.58 |
| 308.15 |
989.23 |
| 318.15 |
986.96 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
| 278.15 |
760.48 |
| 288.15 |
750.41 |
| 298.15 |
740.17 |
| 308.15 |
729.82 |
| 318.15 |
719.35 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass density, kg/m3 - Liquid mixture 1 |
| 278.15 |
990.93 |
| 288.15 |
990.41 |
| 298.15 |
990.58 |
| 308.15 |
989.23 |
| 318.15 |
986.96 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mass density, kg/m3 - Liquid mixture 2 |
| 278.15 |
760.48 |
| 288.15 |
750.41 |
| 298.15 |
740.17 |
| 308.15 |
729.82 |
| 318.15 |
719.35 |
Sources
-
Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane
-
Infinite dilution activity coefficient measurements by inert gas stripping method
-
Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
-
Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
-
Quaternary (liquid + liquid) equilibria for (water + 2-propanol + 1,1-dimethylethyl methyl ether + diisopropyl ether) at the temperature 298.15 K
-
Liquid-liquid equilibrium for ternary systems of water + 2,2,3,3-tetrafluoro-1-propanol + isopropyl ether/tert-butyl methyl ether at 298.2, 308.2 K
-
Liquid-liquid equilibrium study for ternary systems of water + propargyl alcohol + solvents at 308.2 K: Measurement and thermodynamic modelling
-
Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
-
Liquid-Liquid Equilibria of Ionic Liquids-Water-Acetic Acid Mixtures
-
Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
-
Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
-
Liquid-Liquid Equilibrium of MTBE + Ethanol + Water and MTBE + 1-Hexanol + Water over the Temperature Range of 288.15 to 308.15 K
-
Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
-
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
-
Liquid Liquid Equilibria for the Ternary System 2-Methoxy-2-methylpropane + Phenol + Water
