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

Datasets

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

Molar enthalpy of mixing with solvent, kJ/mol of Toluene (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Toluene (2) - Liquid	Solvent: Mole fraction of 1-Propanol (1) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of Toluene (2) - Liquid
298.15	0.9566	0.8000	0.4400
298.15	0.9111	0.8000	0.6320
298.15	0.8676	0.8000	0.7300
298.15	0.8220	0.8000	0.7910
298.15	0.7286	0.8000	0.8390
298.15	0.6331	0.8000	0.8180
298.15	0.5353	0.8000	0.7480
298.15	0.4353	0.8000	0.6440
298.15	0.3310	0.8000	0.5070
298.15	0.2244	0.8000	0.3500
298.15	0.1134	0.8000	0.1770
298.15	0.9507	0.6000	0.3370
298.15	0.8993	0.6000	0.4960
298.15	0.8494	0.6000	0.5750
298.15	0.7993	0.6000	0.6150
298.15	0.7001	0.6000	0.6340
298.15	0.5998	0.6000	0.6020
298.15	0.5003	0.6000	0.5390
298.15	0.3996	0.6000	0.4520
298.15	0.2999	0.6000	0.3500
298.15	0.2010	0.6000	0.2390
298.15	0.1011	0.6000	0.1200
298.15	0.9493	0.3999	0.2360
298.15	0.9008	0.3999	0.3560
298.15	0.8494	0.3999	0.4250
298.15	0.8003	0.3999	0.4560
298.15	0.7006	0.3999	0.4690
298.15	0.6001	0.3999	0.4450
298.15	0.4992	0.3999	0.3940
298.15	0.4000	0.3999	0.3300
298.15	0.3010	0.3999	0.2560
298.15	0.2000	0.3999	0.1730
298.15	0.0996	0.3999	0.0870
298.15	0.9496	0.2000	0.1220
298.15	0.9000	0.2000	0.1990
298.15	0.8500	0.2000	0.2480
298.15	0.7997	0.2000	0.2750
298.15	0.6998	0.2000	0.2920
298.15	0.5998	0.2000	0.2800
298.15	0.5003	0.2000	0.2520
298.15	0.4001	0.2000	0.2110
298.15	0.2998	0.2000	0.1640
298.15	0.2001	0.2000	0.1120
298.15	0.0991	0.2000	0.0550
313.15	0.9566	0.8000	0.4780
313.15	0.9111	0.8000	0.7300
313.15	0.8675	0.8000	0.8620
313.15	0.8220	0.8000	0.9450
313.15	0.7287	0.8000	1.022
313.15	0.6332	0.8000	1.011
313.15	0.5354	0.8000	0.9420
313.15	0.4355	0.8000	0.8260
313.15	0.3311	0.8000	0.6630
313.15	0.2245	0.8000	0.4610
313.15	0.1134	0.8000	0.2400
313.15	0.8993	0.6001	0.5750
313.15	0.7993	0.6001	0.7450
313.15	0.7001	0.6001	0.7860
313.15	0.5998	0.6001	0.7570
313.15	0.5003	0.6001	0.6880
313.15	0.3997	0.6001	0.5860
313.15	0.2999	0.6001	0.4600
313.15	0.2011	0.6001	0.3190
313.15	0.1011	0.6001	0.1640
313.15	0.9493	0.4000	0.2460
313.15	0.9008	0.4000	0.3930
313.15	0.8494	0.4000	0.4880
313.15	0.8003	0.4000	0.5370
313.15	0.7006	0.4000	0.5700
313.15	0.6002	0.4000	0.5480
313.15	0.4992	0.4000	0.4930
313.15	0.4001	0.4000	0.4180
313.15	0.3010	0.4000	0.3270
313.15	0.2001	0.4000	0.2240
313.15	0.0996	0.4000	0.1140
313.15	0.9496	0.2000	0.1200
313.15	0.9001	0.2000	0.2070
313.15	0.8501	0.2000	0.2690
313.15	0.7998	0.2000	0.3050
313.15	0.7000	0.2000	0.3360
313.15	0.5998	0.2000	0.3300
313.15	0.5004	0.2000	0.3020
313.15	0.4002	0.2000	0.2570
313.15	0.2998	0.2000	0.2020
313.15	0.2002	0.2000	0.1400
313.15	0.0991	0.2000	0.0710

Molar enthalpy of mixing with solvent, kJ/mol of Toluene (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Toluene (2) - Liquid	Solvent: Mole fraction of 1-Propanol (1) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of Toluene (2) - Liquid
298.15	0.9566	0.8000	0.4400
298.15	0.9111	0.8000	0.6320
298.15	0.8676	0.8000	0.7300
298.15	0.8220	0.8000	0.7910
298.15	0.7286	0.8000	0.8390
298.15	0.6331	0.8000	0.8180
298.15	0.5353	0.8000	0.7480
298.15	0.4353	0.8000	0.6440
298.15	0.3310	0.8000	0.5070
298.15	0.2244	0.8000	0.3500
298.15	0.1134	0.8000	0.1770
298.15	0.9507	0.6000	0.3370
298.15	0.8993	0.6000	0.4960
298.15	0.8494	0.6000	0.5750
298.15	0.7993	0.6000	0.6150
298.15	0.7001	0.6000	0.6340
298.15	0.5998	0.6000	0.6020
298.15	0.5003	0.6000	0.5390
298.15	0.3996	0.6000	0.4520
298.15	0.2999	0.6000	0.3500
298.15	0.2010	0.6000	0.2390
298.15	0.1011	0.6000	0.1200
298.15	0.9493	0.3999	0.2360
298.15	0.9008	0.3999	0.3560
298.15	0.8494	0.3999	0.4250
298.15	0.8003	0.3999	0.4560
298.15	0.7006	0.3999	0.4690
298.15	0.6001	0.3999	0.4450
298.15	0.4992	0.3999	0.3940
298.15	0.4000	0.3999	0.3300
298.15	0.3010	0.3999	0.2560
298.15	0.2000	0.3999	0.1730
298.15	0.0996	0.3999	0.0870
298.15	0.9496	0.2000	0.1220
298.15	0.9000	0.2000	0.1990
298.15	0.8500	0.2000	0.2480
298.15	0.7997	0.2000	0.2750
298.15	0.6998	0.2000	0.2920
298.15	0.5998	0.2000	0.2800
298.15	0.5003	0.2000	0.2520
298.15	0.4001	0.2000	0.2110
298.15	0.2998	0.2000	0.1640
298.15	0.2001	0.2000	0.1120
298.15	0.0991	0.2000	0.0550
313.15	0.9566	0.8000	0.4780
313.15	0.9111	0.8000	0.7300
313.15	0.8675	0.8000	0.8620
313.15	0.8220	0.8000	0.9450
313.15	0.7287	0.8000	1.022
313.15	0.6332	0.8000	1.011
313.15	0.5354	0.8000	0.9420
313.15	0.4355	0.8000	0.8260
313.15	0.3311	0.8000	0.6630
313.15	0.2245	0.8000	0.4610
313.15	0.1134	0.8000	0.2400
313.15	0.8993	0.6001	0.5750
313.15	0.7993	0.6001	0.7450
313.15	0.7001	0.6001	0.7860
313.15	0.5998	0.6001	0.7570
313.15	0.5003	0.6001	0.6880
313.15	0.3997	0.6001	0.5860
313.15	0.2999	0.6001	0.4600
313.15	0.2011	0.6001	0.3190
313.15	0.1011	0.6001	0.1640
313.15	0.9493	0.4000	0.2460
313.15	0.9008	0.4000	0.3930
313.15	0.8494	0.4000	0.4880
313.15	0.8003	0.4000	0.5370
313.15	0.7006	0.4000	0.5700
313.15	0.6002	0.4000	0.5480
313.15	0.4992	0.4000	0.4930
313.15	0.4001	0.4000	0.4180
313.15	0.3010	0.4000	0.3270
313.15	0.2001	0.4000	0.2240
313.15	0.0996	0.4000	0.1140
313.15	0.9496	0.2000	0.1200
313.15	0.9001	0.2000	0.2070
313.15	0.8501	0.2000	0.2690
313.15	0.7998	0.2000	0.3050
313.15	0.7000	0.2000	0.3360
313.15	0.5998	0.2000	0.3300
313.15	0.5004	0.2000	0.3020
313.15	0.4002	0.2000	0.2570
313.15	0.2998	0.2000	0.2020
313.15	0.2002	0.2000	0.1400
313.15	0.0991	0.2000	0.0710

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