Mixture of Diisopropyl ether + 1-Propanol, 2-methyl-

Datasets

1. Excess molar enthalpy (molar enthalpy (2)
2. P_vap - Vapor or sublimation pressure, kPa

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

Operational conditions:

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

Mole fraction of Diisopropyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0890	0.0450
0.1400	0.1179
0.1920	0.1952
0.2540	0.2893
0.3090	0.3654
0.3390	0.3996
0.3750	0.4185
0.4310	0.4445
0.5050	0.4623
0.6010	0.4598
0.6370	0.4606
0.7030	0.4421
0.7690	0.4140
0.8040	0.3963
0.8440	0.3582
0.9230	0.2381

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

Fixed			Measured
Mole fraction of Diisopropyl ether (1) - Liquid	Pressure, kPa - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.5000	101.00	303.15	0.4669

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	4.00
0.0582	8.05
0.1047	10.98
0.1562	13.89
0.2026	16.20
0.2497	18.30
0.3012	20.33
0.3027	20.39
0.3486	21.98
0.3998	23.59
0.4041	23.74
0.4445	24.85
0.4511	25.06
0.4993	26.27
0.5013	26.34
0.5492	27.45
0.5516	27.52
0.5998	28.56
0.6037	28.65
0.6484	29.57
0.6870	30.32
0.7004	30.59
0.7506	31.59
0.8008	32.58
0.8502	33.59
0.9006	34.68
0.9505	35.85
1.0000	37.11

Sources

• Phase equilibria properties of binary and ternary systems containing di-isopropyl ether + isobutanol + benzene at 313.15K
• Experimental and predicted excess molar enthalpies of binary mixtures containing 2,2'-oxybis[propane], benzene, butan-1-ol, 2-methylpropan-1-ol, 2-methyl-2-ene-1-propanol at 303.15 K

Note: These property values are available through the Cheméo API. A free account gives you an access key.