Mixture of Propyl vinyl ether + Ethanol

Datasets

1. Mole fraction
2. Excess molar enthalpy (molar enthalpy
3. n₀ - Refractive index (Na D-line)
4. ρ_l - Mass density, kg/m3

Mole fraction of Propyl vinyl ether (1) [ref]

Operational condition: Temperature, K = 323.15 (Gas)

Mole fraction of Propyl vinyl ether (1) - Liquid	Mole fraction of Propyl vinyl ether (1) - Gas
0.0201	0.1681
0.0398	0.2625
0.0592	0.2997
0.0797	0.3702
0.1193	0.4554
0.1688	0.5189
0.2290	0.5670
0.2898	0.6081
0.3490	0.6253
0.4086	0.6476
0.4686	0.6621
0.5294	0.6837
0.5894	0.7087
0.6512	0.7311
0.7088	0.7562
0.7700	0.7799
0.8287	0.8009
0.8778	0.8297
0.9195	0.8549
0.9416	0.8772
0.9601	0.9087
0.9784	0.9397

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mole fraction of Propyl vinyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0265	0.0585
0.0543	0.1189
0.0836	0.1845
0.1145	0.2518
0.1470	0.3203
0.1814	0.3914
0.2178	0.4648
0.2564	0.5390
0.2973	0.6123
0.3409	0.6857
0.3873	0.7481
0.4368	0.8145
0.4899	0.8742
0.5468	0.9245
0.6080	0.9602
0.6741	0.9745
0.7456	0.9505
0.8231	0.8673
0.9076	0.6556

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Propyl vinyl ether (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3616
0.0499	1.3637
0.1000	1.3655
0.2002	1.3695
0.2996	1.3736
0.4004	1.3769
0.5006	1.3802
0.6005	1.3826
0.7005	1.3852
0.8002	1.3872
0.8997	1.3893
0.9492	1.3901
1.0000	1.3909

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 293.15 (Liquid)

Mole fraction of Propyl vinyl ether (1) - Liquid	Mass density, kg/m3 - Liquid
0.0499	787.89
0.1000	786.34
0.2002	783.37
0.2996	780.78
0.4004	778.49
0.5006	776.39
0.6005	774.44
0.7005	772.61
0.8002	771.01
0.8997	769.67
0.9492	769.18

Sources

• Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
• Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
• Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K