Mixture of Toluene + 2-Pentanol

Datasets

1. Mole fraction
2. Excess molar enthalpy (molar enthalpy
3. Vapor or sublimation pressure, kPa

Mole fraction of 2-Pentanol (2) [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (2) - Liquid	Mole fraction of 2-Pentanol (2) - Gas
0.0000	0.0000
0.0498	0.0592
0.0995	0.0912
0.1495	0.1122
0.1996	0.1281
0.2499	0.1416
0.2998	0.1540
0.3497	0.1660
0.3997	0.1782
0.4004	0.1784
0.4498	0.1911
0.4504	0.1913
0.4999	0.2051
0.5004	0.2053
0.5499	0.2207
0.5504	0.2209
0.5999	0.2388
0.6005	0.2390
0.6506	0.2604
0.7006	0.2865
0.7628	0.3287
0.8008	0.3626
0.8507	0.4223
0.9008	0.5125
0.9509	0.6675
1.0000	1.0000

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Pentanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15	0.0000	0.0000
298.15	0.0508	0.6244
298.15	0.0998	0.9472
298.15	0.1510	1.1545
298.15	0.2002	1.2962
298.15	0.2496	1.4021
298.15	0.3009	1.481
298.15	0.3506	1.5357
298.15	0.4003	1.5618
298.15	0.4501	1.5621
298.15	0.5001	1.5437
298.15	0.5501	1.5023
298.15	0.6003	1.4414
298.15	0.6506	1.3394
298.15	0.7010	1.2249
298.15	0.7495	1.0838
298.15	0.8002	0.9217
298.15	0.8509	0.7230
298.15	0.8996	0.5005
298.15	0.9508	0.2499
298.15	1.0000	0.0000
313.15	0.0000	0.0000
313.15	0.0508	0.6440
313.15	0.0999	1.0266
313.15	0.1510	1.2828
313.15	0.2003	1.4458
313.15	0.2496	1.5672
313.15	0.3010	1.6595
313.15	0.3506	1.7089
313.15	0.4003	1.7317
313.15	0.4502	1.7328
313.15	0.5001	1.7032
313.15	0.5502	1.6495
313.15	0.6003	1.5772
313.15	0.6505	1.4754
313.15	0.7010	1.3406
313.15	0.7495	1.1797
313.15	0.8002	0.9991
313.15	0.8510	0.7821
313.15	0.8998	0.5505
313.15	0.9509	0.2765
313.15	1.0000	0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Gas)

Mole fraction of 2-Pentanol (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	7.88
0.0498	8.05
0.0995	8.04
0.1495	8.00
0.1996	7.96
0.2499	7.88
0.2998	7.78
0.3497	7.63
0.3997	7.53
0.4004	7.53
0.4498	7.36
0.4504	7.38
0.4999	7.19
0.5004	7.18
0.5499	6.98
0.5504	6.90
0.5999	6.74
0.6005	6.74
0.6506	6.46
0.7006	6.07
0.7628	5.65
0.8008	5.25
0.8507	4.72
0.9008	4.05
0.9509	3.27
1.0000	2.30

Sources

• Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels

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