| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 800.30 | kJ/mol | NIST |
| BasG | 769.50 | kJ/mol | NIST |
| ΔcH°liquid | [-3096.00; -3073.80] | kJ/mol |
|
| ΔcH°liquid | -3088.08 ± 0.42 | kJ/mol | NIST |
| ΔcH°liquid | -3096.00 | kJ/mol | NIST |
| ΔcH°liquid | -3073.80 | kJ/mol | NIST |
| η | 0.0016860 | Pa×s | Ion Pair and Triple Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of Carbon Tetrachloride + Nitrobenzene |
| EA | [0.40; 1.18] | eV |
|
| EA | 1.00 ± 0.01 | eV | NIST |
| EA | 1.01 ± 0.10 | eV | NIST |
| EA | 1.00 ± 0.06 | eV | NIST |
| EA | 1.00 ± 0.02 | eV | NIST |
| EA | 1.02 ± 0.05 | eV | NIST |
| EA | 1.18 ± 0.05 | eV | NIST |
| EA | 1.10 | eV | NIST |
| EA | 0.70 ± 0.20 | eV | NIST |
| EA | Outlier 0.40 | eV | NIST |
| ΔfH°gas | 68.53 ± 0.67 | kJ/mol | NIST |
| ΔfH°liquid | [-16.00; 12.50] | kJ/mol |
|
| ΔfH°liquid | 12.50 ± 0.54 | kJ/mol | NIST |
| ΔfH°liquid | -16.00 | kJ/mol | NIST |
| ΔfusH° | 16.70 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [54.50; 56.10] | kJ/mol |
|
| ΔvapH° | 54.50 | kJ/mol | NIST |
| ΔvapH° | 55.01 ± 0.02 | kJ/mol | NIST |
| ΔvapH° | 55.00 | kJ/mol | NIST |
| ΔvapH° | 56.10 ± 1.70 | kJ/mol | NIST |
| ΔvapH° | 56.10 ± 1.70 | kJ/mol | NIST |
| IE | [9.60; 10.80] | eV |
|
| IE | 9.94 ± 0.08 | eV | NIST |
| IE | 9.67 | eV | NIST |
| IE | 9.80 | eV | NIST |
| IE | 10.16 ± 0.08 | eV | NIST |
| IE | 9.92 | eV | NIST |
| IE | 10.16 ± 0.08 | eV | NIST |
| IE | 9.87 ± 0.05 | eV | NIST |
| IE | 9.93 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | 9.99 | eV | NIST |
| IE | 9.99 ± 0.01 | eV | NIST |
| IE | 9.85 ± 0.03 | eV | NIST |
| IE | 9.94 ± 0.03 | eV | NIST |
| IE | 9.90 | eV | NIST |
| IE | 9.86 ± 0.05 | eV | NIST |
| IE | 9.90 ± 0.03 | eV | NIST |
| IE | 10.16 ± 0.04 | eV | NIST |
| IE | 9.70 ± 0.10 | eV | NIST |
| IE | 9.92 | eV | NIST |
| IE | 9.86 | eV | NIST |
| IE | 9.90 | eV | NIST |
| IE | 9.92 | eV | NIST |
| IE | 9.93 | eV | NIST |
| IE | Outlier 10.80 | eV | NIST |
| IE | 9.93 | eV | NIST |
| IE | 10.10 ± 0.10 | eV | NIST |
| IE | 9.88 ± 0.01 | eV | NIST |
| IE | 10.26 | eV | NIST |
| log10WS | [-1.81; -1.80] |
|
|
| log10WS | -1.81 | Aq. Solubility Prediction | |
| log10WS | -1.80 | Estimated Solubility | |
| logPoct/wat | 1.595 | Crippen Calculated Property | |
| McVol | 89.060 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 3 | KDB | |
| NFPA Safety | 2 | KDB | |
| Inp | [180.05; 1114.00] |
|
|
| Inp | 1049.40 | NIST | |
| Inp | 1058.30 | NIST | |
| Inp | 1066.70 | NIST | |
| Inp | 1049.20 | NIST | |
| Inp | 1057.40 | NIST | |
| Inp | 1068.50 | NIST | |
| Inp | 1048.20 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1088.80 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | Outlier 180.05 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1088.80 | NIST | |
| Inp | 1049.40 | NIST | |
| Inp | 1068.50 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1100.00 | NIST | |
| I | [1683.00; 1683.00] |
|
|
| I | 1683.00 | NIST | |
| I | 1683.00 | NIST | |
| I | 1683.00 | NIST | |
| S°liquid | 224.30 | J/mol×K | NIST |
| Tboil | [478.15; 485.09] | K |
|
| Tboil | 483.90 | K | KDB |
| Tboil | 483.80 ± 0.40 | K | NIST |
| Tboil | 484.00 ± 1.00 | K | NIST |
| Tboil | 484.20 ± 0.50 | K | NIST |
| Tboil | 483.70 ± 0.50 | K | NIST |
| Tboil | 484.00 | K | NIST |
| Tboil | 483.70 ± 0.50 | K | NIST |
| Tboil | 483.55 ± 0.40 | K | NIST |
| Tboil | 483.71 ± 0.40 | K | NIST |
| Tboil | 483.95 ± 0.70 | K | NIST |
| Tboil | 481.10 ± 1.00 | K | NIST |
| Tboil | 483.95 ± 0.50 | K | NIST |
| Tboil | 485.09 ± 0.25 | K | NIST |
| Tboil | 482.15 ± 1.00 | K | NIST |
| Tboil | 483.90 ± 0.50 | K | NIST |
| Tboil | 483.90 ± 0.30 | K | NIST |
| Tboil | 483.95 ± 0.30 | K | NIST |
| Tboil | 483.90 ± 0.30 | K | NIST |
| Tboil | 483.90 ± 0.50 | K | NIST |
| Tboil | 482.65 ± 0.50 | K | NIST |
| Tboil | 484.00 ± 0.40 | K | NIST |
| Tboil | 482.15 ± 2.00 | K | NIST |
| Tboil | 482.00 ± 2.00 | K | NIST |
| Tboil | 484.00 ± 0.35 | K | NIST |
| Tboil | 483.95 ± 1.00 | K | NIST |
| Tboil | Outlier 478.15 ± 1.50 | K | NIST |
| Tfus | [278.80; 279.15] | K |
|
| Tfus | 278.81 | K | KDB |
| Tfus | 278.82 | K | Aq. Solubility Prediction |
| Tfus | 278.90 ± 0.20 | K | NIST |
| Tfus | Outlier 279.15 ± 1.00 | K | NIST |
| Tfus | 278.90 ± 0.20 | K | NIST |
| Tfus | 278.87 ± 0.15 | K | NIST |
| Tfus | 278.89 ± 0.10 | K | NIST |
| Tfus | Outlier 279.15 ± 0.50 | K | NIST |
| Tfus | 278.85 ± 0.50 | K | NIST |
| Tfus | 278.84 ± 0.07 | K | NIST |
| Tfus | 278.80 ± 0.08 | K | NIST |
| Tfus | 278.80 ± 0.08 | K | NIST |
| Tfus | 278.85 ± 0.20 | K | NIST |
| Tfus | 279.00 ± 1.50 | K | NIST |
| Tfus | 278.90 ± 0.30 | K | NIST |
| Tfus | 279.00 ± 1.50 | K | NIST |
| Tfus | 278.85 ± 0.20 | K | NIST |
| Tfus | 278.90 ± 0.30 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Isobaric coefficient of expansion, 1/K - Liquid |
| 288.15 | 5000.00 | 0.0008 |
| 288.15 | 10000.00 | 0.0008 |
| 288.15 | 15000.00 | 0.0008 |
| 288.15 | 20000.00 | 0.0008 |
| 288.15 | 25000.00 | 0.0008 |
| 288.15 | 30000.00 | 0.0008 |
| 288.15 | 35000.00 | 0.0007 |
| 288.15 | 40000.00 | 0.0007 |
| 288.15 | 45000.00 | 0.0007 |
| 288.15 | 50000.00 | 0.0007 |
| 288.15 | 55000.00 | 0.0007 |
| 298.15 | 5000.00 | 0.0008 |
| 298.15 | 10000.00 | 0.0008 |
| 298.15 | 15000.00 | 0.0008 |
| 298.15 | 20000.00 | 0.0008 |
| 298.15 | 25000.00 | 0.0008 |
| 298.15 | 30000.00 | 0.0008 |
| 298.15 | 35000.00 | 0.0008 |
| 298.15 | 40000.00 | 0.0007 |
| 298.15 | 45000.00 | 0.0007 |
| 298.15 | 50000.00 | 0.0007 |
| 298.15 | 55000.00 | 0.0007 |
| 308.15 | 5000.00 | 0.0008 |
| 308.15 | 10000.00 | 0.0008 |
| 308.15 | 15000.00 | 0.0008 |
| 308.15 | 20000.00 | 0.0008 |
| 308.15 | 25000.00 | 0.0008 |
| 308.15 | 30000.00 | 0.0008 |
| 308.15 | 35000.00 | 0.0008 |
| 308.15 | 40000.00 | 0.0007 |
| 308.15 | 45000.00 | 0.0007 |
| 308.15 | 50000.00 | 0.0007 |
| 308.15 | 55000.00 | 0.0007 |
| 318.15 | 5000.00 | 0.0008 |
| 318.15 | 10000.00 | 0.0008 |
| 318.15 | 15000.00 | 0.0008 |
| 318.15 | 20000.00 | 0.0008 |
| 318.15 | 25000.00 | 0.0008 |
| 318.15 | 30000.00 | 0.0008 |
| 318.15 | 35000.00 | 0.0007 |
| 318.15 | 40000.00 | 0.0007 |
| 318.15 | 45000.00 | 0.0007 |
| 318.15 | 50000.00 | 0.0007 |
| 318.15 | 55000.00 | 0.0007 |
| 328.15 | 5000.00 | 0.0008 |
| 328.15 | 10000.00 | 0.0008 |
| 328.15 | 15000.00 | 0.0008 |
| 328.15 | 20000.00 | 0.0008 |
| 328.15 | 25000.00 | 0.0008 |
| 328.15 | 30000.00 | 0.0008 |
| 328.15 | 35000.00 | 0.0008 |
| 328.15 | 40000.00 | 0.0007 |
| 328.15 | 45000.00 | 0.0007 |
| 328.15 | 50000.00 | 0.0007 |
| 328.15 | 55000.00 | 0.0007 |
| 338.15 | 5000.00 | 0.0008 |
| 338.15 | 10000.00 | 0.0008 |
| 338.15 | 15000.00 | 0.0008 |
| 338.15 | 20000.00 | 0.0008 |
| 338.15 | 25000.00 | 0.0008 |
| 338.15 | 30000.00 | 0.0008 |
| 338.15 | 35000.00 | 0.0008 |
| 338.15 | 40000.00 | 0.0007 |
| 338.15 | 45000.00 | 0.0007 |
| 338.15 | 50000.00 | 0.0007 |
| 338.15 | 55000.00 | 0.0007 |
| 348.15 | 5000.00 | 0.0009 |
| 348.15 | 10000.00 | 0.0008 |
| 348.15 | 15000.00 | 0.0008 |
| 348.15 | 20000.00 | 0.0008 |
| 348.15 | 25000.00 | 0.0008 |
| 348.15 | 30000.00 | 0.0008 |
| 348.15 | 35000.00 | 0.0008 |
| 348.15 | 40000.00 | 0.0007 |
| 348.15 | 45000.00 | 0.0007 |
| 348.15 | 50000.00 | 0.0007 |
| 348.15 | 55000.00 | 0.0007 |
| Reference | ||
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Frequency, MHz - Liquid | Speed of sound, m/s - Liquid |
| 303.15 | 100.00 | 2.0 | 1445.6 |
| Reference | |||
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [359.28; 513.96] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53379e+01 | |||
| Coefficient B | -4.64614e+03 | |||
| Coefficient C | -5.05750e+01 | |||
| Temperature range, min. | 359.28 | |||
| Temperature range, max. | 513.96 | |||
| Pvap | 1.33 | kPa | 359.28 | Calculated Property |
| Pvap | 2.95 | kPa | 376.47 | Calculated Property |
| Pvap | 6.02 | kPa | 393.65 | Calculated Property |
| Pvap | 11.49 | kPa | 410.84 | Calculated Property |
| Pvap | 20.67 | kPa | 428.03 | Calculated Property |
| Pvap | 35.33 | kPa | 445.21 | Calculated Property |
| Pvap | 57.75 | kPa | 462.40 | Calculated Property |
| Pvap | 90.75 | kPa | 479.59 | Calculated Property |
| Pvap | 137.72 | kPa | 496.77 | Calculated Property |
| Pvap | 202.63 | kPa | 513.96 | Calculated Property |
| Pvap | [6.43e-03; 4167.87] | kPa | [278.91; 719.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.29288e+02 | |||
| Coefficient B | -1.14658e+04 | |||
| Coefficient C | -1.66824e+01 | |||
| Coefficient D | 9.14721e-06 | |||
| Temperature range, min. | 278.91 | |||
| Temperature range, max. | 719.00 | |||
| Pvap | 6.43e-03 | kPa | 278.91 | Calculated Property |
| Pvap | 0.26 | kPa | 327.81 | Calculated Property |
| Pvap | 3.31 | kPa | 376.71 | Calculated Property |
| Pvap | 20.44 | kPa | 425.61 | Calculated Property |
| Pvap | 80.01 | kPa | 474.51 | Calculated Property |
| Pvap | 232.70 | kPa | 523.40 | Calculated Property |
| Pvap | 556.46 | kPa | 572.30 | Calculated Property |
| Pvap | 1169.96 | kPa | 621.20 | Calculated Property |
| Pvap | 2264.56 | kPa | 670.10 | Calculated Property |
| Pvap | 4167.87 | kPa | 719.00 | Calculated Property |
Find more compounds similar to Benzene, nitro-.
Find more mixtures with Benzene, nitro-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.