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

Datasets

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

Molar enthalpy of mixing with solvent, kJ/mol of 1-Hexene (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (3) - Liquid	Mole fraction of 1-Hexene (2) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of 1-Hexene (2) - Liquid
298.15	0.2499	0.9498	0.3700
298.15	0.2499	0.8996	0.4670
298.15	0.2499	0.8506	0.5120
298.15	0.2499	0.8005	0.5420
298.15	0.2499	0.7006	0.5550
298.15	0.2499	0.6006	0.5290
298.15	0.2499	0.4997	0.4720
298.15	0.2499	0.4005	0.3980
298.15	0.2499	0.3006	0.3090
298.15	0.2499	0.2004	0.2100
298.15	0.2499	0.1006	0.1060
298.15	0.6667	0.9502	0.3010
298.15	0.6667	0.8998	0.3780
298.15	0.6667	0.8498	0.4100
298.15	0.6667	0.7993	0.4250
298.15	0.6667	0.7000	0.4240
298.15	0.6667	0.5995	0.3970
298.15	0.6667	0.4992	0.3510
298.15	0.6667	0.4001	0.2950
298.15	0.6667	0.3001	0.2280
298.15	0.6667	0.1995	0.1550
298.15	0.6667	0.1001	0.0780
298.15	1.5005	0.9504	0.2250
298.15	1.5005	0.8996	0.2900
298.15	1.5005	0.8504	0.3130
298.15	1.5005	0.8000	0.3200
298.15	1.5005	0.7004	0.3120
298.15	1.5005	0.5999	0.2860
298.15	1.5005	0.5004	0.2490
298.15	1.5005	0.3999	0.2070
298.15	1.5005	0.3004	0.1590
298.15	1.5005	0.1999	0.1080
298.15	1.5005	0.1005	0.0540
298.15	4.0052	0.9496	0.1220
298.15	4.0052	0.8999	0.1740
298.15	4.0052	0.8501	0.1940
298.15	4.0052	0.8002	0.1990
298.15	4.0052	0.7001	0.1910
298.15	4.0052	0.6000	0.1720
298.15	4.0052	0.5000	0.1470
298.15	4.0052	0.4005	0.1200
298.15	4.0052	0.3004	0.0900
298.15	4.0052	0.2000	0.0600
298.15	4.0052	0.1006	0.0300
313.15	0.2500	0.9498	0.4660
313.15	0.2500	0.8997	0.6100
313.15	0.2500	0.8507	0.6800
313.15	0.2500	0.8006	0.7190
313.15	0.2500	0.7007	0.7410
313.15	0.2500	0.6007	0.7100
313.15	0.2500	0.4998	0.6410
313.15	0.2500	0.4006	0.5430
313.15	0.2500	0.3006	0.4260
313.15	0.2500	0.2004	0.2920
313.15	0.2500	0.1005	0.1490
313.15	0.6667	0.9502	0.3690
313.15	0.6667	0.8998	0.4920
313.15	0.6667	0.8499	0.5460
313.15	0.6667	0.8005	0.5700
313.15	0.6667	0.7000	0.5750
313.15	0.6667	0.5997	0.5410
313.15	0.6667	0.5004	0.4840
313.15	0.6667	0.4001	0.4080
313.15	0.6667	0.3001	0.3190
313.15	0.6667	0.2004	0.2190
313.15	0.6667	0.1001	0.1110
313.15	1.5003	0.9504	0.2570
313.15	1.5003	0.8996	0.3640
313.15	1.5003	0.8505	0.4070
313.15	1.5003	0.8000	0.4240
313.15	1.5003	0.7004	0.4200
313.15	1.5003	0.5998	0.3890
313.15	1.5003	0.5003	0.3430
313.15	1.5003	0.3998	0.2860
313.15	1.5003	0.3003	0.2210
313.15	1.5003	0.1999	0.1500
313.15	1.5003	0.1004	0.0770
313.15	4.0036	0.9496	0.1250
313.15	4.0036	0.9000	0.1960
313.15	4.0036	0.8499	0.2320
313.15	4.0036	0.7001	0.2460
313.15	4.0036	0.5999	0.2280
313.15	4.0036	0.5000	0.1980
313.15	4.0036	0.4003	0.1630
313.15	4.0036	0.3003	0.1250
313.15	4.0036	0.1999	0.0840
313.15	4.0036	0.1006	0.0420

Molar enthalpy of mixing with solvent, kJ/mol of 1-Hexene (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Solvent: Amount ratio of component to other component of binary solvent of n-Butyl ether (3) - Liquid	Mole fraction of 1-Hexene (2) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of 1-Hexene (2) - Liquid
298.15	0.2499	0.9498	0.3700
298.15	0.2499	0.8996	0.4670
298.15	0.2499	0.8506	0.5120
298.15	0.2499	0.8005	0.5420
298.15	0.2499	0.7006	0.5550
298.15	0.2499	0.6006	0.5290
298.15	0.2499	0.4997	0.4720
298.15	0.2499	0.4005	0.3980
298.15	0.2499	0.3006	0.3090
298.15	0.2499	0.2004	0.2100
298.15	0.2499	0.1006	0.1060
298.15	0.6667	0.9502	0.3010
298.15	0.6667	0.8998	0.3780
298.15	0.6667	0.8498	0.4100
298.15	0.6667	0.7993	0.4250
298.15	0.6667	0.7000	0.4240
298.15	0.6667	0.5995	0.3970
298.15	0.6667	0.4992	0.3510
298.15	0.6667	0.4001	0.2950
298.15	0.6667	0.3001	0.2280
298.15	0.6667	0.1995	0.1550
298.15	0.6667	0.1001	0.0780
298.15	1.5005	0.9504	0.2250
298.15	1.5005	0.8996	0.2900
298.15	1.5005	0.8504	0.3130
298.15	1.5005	0.8000	0.3200
298.15	1.5005	0.7004	0.3120
298.15	1.5005	0.5999	0.2860
298.15	1.5005	0.5004	0.2490
298.15	1.5005	0.3999	0.2070
298.15	1.5005	0.3004	0.1590
298.15	1.5005	0.1999	0.1080
298.15	1.5005	0.1005	0.0540
298.15	4.0052	0.9496	0.1220
298.15	4.0052	0.8999	0.1740
298.15	4.0052	0.8501	0.1940
298.15	4.0052	0.8002	0.1990
298.15	4.0052	0.7001	0.1910
298.15	4.0052	0.6000	0.1720
298.15	4.0052	0.5000	0.1470
298.15	4.0052	0.4005	0.1200
298.15	4.0052	0.3004	0.0900
298.15	4.0052	0.2000	0.0600
298.15	4.0052	0.1006	0.0300
313.15	0.2500	0.9498	0.4660
313.15	0.2500	0.8997	0.6100
313.15	0.2500	0.8507	0.6800
313.15	0.2500	0.8006	0.7190
313.15	0.2500	0.7007	0.7410
313.15	0.2500	0.6007	0.7100
313.15	0.2500	0.4998	0.6410
313.15	0.2500	0.4006	0.5430
313.15	0.2500	0.3006	0.4260
313.15	0.2500	0.2004	0.2920
313.15	0.2500	0.1005	0.1490
313.15	0.6667	0.9502	0.3690
313.15	0.6667	0.8998	0.4920
313.15	0.6667	0.8499	0.5460
313.15	0.6667	0.8005	0.5700
313.15	0.6667	0.7000	0.5750
313.15	0.6667	0.5997	0.5410
313.15	0.6667	0.5004	0.4840
313.15	0.6667	0.4001	0.4080
313.15	0.6667	0.3001	0.3190
313.15	0.6667	0.2004	0.2190
313.15	0.6667	0.1001	0.1110
313.15	1.5003	0.9504	0.2570
313.15	1.5003	0.8996	0.3640
313.15	1.5003	0.8505	0.4070
313.15	1.5003	0.8000	0.4240
313.15	1.5003	0.7004	0.4200
313.15	1.5003	0.5998	0.3890
313.15	1.5003	0.5003	0.3430
313.15	1.5003	0.3998	0.2860
313.15	1.5003	0.3003	0.2210
313.15	1.5003	0.1999	0.1500
313.15	1.5003	0.1004	0.0770
313.15	4.0036	0.9496	0.1250
313.15	4.0036	0.9000	0.1960
313.15	4.0036	0.8499	0.2320
313.15	4.0036	0.7001	0.2460
313.15	4.0036	0.5999	0.2280
313.15	4.0036	0.5000	0.1980
313.15	4.0036	0.4003	0.1630
313.15	4.0036	0.3003	0.1250
313.15	4.0036	0.1999	0.0840
313.15	4.0036	0.1006	0.0420

Sources

• Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K