- Name
- Benzene
- InChI
- InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
- InChI Key
- UHOVQNZJYSORNB-UHFFFAOYSA-N
- Formula
- C6H6
- SMILES
- c1ccccc1
- Mol. Weight (g/mol)
- 78.11
- CAS
- 71-43-2
- Name
- Butanenitrile
- InChI
- InChI=1S/C4H7N/c1-2-3-4-5/h2-3H2,1H3
- InChI Key
- KVNRLNFWIYMESJ-UHFFFAOYSA-N
- Formula
- C4H7N
- SMILES
- CCCC#N
- Mol. Weight (g/mol)
- 69.11
- CAS
- 109-74-0
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Datasets
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- γ - Surface tension liquid-gas, N/m (2)
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 |
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 |
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 |
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