Mixture of n-Butyl ether + Cyclohexane

Datasets

1. Excess molar enthalpy (molar enthalpy (4)
2. P_vap - Vapor or sublimation pressure, kPa (4)

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0498	0.0738
0.0997	0.1291
0.1502	0.1713
0.2003	0.2032
0.2498	0.2246
0.3001	0.2398
0.3502	0.2470
0.3999	0.2496
0.4499	0.2474
0.4992	0.2414
0.5497	0.2299
0.6002	0.2166
0.6493	0.1984
0.6993	0.1777
0.7502	0.1535
0.7991	0.1251
0.8500	0.0981
0.9001	0.0659
0.9506	0.0327

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

Operational conditions:

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

Mole fraction of n-Butyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0499	0.0752
0.0997	0.1341
0.1502	0.1804
0.2002	0.2145
0.2497	0.2385
0.2999	0.2554
0.3500	0.2649
0.3996	0.2686
0.4497	0.2664
0.4990	0.2596
0.5495	0.2481
0.6000	0.2326
0.6491	0.2139
0.6992	0.1911
0.7501	0.1641
0.7990	0.1367
0.8500	0.1041
0.9001	0.0693
0.9507	0.0328

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

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0498	0.0738
0.0997	0.1291
0.1502	0.1713
0.2003	0.2032
0.2498	0.2246
0.3001	0.2398
0.3502	0.2470
0.3999	0.2496
0.4499	0.2474
0.4992	0.2414
0.5497	0.2299
0.6002	0.2166
0.6493	0.1984
0.6993	0.1777
0.7502	0.1535
0.7991	0.1251
0.8500	0.0981
0.9001	0.0659
0.9506	0.0327

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

Operational conditions:

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

Mole fraction of n-Butyl ether (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0499	0.0752
0.0997	0.1341
0.1502	0.1804
0.2002	0.2145
0.2497	0.2385
0.2999	0.2554
0.3500	0.2649
0.3996	0.2686
0.4497	0.2664
0.4990	0.2596
0.5495	0.2481
0.6000	0.2326
0.6491	0.2139
0.6992	0.1911
0.7501	0.1641
0.7990	0.1367
0.8500	0.1041
0.9001	0.0693
0.9507	0.0328

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	24.62
0.0464	23.57
0.1048	22.24
0.1511	21.21
0.1998	20.12
0.2524	18.93
0.3011	17.83
0.3044	17.76
0.3502	16.73
0.3973	15.65
0.4003	15.58
0.4479	14.49
0.4484	14.49
0.4985	13.35
0.5006	13.30
0.5470	12.25
0.5478	12.23
0.5980	11.09
0.5991	11.07
0.6534	9.85
0.6988	8.81
0.7560	7.52
0.7999	6.53
0.8381	5.68
0.8539	5.31
0.8964	4.35
0.9550	3.06
1.0000	2.06

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2975	17.90
0.3153	17.55
0.6878	9.10
0.7139	8.51

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	24.62
0.0464	23.57
0.1048	22.24
0.1511	21.21
0.1998	20.12
0.2524	18.93
0.3011	17.83
0.3044	17.76
0.3502	16.73
0.3973	15.65
0.4003	15.58
0.4479	14.49
0.4484	14.49
0.4985	13.35
0.5006	13.30
0.5470	12.25
0.5478	12.23
0.5980	11.09
0.5991	11.07
0.6534	9.85
0.6988	8.81
0.7560	7.52
0.7999	6.53
0.8381	5.68
0.8539	5.31
0.8964	4.35
0.9550	3.06
1.0000	2.06

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of n-Butyl ether (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.2975	17.90
0.3153	17.55
0.6878	9.10
0.7139	8.51

Sources

• Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
• Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and Heptane or 1-Hexene at T ) 313.15 K
• Excess Enthalpies of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and 1-Butanol at 298.15 K