Mixture of Benzene + 1-Propanol, 2-methyl-

Datasets

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

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

Fixed			Measured
Mole fraction of Benzene (1) - Liquid	Pressure, kPa - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.5000	101.00	303.15	1.4976

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

Operational conditions:

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

Mole fraction of Benzene (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1090	0.3583
0.1690	0.5511
0.2310	0.7606
0.3520	1.1094
0.4480	1.4003
0.4980	1.4925
0.5380	1.566
0.6020	1.6251
0.6990	1.5801
0.7950	1.36
0.8360	1.1801
0.8910	0.8836
0.9300	0.6104

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Benzene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	4.00
0.0584	8.18
0.0982	10.54
0.1500	13.10
0.2072	15.36
0.2539	16.88
0.2995	18.06
0.3496	19.16
0.3991	20.05
0.3996	20.08
0.4488	20.81
0.4495	20.83
0.4994	21.46
0.4995	21.45
0.5492	21.99
0.5495	22.00
0.5990	22.46
0.6013	22.48
0.6488	22.88
0.6995	23.25
0.7491	23.57
0.8001	23.88
0.8553	24.14
0.8990	24.34
0.9518	24.52
1.0000	24.38

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.3009	23.23
0.6935	18.25

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.