Mixture of Butane, 1-bromo- + 1-Octanol

Datasets

1. Excess molar enthalpy (molar enthalpy
2. P_vap - Vapor or sublimation pressure, kPa
3. Excess molar volume, m3/mol

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Octanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0250	0.3640
0.0571	0.6020
0.1224	0.8400
0.1949	0.9760
0.2361	1.021
0.2760	1.048
0.3205	1.057
0.3670	1.056
0.4661	1.005
0.5784	0.8890
0.7064	0.6920
0.8484	0.4000
0.9311	0.2040

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Octanol (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
278.15	0.1029	1.76
278.15	0.1957	1.73
278.15	0.2650	1.69
278.15	0.3503	1.60
278.15	0.4477	1.49
278.15	0.5528	1.34
278.15	0.6397	1.19
278.15	0.7345	0.96
278.15	0.8543	0.60
278.15	0.9136	0.38
283.15	0.1029	2.37
283.15	0.1957	2.30
283.15	0.2650	2.24
283.15	0.3504	2.12
283.15	0.4477	1.98
283.15	0.5529	1.78
283.15	0.6398	1.57
283.15	0.7345	1.27
283.15	0.8543	0.77
283.15	0.9136	0.49
288.15	0.1030	3.10
288.15	0.1958	3.02
288.15	0.2651	2.92
288.15	0.3504	2.78
288.15	0.4478	2.59
288.15	0.5530	2.31
288.15	0.6399	2.04
288.15	0.7346	1.64
288.15	0.8544	1.02
288.15	0.9137	0.64
293.15	0.1030	4.03
293.15	0.1958	3.92
293.15	0.2651	3.79
293.15	0.3505	3.59
293.15	0.4479	3.35
293.15	0.5531	2.98
293.15	0.6400	2.62
293.15	0.7347	2.10
293.15	0.8544	1.30
293.15	0.9137	0.81
298.15	0.1030	5.17
298.15	0.1959	5.03
298.15	0.2652	4.85
298.15	0.3506	4.60
298.15	0.4481	4.26
298.15	0.5532	3.81
298.15	0.6401	3.34
298.15	0.7349	2.68
298.15	0.8545	1.66
298.15	0.9138	1.03
303.15	0.1031	6.61
303.15	0.1960	6.40
303.15	0.2653	6.18
303.15	0.3508	5.85
303.15	0.4482	5.41
303.15	0.5534	4.81
303.15	0.6403	4.22
303.15	0.7350	3.38
303.15	0.8547	2.09
303.15	0.9138	1.31
308.15	0.1031	8.36
308.15	0.1961	8.06
308.15	0.2654	7.75
308.15	0.3510	7.33
308.15	0.4485	6.77
308.15	0.5537	6.02
308.15	0.6406	5.26
308.15	0.7352	4.23
308.15	0.8548	2.61
308.15	0.9139	1.63
313.15	0.1032	10.44
313.15	0.1962	10.06
313.15	0.2656	9.66
313.15	0.3512	9.12
313.15	0.4488	8.41
313.15	0.5540	7.46
313.15	0.6409	6.50
313.15	0.7355	5.21
313.15	0.8550	3.21
313.15	0.9140	2.03
318.15	0.1033	12.96
318.15	0.1965	12.42
318.15	0.2658	11.95
318.15	0.3516	11.26
318.15	0.4492	10.35
318.15	0.5544	9.16
318.15	0.6413	7.96
318.15	0.7358	6.36
318.15	0.8552	3.91
318.15	0.9141	2.47
323.15	0.1034	15.93
323.15	0.1967	15.25
323.15	0.2661	14.64
323.15	0.3520	13.78
323.15	0.4497	12.63
323.15	0.5550	11.16
323.15	0.6418	9.69
323.15	0.7362	7.70
323.15	0.8555	4.75
323.15	0.9143	3.01

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1-Octanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0702	1.0400e-07
0.1016	1.2700e-07
0.2062	1.6700e-07
0.2980	1.8300e-07
0.3954	1.8700e-07
0.4953	1.8200e-07
0.5976	1.6800e-07
0.6922	1.4200e-07
0.7908	1.1100e-07
0.8530	8.1000e-08
0.8904	5.7000e-08

Sources

• Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol

Note: These property values are available through the Cheméo API. A free account gives you an access key.