Mixture of 1-Decanol + Water

Datasets

1. Mole fraction (12)
2. n₀ - Refractive index (Na D-line) (2)

Mole fraction of Water (2) [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid mixture 1)
• Temperature, K = 298.2 (Liquid mixture 1)

Mole fraction of Water (2) - Liquid mixture 1
0.9997
0.9998

Mole fraction of Water (2) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid mixture 2)
• Pressure, kPa = 101.3 (Liquid mixture 2)

Mole fraction of Water (2) - Liquid mixture 2
0.1765
0.1784

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 1
298.20	0.0200
303.20	0.0200
313.20	0.0220
323.20	0.0220

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 1
303.20	0.9994
303.20	0.0142
313.20	0.9989
313.20	0.0161
323.20	0.9983
323.20	0.0207

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	0.9975
308.20	0.9938
318.20	0.9901
328.20	0.9864

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 2
288.15	0.0334
298.15	0.0268

Mole fraction of Water (2) [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid mixture 1)
• Temperature, K = 298.2 (Liquid mixture 1)

Mole fraction of Water (2) - Liquid mixture 1
0.9997
0.9998

Mole fraction of Water (2) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid mixture 2)
• Pressure, kPa = 101.3 (Liquid mixture 2)

Mole fraction of Water (2) - Liquid mixture 2
0.1765
0.1784

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 1
298.20	0.0200
303.20	0.0200
313.20	0.0220
323.20	0.0220

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 1
303.20	0.9994
303.20	0.0142
313.20	0.9989
313.20	0.0161
323.20	0.9983
323.20	0.0207

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	0.9975
308.20	0.9938
318.20	0.9901
328.20	0.9864

Mass fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 2	Mass fraction of Water (2) - Liquid mixture 2
288.15	0.0334
298.15	0.0268

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
298.20	0.9975	1.3355
308.20	0.9938	1.3346
318.20	0.9901	1.3332
328.20	0.9864	1.3322

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
298.20	0.9975	1.3355
308.20	0.9938	1.3346
318.20	0.9901	1.3332
328.20	0.9864	1.3322

Sources

• Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
• Tie-line data for water- formic acid-1-decanol ternary system at T = (298.2, 303.2, 313.2, 323.2) K
• Solubility and Tie Line Data of the Water - Phosphoric Acid Solvents at T = (303.2 and 313.2) K: An Experimental and Correlational Study
• Experimental Data of Citric Acid Extraction from Aqueous Solution with 1-Decanol by Using Liquid-Liquid Equilibrium
• Influence of the Temperature on the Liquid-Liquid-Solid Equilibria of the Ternary System Water + Ethanol + 1-Decanol