Mixture of Benzene + Butanenitrile

Datasets

1. Excess molar enthalpy (molar enthalpy
2. ρ_l - Mass density, kg/m3
3. γ - Surface tension liquid-gas, N/m

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Butanenitrile (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0922	-0.0154
0.1126	-0.0246
0.1447	-0.0331
0.2024	-0.0457
0.2528	-0.0571
0.2757	-0.0611
0.3367	-0.0658
0.4322	-0.0666
0.5037	-0.0659
0.5751	-0.0562
0.6700	-0.0434
0.7528	-0.0312
0.8024	-0.0229
0.8904	-0.0096
0.9241	-0.0059
0.9384	-0.0048

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butanenitrile (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	878.93
293.15	0.0500	875.009
293.15	0.1000	871.003
293.15	0.1500	866.924
293.15	0.2000	862.779
293.15	0.3000	854.249
293.15	0.4000	845.528
293.15	0.5000	836.701
293.15	0.6000	827.703
293.15	0.7000	818.583
293.15	0.8000	809.399
293.15	0.9000	800.152
293.15	1.0000	790.859
298.15	0.0000	873.621
298.15	0.0500	869.759
298.15	0.1000	865.809
298.15	0.1500	861.784
298.15	0.2000	857.694
298.15	0.3000	849.254
298.15	0.4000	840.62
298.15	0.5000	831.855
298.15	0.6000	822.92
298.15	0.7000	813.854
298.15	0.8000	804.716
298.15	0.9000	795.509
298.15	1.0000	786.254
303.15	0.0000	868.287
303.15	0.0500	864.486
303.15	0.1000	860.593
303.15	0.1500	856.625
303.15	0.2000	852.585
303.15	0.3000	844.236
303.15	0.4000	835.684
303.15	0.5000	826.989
303.15	0.6000	818.113
303.15	0.7000	809.101
303.15	0.8000	800.012
303.15	0.9000	790.845
303.15	1.0000	781.629
308.15	0.0000	862.942
308.15	0.0500	859.199
308.15	0.1000	855.364
308.15	0.1500	851.447
308.15	0.2000	847.456
308.15	0.3000	839.2
308.15	0.4000	830.726
308.15	0.5000	822.102
308.15	0.6000	813.287
308.15	0.7000	804.33
308.15	0.8000	795.287
308.15	0.9000	786.163
308.15	1.0000	776.987
313.15	0.0000	857.576
313.15	0.0500	853.894
313.15	0.1000	850.11
313.15	0.1500	846.246
313.15	0.2000	842.297
313.15	0.3000	834.141
313.15	0.4000	825.744
313.15	0.5000	817.19
313.15	0.6000	808.433
313.15	0.7000	799.532
313.15	0.8000	790.539
313.15	0.9000	781.462
313.15	1.0000	772.321
318.15	0.0000	852.187
318.15	0.0500	848.562
318.15	0.1000	844.834
318.15	0.1500	841.02
318.15	0.2000	837.122
318.15	0.3000	829.052
318.15	0.4000	820.739
318.15	0.5000	812.25
318.15	0.6000	803.56
318.15	0.7000	794.713
318.15	0.8000	785.769
318.15	0.9000	776.736
318.15	1.0000	767.637
323.15	0.0000	846.775
323.15	0.0500	843.206
323.15	0.1000	839.531
323.15	0.1500	835.769
323.15	0.2000	831.921
323.15	0.3000	823.94
323.15	0.4000	815.705
323.15	0.5000	807.289
323.15	0.6000	798.661
323.15	0.7000	789.869
323.15	0.8000	780.977
323.15	0.9000	771.989
323.15	1.0000	762.929

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butanenitrile (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.15	0.0000	0.0292
293.15	0.0500	0.0292
293.15	0.1000	0.0292
293.15	0.1500	0.0292
293.15	0.2000	0.0291
293.15	0.3000	0.0290
293.15	0.4000	0.0289
293.15	0.5000	0.0286
293.15	0.6000	0.0284
293.15	0.7000	0.0281
293.15	0.8000	0.0279
293.15	0.9000	0.0276
293.15	1.0000	0.0273
298.15	0.0000	0.0285
298.15	0.0500	0.0285
298.15	0.1000	0.0285
298.15	0.1500	0.0285
298.15	0.2000	0.0285
298.15	0.3000	0.0284
298.15	0.4000	0.0283
298.15	0.5000	0.0281
298.15	0.6000	0.0278
298.15	0.7000	0.0276
298.15	0.8000	0.0273
298.15	0.9000	0.0271
298.15	1.0000	0.0268
303.15	0.0000	0.0278
303.15	0.0500	0.0279
303.15	0.1000	0.0279
303.15	0.1500	0.0279
303.15	0.2000	0.0279
303.15	0.3000	0.0278
303.15	0.4000	0.0276
303.15	0.5000	0.0274
303.15	0.6000	0.0272
303.15	0.7000	0.0270
303.15	0.8000	0.0267
303.15	0.9000	0.0265
303.15	1.0000	0.0262
308.15	0.0000	0.0271
308.15	0.0500	0.0272
308.15	0.1000	0.0273
308.15	0.1500	0.0273
308.15	0.2000	0.0273
308.15	0.3000	0.0272
308.15	0.4000	0.0270
308.15	0.5000	0.0269
308.15	0.6000	0.0267
308.15	0.7000	0.0265
308.15	0.8000	0.0262
308.15	0.9000	0.0259
308.15	1.0000	0.0256
313.15	0.0000	0.0265
313.15	0.0500	0.0266
313.15	0.1000	0.0267
313.15	0.1500	0.0267
313.15	0.2000	0.0267
313.15	0.3000	0.0266
313.15	0.4000	0.0265
313.15	0.5000	0.0263
313.15	0.6000	0.0262
313.15	0.7000	0.0259
313.15	0.8000	0.0257
313.15	0.9000	0.0254
313.15	1.0000	0.0251

Sources

• Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
• Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions

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