Datasets
-
Activity coefficient (8)
-
Mole fraction (28)
-
Interfacial tension, N/m (2)
-
n0 - Refractive index (Na D-line) (2)
-
ρl - Mass density, kg/m3 (4)
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 273.35 |
121.0 |
| 283.15 |
156.0 |
| 293.15 |
184.0 |
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 303.15 |
203.0 |
| 313.15 |
221.0 |
| 323.15 |
230.0 |
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 333.15 |
221.0 |
| 343.15 |
206.0 |
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 353.15 |
203.0 |
| 363.15 |
181.0 |
| 371.15 |
169.0 |
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 273.35 |
121.0 |
| 283.15 |
156.0 |
| 293.15 |
184.0 |
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 303.15 |
203.0 |
| 313.15 |
221.0 |
| 323.15 |
230.0 |
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 333.15 |
221.0 |
| 343.15 |
206.0 |
Activity coefficient of 1-Pentanol (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Pentanol (1) - Liquid |
| 353.15 |
203.0 |
| 363.15 |
181.0 |
| 371.15 |
169.0 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 283.15 |
0.0032 |
| 323.15 |
0.0024 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 283.15 |
0.6526 |
| 323.15 |
0.6086 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
500 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 298.15 |
0.0040 |
| 323.15 |
0.0036 |
Mass fraction of 1-Pentanol (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 2)
- Temperature, K = 298 (Liquid mixture 2)
| Mass fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 0.8973 |
| 0.0215 |
Mole fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 303.15 |
101.00 |
0.6580 |
Mole fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 303.15 |
101.00 |
0.0050 |
Mass fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid mixture 1)
- Temperature, K = 298.15 (Liquid mixture 1)
| Mass fraction of Water (2) - Liquid mixture 1 |
| 0.1014 |
| 0.9757 |
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 |
| 293.15 |
0.1031 |
| 293.15 |
0.9757 |
| 313.15 |
0.1157 |
| 313.15 |
0.9794 |
| 333.15 |
0.1391 |
| 333.15 |
0.9808 |
Mass fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 298.20 |
101.00 |
0.0208 |
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 |
| 298.20 |
101.00 |
0.1075 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.9950 |
| 308.15 |
0.9980 |
| 318.15 |
0.9920 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
0.3630 |
| 308.15 |
0.3480 |
| 318.15 |
0.3470 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.33 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 293.15 |
0.0049 |
| 303.15 |
0.0047 |
| 313.15 |
0.0044 |
| 323.15 |
0.0042 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.33 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 293.15 |
0.6562 |
| 303.15 |
0.6484 |
| 313.15 |
0.6408 |
| 323.15 |
0.6245 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 283.15 |
0.0032 |
| 323.15 |
0.0024 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 283.15 |
0.6526 |
| 323.15 |
0.6086 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
500 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 298.15 |
0.0040 |
| 323.15 |
0.0036 |
Mass fraction of 1-Pentanol (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid mixture 2)
- Temperature, K = 298 (Liquid mixture 2)
| Mass fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 0.8973 |
| 0.0215 |
Mole fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 303.15 |
101.00 |
0.6580 |
Mole fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 303.15 |
101.00 |
0.0050 |
Mass fraction of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid mixture 1)
- Temperature, K = 298.15 (Liquid mixture 1)
| Mass fraction of Water (2) - Liquid mixture 1 |
| 0.1014 |
| 0.9757 |
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 |
| 293.15 |
0.1031 |
| 293.15 |
0.9757 |
| 313.15 |
0.1157 |
| 313.15 |
0.9794 |
| 333.15 |
0.1391 |
| 333.15 |
0.9808 |
Mass fraction of 1-Pentanol (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 298.20 |
101.00 |
0.0208 |
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 |
| 298.20 |
101.00 |
0.1075 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.9950 |
| 308.15 |
0.9980 |
| 318.15 |
0.9920 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
0.3630 |
| 308.15 |
0.3480 |
| 318.15 |
0.3470 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.33 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 2 |
| 293.15 |
0.0049 |
| 303.15 |
0.0047 |
| 313.15 |
0.0044 |
| 323.15 |
0.0042 |
Mole fraction of 1-Pentanol (1)
[ref]
Operational condition: Pressure, kPa =
101.33 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Pentanol (1) - Liquid mixture 1 |
| 293.15 |
0.6562 |
| 303.15 |
0.6484 |
| 313.15 |
0.6408 |
| 323.15 |
0.6245 |
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 |
0.0040 |
| 288.15 |
0.0042 |
| 298.15 |
0.0043 |
| 308.15 |
0.0045 |
| 318.15 |
0.0045 |
| 328.15 |
0.0044 |
| 338.15 |
0.0044 |
| 348.15 |
0.0042 |
| 358.15 |
0.0039 |
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 |
0.0040 |
| 288.15 |
0.0042 |
| 298.15 |
0.0043 |
| 308.15 |
0.0045 |
| 318.15 |
0.0045 |
| 328.15 |
0.0044 |
| 338.15 |
0.0044 |
| 348.15 |
0.0042 |
| 358.15 |
0.0039 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mass fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.1014 |
1.4019 |
| 0.9757 |
1.3348 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mass fraction of Water (2) - Liquid |
Refractive index (Na D-line) - Liquid |
| 0.1014 |
1.4019 |
| 0.9757 |
1.3348 |
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 |
996.38 |
| 288.15 |
995.67 |
| 298.15 |
993.79 |
| 308.15 |
990.95 |
| 318.15 |
987.22 |
| 328.15 |
982.82 |
| 338.15 |
977.69 |
| 348.15 |
972.04 |
| 358.15 |
965.99 |
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 |
843.2 |
| 288.15 |
836.12 |
| 298.15 |
829.21 |
| 308.15 |
822.26 |
| 318.15 |
814.67 |
| 328.15 |
808.36 |
| 338.15 |
801.55 |
| 348.15 |
791.23 |
| 358.15 |
787.64 |
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 |
996.38 |
| 288.15 |
995.67 |
| 298.15 |
993.79 |
| 308.15 |
990.95 |
| 318.15 |
987.22 |
| 328.15 |
982.82 |
| 338.15 |
977.69 |
| 348.15 |
972.04 |
| 358.15 |
965.99 |
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 |
843.2 |
| 288.15 |
836.12 |
| 298.15 |
829.21 |
| 308.15 |
822.26 |
| 318.15 |
814.67 |
| 328.15 |
808.36 |
| 338.15 |
801.55 |
| 348.15 |
791.23 |
| 358.15 |
787.64 |
Sources
-
Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
-
Salting effect on the liquid liquid equilibria for the ternary system water +N-methyl-2-pyrrolidone + 1-pentanol
-
Liquid-liquid equilibrium of (water + 1-propanol + 1-pentanol) system at 298.15 and 323.15 K
-
The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
-
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.
-
Solubility, liquid-liquid equilibrium and critical states for quaternary system acetic acid - n-amyl alcohol - n-amyl acetate - water at 303.15 K and atmospheric pressure
-
Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
-
Studying the Liquid-Liquid Equilibrium of Systems Water +2-Hydroxyethylammonium Propanoate or 2-Hydroxyethylammonium Butanoate or 2-Hydroxyethylammonium Pentanoate +1-Pentanol at 293.15, 313.15, and 333.15 K: Experimental Determination and Thermodynamic Modeling
-
Synergistic Extraction of Hydroquinone from Aqueous Solution with Solvent Mixture of 2-Pentanone and n-Pentanol: Liquid-Liquid Equilibria and Data Correlation
-
Liquid-Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures
-
Liquid-Liquid Equilibria of Water + Pentan-1-ol + 2,6,6-Trimethylbicyclo[3.1.1]hep-2-ene or 6,6-Dimethyl-2-methylenebicyclo[3.1.1]heptane at (293.15, 303.15, 313.15, and 323.15) K