Mixture of Benzene + 1-Propanol + n-Butyl ether

Datasets

1. Molar enthalpy of mixing with solvent, kJ/mol (2)

Molar enthalpy of mixing with solvent, kJ/mol of Benzene (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Benzene (1) - Liquid	Solvent: Mole fraction of 1-Propanol (2) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of Benzene (1) - Liquid
298.15	0.9504	0.8000	0.4540
298.15	0.9006	0.8000	0.6640
298.15	0.8504	0.8000	0.7840
298.15	0.8000	0.8000	0.8570
298.15	0.7004	0.8000	0.9160
298.15	0.5999	0.8000	0.8940
298.15	0.5003	0.8000	0.8170
298.15	0.3998	0.8000	0.6980
298.15	0.3003	0.8000	0.5490
298.15	0.1998	0.8000	0.3750
298.15	0.1004	0.8000	0.1900
298.15	0.9503	0.6000	0.3750
298.15	0.8992	0.6000	0.5650
298.15	0.8503	0.6000	0.6680
298.15	0.8000	0.6000	0.7300
298.15	0.6993	0.6000	0.7780
298.15	0.5992	0.6000	0.7580
298.15	0.5002	0.6000	0.6910
298.15	0.4006	0.6000	0.5910
298.15	0.3008	0.6000	0.4640
298.15	0.2010	0.6000	0.3210
298.15	0.0990	0.6000	0.1600
298.15	0.9501	0.4000	0.2820
298.15	0.8993	0.4000	0.4490
298.15	0.8506	0.4000	0.5420
298.15	0.7997	0.4000	0.6010
298.15	0.6997	0.4000	0.6470
298.15	0.6001	0.4000	0.6330
298.15	0.5003	0.4000	0.5790
298.15	0.3990	0.4000	0.4940
298.15	0.2990	0.4000	0.3890
298.15	0.1991	0.4000	0.2680
298.15	0.1001	0.4000	0.1370
298.15	0.9498	0.2001	0.1840
298.15	0.9001	0.2001	0.3130
298.15	0.8498	0.2001	0.3980
298.15	0.7993	0.2001	0.4530
298.15	0.7001	0.2001	0.5050
298.15	0.5998	0.2001	0.5030
298.15	0.5005	0.2001	0.4640
298.15	0.3991	0.2001	0.4000
298.15	0.2998	0.2001	0.3170
298.15	0.1989	0.2001	0.2190
298.15	0.1006	0.2001	0.1150
313.15	0.9007	0.8001	0.7470
313.15	0.8003	0.8001	0.9900
313.15	0.7008	0.8001	1.068
313.15	0.6003	0.8001	1.051
313.15	0.5007	0.8001	0.9680
313.15	0.4002	0.8001	0.8330
313.15	0.3006	0.8001	0.6580
313.15	0.2001	0.8001	0.4530
313.15	0.1505	0.8001	0.3440
313.15	0.1006	0.8001	0.2320
313.15	0.0504	0.8001	0.1160
313.15	0.8995	0.6000	0.6170
313.15	0.8003	0.6000	0.8220
313.15	0.6997	0.6000	0.8850
313.15	0.5996	0.6000	0.8660
313.15	0.5506	0.6000	0.8360
313.15	0.5006	0.6000	0.7940
313.15	0.4493	0.6000	0.7400
313.15	0.4010	0.6000	0.6800
313.15	0.3012	0.6000	0.5370
313.15	0.2013	0.6000	0.3710
313.15	0.0992	0.6000	0.1870
313.15	0.8994	0.3999	0.4670
313.15	0.8000	0.3999	0.6490
313.15	0.7000	0.3999	0.7070
313.15	0.6005	0.3999	0.6940
313.15	0.5008	0.3999	0.6370
313.15	0.3994	0.3999	0.5440
313.15	0.2993	0.3999	0.4290
313.15	0.1993	0.3999	0.2960
313.15	0.1493	0.3999	0.2250
313.15	0.1003	0.3999	0.1520
313.15	0.0495	0.3999	0.0760
313.15	0.9003	0.1998	0.3000
313.15	0.7996	0.1998	0.4520
313.15	0.7005	0.1998	0.5100
313.15	0.6004	0.1998	0.5120
313.15	0.5009	0.1998	0.4750
313.15	0.3995	0.1998	0.4100
313.15	0.3001	0.1998	0.3260
313.15	0.1992	0.1998	0.2250
313.15	0.1496	0.1998	0.1720
313.15	0.1007	0.1998	0.1170
313.15	0.0498	0.1998	0.0570

Molar enthalpy of mixing with solvent, kJ/mol of Benzene (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Benzene (1) - Liquid	Solvent: Mole fraction of 1-Propanol (2) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of Benzene (1) - Liquid
298.15	0.9504	0.8000	0.4540
298.15	0.9006	0.8000	0.6640
298.15	0.8504	0.8000	0.7840
298.15	0.8000	0.8000	0.8570
298.15	0.7004	0.8000	0.9160
298.15	0.5999	0.8000	0.8940
298.15	0.5003	0.8000	0.8170
298.15	0.3998	0.8000	0.6980
298.15	0.3003	0.8000	0.5490
298.15	0.1998	0.8000	0.3750
298.15	0.1004	0.8000	0.1900
298.15	0.9503	0.6000	0.3750
298.15	0.8992	0.6000	0.5650
298.15	0.8503	0.6000	0.6680
298.15	0.8000	0.6000	0.7300
298.15	0.6993	0.6000	0.7780
298.15	0.5992	0.6000	0.7580
298.15	0.5002	0.6000	0.6910
298.15	0.4006	0.6000	0.5910
298.15	0.3008	0.6000	0.4640
298.15	0.2010	0.6000	0.3210
298.15	0.0990	0.6000	0.1600
298.15	0.9501	0.4000	0.2820
298.15	0.8993	0.4000	0.4490
298.15	0.8506	0.4000	0.5420
298.15	0.7997	0.4000	0.6010
298.15	0.6997	0.4000	0.6470
298.15	0.6001	0.4000	0.6330
298.15	0.5003	0.4000	0.5790
298.15	0.3990	0.4000	0.4940
298.15	0.2990	0.4000	0.3890
298.15	0.1991	0.4000	0.2680
298.15	0.1001	0.4000	0.1370
298.15	0.9498	0.2001	0.1840
298.15	0.9001	0.2001	0.3130
298.15	0.8498	0.2001	0.3980
298.15	0.7993	0.2001	0.4530
298.15	0.7001	0.2001	0.5050
298.15	0.5998	0.2001	0.5030
298.15	0.5005	0.2001	0.4640
298.15	0.3991	0.2001	0.4000
298.15	0.2998	0.2001	0.3170
298.15	0.1989	0.2001	0.2190
298.15	0.1006	0.2001	0.1150
313.15	0.9007	0.8001	0.7470
313.15	0.8003	0.8001	0.9900
313.15	0.7008	0.8001	1.068
313.15	0.6003	0.8001	1.051
313.15	0.5007	0.8001	0.9680
313.15	0.4002	0.8001	0.8330
313.15	0.3006	0.8001	0.6580
313.15	0.2001	0.8001	0.4530
313.15	0.1505	0.8001	0.3440
313.15	0.1006	0.8001	0.2320
313.15	0.0504	0.8001	0.1160
313.15	0.8995	0.6000	0.6170
313.15	0.8003	0.6000	0.8220
313.15	0.6997	0.6000	0.8850
313.15	0.5996	0.6000	0.8660
313.15	0.5506	0.6000	0.8360
313.15	0.5006	0.6000	0.7940
313.15	0.4493	0.6000	0.7400
313.15	0.4010	0.6000	0.6800
313.15	0.3012	0.6000	0.5370
313.15	0.2013	0.6000	0.3710
313.15	0.0992	0.6000	0.1870
313.15	0.8994	0.3999	0.4670
313.15	0.8000	0.3999	0.6490
313.15	0.7000	0.3999	0.7070
313.15	0.6005	0.3999	0.6940
313.15	0.5008	0.3999	0.6370
313.15	0.3994	0.3999	0.5440
313.15	0.2993	0.3999	0.4290
313.15	0.1993	0.3999	0.2960
313.15	0.1493	0.3999	0.2250
313.15	0.1003	0.3999	0.1520
313.15	0.0495	0.3999	0.0760
313.15	0.9003	0.1998	0.3000
313.15	0.7996	0.1998	0.4520
313.15	0.7005	0.1998	0.5100
313.15	0.6004	0.1998	0.5120
313.15	0.5009	0.1998	0.4750
313.15	0.3995	0.1998	0.4100
313.15	0.3001	0.1998	0.3260
313.15	0.1992	0.1998	0.2250
313.15	0.1496	0.1998	0.1720
313.15	0.1007	0.1998	0.1170
313.15	0.0498	0.1998	0.0570

Sources

• Excess enthalpies of ternary mixtures of (oxygenated additives + aromatic hydrocarbon) mixtures in fuels and bio-fuels: (Dibutyl-ether + 1-propanol + benzene), or toluene, at T = (298.15 and 313.15) K