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

Datasets

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

Molar enthalpy of mixing with solvent, kJ/mol of Heptane (3) [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 (2) - Liquid	Mole fraction of Heptane (3) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of Heptane (3) - Liquid
298.15	0.2502	0.9003	0.4250
298.15	0.2502	0.8007	0.5170
298.15	0.2502	0.6996	0.5550
298.15	0.2502	0.6004	0.5540
298.15	0.2502	0.3002	0.3890
298.15	0.2502	0.2004	0.2860
298.15	0.2502	0.1503	0.2250
298.15	0.2502	0.0998	0.1570
298.15	0.2502	0.5005	0.5240
298.15	0.2502	0.4000	0.4680
298.15	0.2502	0.0499	0.0820
298.15	0.6667	0.8995	0.3650
298.15	0.6667	0.7999	0.4350
298.15	0.6667	0.7005	0.4610
298.15	0.6667	0.6004	0.4600
298.15	0.6667	0.5001	0.4360
298.15	0.6667	0.4001	0.3890
298.15	0.6667	0.3006	0.3240
298.15	0.6667	0.2003	0.2380
298.15	0.6667	0.1501	0.1870
298.15	0.6667	0.1005	0.1310
298.15	0.6667	0.0499	0.0680
298.15	1.5304	0.9501	0.2330
298.15	1.5304	0.8996	0.2980
298.15	1.5304	0.8496	0.3320
298.15	1.5304	0.8001	0.3530
298.15	1.5304	0.6996	0.3730
298.15	1.5304	0.6001	0.3710
298.15	1.5304	0.4998	0.3500
298.15	1.5304	0.3996	0.3130
298.15	1.5304	0.2997	0.2590
298.15	1.5304	0.2001	0.1900
298.15	1.5304	0.0999	0.1030
298.15	4.0	0.9503	0.1560
298.15	4.0	0.9004	0.2170
298.15	4.0	0.8504	0.2500
298.15	4.0	0.8002	0.2710
298.15	4.0	0.7005	0.2910
298.15	4.0	0.6003	0.2920
298.15	4.0	0.5006	0.2760
298.15	4.0	0.4003	0.2470
298.15	4.0	0.3006	0.2050
298.15	4.0	0.2003	0.1490
298.15	4.0	0.1004	0.0820
313.15	0.2501	0.9508	0.4460
313.15	0.2501	0.9004	0.5760
313.15	0.2501	0.8503	0.6480
313.15	0.2501	0.8008	0.6940
313.15	0.2501	0.5016	0.6830
313.15	0.2501	0.4011	0.6050
313.15	0.2501	0.3011	0.4990
313.15	0.2501	0.2012	0.3640
313.15	0.2501	0.7010	0.7350
313.15	0.2501	0.6016	0.7270
313.15	0.2501	0.1006	0.1980
313.15	0.6674	0.9498	0.3770
313.15	0.6674	0.8994	0.4900
313.15	0.6674	0.8503	0.5440
313.15	0.6674	0.7999	0.5790
313.15	0.6674	0.7005	0.6040
313.15	0.6674	0.6003	0.5940
313.15	0.6674	0.5000	0.5560
313.15	0.6674	0.4001	0.4920
313.15	0.6674	0.3006	0.4050
313.15	0.6674	0.2002	0.2940
313.15	0.6674	0.1005	0.1590
313.15	1.4997	0.9501	0.2880
313.15	1.4997	0.8996	0.3920
313.15	1.4997	0.8495	0.4390
313.15	1.4997	0.8001	0.4660
313.15	1.4997	0.6995	0.4850
313.15	1.4997	0.6000	0.4750
313.15	1.4997	0.4997	0.4420
313.15	1.4997	0.3995	0.3890
313.15	1.4997	0.2996	0.3190
313.15	1.4997	0.2000	0.2310
313.15	1.4997	0.0998	0.1240
313.15	4.0032	0.9503	0.1650
313.15	4.0032	0.9004	0.2540
313.15	4.0032	0.8503	0.3020
313.15	4.0032	0.8001	0.3300
313.15	4.0032	0.7004	0.3520
313.15	4.0032	0.6001	0.3480
313.15	4.0032	0.5004	0.3270
313.15	4.0032	0.4002	0.2890
313.15	4.0032	0.3004	0.2370
313.15	4.0032	0.2002	0.1710
313.15	4.0032	0.1004	0.0910

Molar enthalpy of mixing with solvent, kJ/mol of Heptane (3) [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 (2) - Liquid	Mole fraction of Heptane (3) - Liquid	Molar enthalpy of mixing with solvent, kJ/mol of Heptane (3) - Liquid
298.15	0.2502	0.9003	0.4250
298.15	0.2502	0.8007	0.5170
298.15	0.2502	0.6996	0.5550
298.15	0.2502	0.6004	0.5540
298.15	0.2502	0.3002	0.3890
298.15	0.2502	0.2004	0.2860
298.15	0.2502	0.1503	0.2250
298.15	0.2502	0.0998	0.1570
298.15	0.2502	0.5005	0.5240
298.15	0.2502	0.4000	0.4680
298.15	0.2502	0.0499	0.0820
298.15	0.6667	0.8995	0.3650
298.15	0.6667	0.7999	0.4350
298.15	0.6667	0.7005	0.4610
298.15	0.6667	0.6004	0.4600
298.15	0.6667	0.5001	0.4360
298.15	0.6667	0.4001	0.3890
298.15	0.6667	0.3006	0.3240
298.15	0.6667	0.2003	0.2380
298.15	0.6667	0.1501	0.1870
298.15	0.6667	0.1005	0.1310
298.15	0.6667	0.0499	0.0680
298.15	1.5304	0.9501	0.2330
298.15	1.5304	0.8996	0.2980
298.15	1.5304	0.8496	0.3320
298.15	1.5304	0.8001	0.3530
298.15	1.5304	0.6996	0.3730
298.15	1.5304	0.6001	0.3710
298.15	1.5304	0.4998	0.3500
298.15	1.5304	0.3996	0.3130
298.15	1.5304	0.2997	0.2590
298.15	1.5304	0.2001	0.1900
298.15	1.5304	0.0999	0.1030
298.15	4.0	0.9503	0.1560
298.15	4.0	0.9004	0.2170
298.15	4.0	0.8504	0.2500
298.15	4.0	0.8002	0.2710
298.15	4.0	0.7005	0.2910
298.15	4.0	0.6003	0.2920
298.15	4.0	0.5006	0.2760
298.15	4.0	0.4003	0.2470
298.15	4.0	0.3006	0.2050
298.15	4.0	0.2003	0.1490
298.15	4.0	0.1004	0.0820
313.15	0.2501	0.9508	0.4460
313.15	0.2501	0.9004	0.5760
313.15	0.2501	0.8503	0.6480
313.15	0.2501	0.8008	0.6940
313.15	0.2501	0.5016	0.6830
313.15	0.2501	0.4011	0.6050
313.15	0.2501	0.3011	0.4990
313.15	0.2501	0.2012	0.3640
313.15	0.2501	0.7010	0.7350
313.15	0.2501	0.6016	0.7270
313.15	0.2501	0.1006	0.1980
313.15	0.6674	0.9498	0.3770
313.15	0.6674	0.8994	0.4900
313.15	0.6674	0.8503	0.5440
313.15	0.6674	0.7999	0.5790
313.15	0.6674	0.7005	0.6040
313.15	0.6674	0.6003	0.5940
313.15	0.6674	0.5000	0.5560
313.15	0.6674	0.4001	0.4920
313.15	0.6674	0.3006	0.4050
313.15	0.6674	0.2002	0.2940
313.15	0.6674	0.1005	0.1590
313.15	1.4997	0.9501	0.2880
313.15	1.4997	0.8996	0.3920
313.15	1.4997	0.8495	0.4390
313.15	1.4997	0.8001	0.4660
313.15	1.4997	0.6995	0.4850
313.15	1.4997	0.6000	0.4750
313.15	1.4997	0.4997	0.4420
313.15	1.4997	0.3995	0.3890
313.15	1.4997	0.2996	0.3190
313.15	1.4997	0.2000	0.2310
313.15	1.4997	0.0998	0.1240
313.15	4.0032	0.9503	0.1650
313.15	4.0032	0.9004	0.2540
313.15	4.0032	0.8503	0.3020
313.15	4.0032	0.8001	0.3300
313.15	4.0032	0.7004	0.3520
313.15	4.0032	0.6001	0.3480
313.15	4.0032	0.5004	0.3270
313.15	4.0032	0.4002	0.2890
313.15	4.0032	0.3004	0.2370
313.15	4.0032	0.2002	0.1710
313.15	4.0032	0.1004	0.0910

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