| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3025 | Relay (1.0) Calculated Property | |
| ΔfG° | 108.54 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 19.00 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | -33.00 ± 3.00 | kJ/mol | NIST |
| ΔfusH° | 12.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [49.90; 51.00] | kJ/mol |
|
| ΔvapH° | 50.10 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 49.90 | kJ/mol | NIST |
| ΔvapH° | 50.10 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 51.00 ± 2.00 | kJ/mol | NIST |
| IE | [9.10; 9.30] | eV |
|
| IE | 9.10 ± 0.02 | eV | NIST |
| IE | 9.14 ± 0.01 | eV | NIST |
| IE | 9.14 ± 0.01 | eV | NIST |
| IE | 9.10 ± 0.05 | eV | NIST |
| IE | 9.30 | eV | NIST |
| IE | 9.29 | eV | NIST |
| IE | 9.30 | eV | NIST |
| log10WS | [-2.39; -2.39] |
|
|
| log10WS | -2.39 | Aq. Solubility Prediction | |
| log10WS | -2.39 | Estimated Solubility | |
| logPoct/wat | 2.425 | Crippen Calculated Property | |
| McVol | 97.970 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | 3925.85 | kPa | Joback Calculated Property |
| Inp | [977.90; 1023.00] |
|
|
| Inp | 1015.00 | NIST | |
| Inp | 977.90 | NIST | |
| Inp | Outlier 1023.00 | NIST | |
| Inp | 985.60 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 983.00 | NIST | |
| I | [1478.00; 1497.00] |
|
|
| I | 1478.00 | NIST | |
| I | 1497.00 | NIST | |
| I | 1478.00 | NIST | |
| Tboil | 452.15 | K | KDB |
| Tc | 676.66 | K | Relay (1.0) Calculated Property |
| Tfus | [225.30; 233.95] | K |
|
| Tfus | 233.95 | K | KDB |
| Tfus | 229.48 | K | Aq. Solubility Prediction |
| Tfus | 233.95 ± 0.30 | K | NIST |
| Tfus | 233.45 ± 0.40 | K | NIST |
| Tfus | 225.30 ± 0.50 | K | NIST |
| Vc | 0.350 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [163.08; 218.66] | J/mol×K | [423.67; 643.33] | |
| Cp,gas | 163.08 | J/mol×K | 423.67 | Joback Calculated Property |
| Cp,gas | 173.99 | J/mol×K | 460.28 | Joback Calculated Property |
| Cp,gas | 184.20 | J/mol×K | 496.89 | Joback Calculated Property |
| Cp,gas | 193.74 | J/mol×K | 533.50 | Joback Calculated Property |
| Cp,gas | 202.64 | J/mol×K | 570.11 | Joback Calculated Property |
| Cp,gas | 210.94 | J/mol×K | 606.72 | Joback Calculated Property |
| Cp,gas | 218.66 | J/mol×K | 643.33 | Joback Calculated Property |
| Cp,liquid | 182.40 | J/mol×K | 298.50 | NIST |
| η | [0.0002746; 0.0031741] | Pa×s | [224.99; 423.67] | |
| η | 0.0031741 | Pa×s | 224.99 | Joback Calculated Property |
| η | 0.0016248 | Pa×s | 258.10 | Joback Calculated Property |
| η | 0.0009686 | Pa×s | 291.22 | Joback Calculated Property |
| η | 0.0006417 | Pa×s | 324.33 | Joback Calculated Property |
| η | 0.0004588 | Pa×s | 357.44 | Joback Calculated Property |
| η | 0.0003473 | Pa×s | 390.56 | Joback Calculated Property |
| η | 0.0002746 | Pa×s | 423.67 | Joback Calculated Property |
| ΔfusH | 8.74 | kJ/mol | 230.00 | NIST |
| ΔvapH | [48.60; 48.60] | kJ/mol | [355.00; 374.00] | |
| ΔvapH | 48.60 | kJ/mol | 355.00 | NIST |
| ΔvapH | 48.60 | kJ/mol | 374.00 | NIST |
| ρl | 1094.82 | kg/m3 | 298.15 | Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [332.04; 482.07] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41881e+01 | |||
| Coefficient B | -3.68477e+03 | |||
| Coefficient C | -6.69590e+01 | |||
| Temperature range, min. | 332.04 | |||
| Temperature range, max. | 482.07 | |||
| Pvap | 1.33 | kPa | 332.04 | Calculated Property |
| Pvap | 3.03 | kPa | 348.71 | Calculated Property |
| Pvap | 6.30 | kPa | 365.38 | Calculated Property |
| Pvap | 12.11 | kPa | 382.05 | Calculated Property |
| Pvap | 21.79 | kPa | 398.72 | Calculated Property |
| Pvap | 37.07 | kPa | 415.39 | Calculated Property |
| Pvap | 60.08 | kPa | 432.06 | Calculated Property |
| Pvap | 93.35 | kPa | 448.73 | Calculated Property |
| Pvap | 139.79 | kPa | 465.40 | Calculated Property |
| Pvap | 202.66 | kPa | 482.07 | Calculated Property |
| Pvap | [7.17e-04; 3776.09] | kPa | [234.15; 686.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.79326e+01 | |||
| Coefficient B | -7.14622e+03 | |||
| Coefficient C | -4.52442e+00 | |||
| Coefficient D | 5.72779e-07 | |||
| Temperature range, min. | 234.15 | |||
| Temperature range, max. | 686.00 | |||
| Pvap | 7.17e-04 | kPa | 234.15 | Calculated Property |
| Pvap | 0.07 | kPa | 284.36 | Calculated Property |
| Pvap | 1.40 | kPa | 334.56 | Calculated Property |
| Pvap | 12.33 | kPa | 384.77 | Calculated Property |
| Pvap | 61.85 | kPa | 434.97 | Calculated Property |
| Pvap | 212.08 | kPa | 485.18 | Calculated Property |
| Pvap | 556.70 | kPa | 535.38 | Calculated Property |
| Pvap | 1203.63 | kPa | 585.59 | Calculated Property |
| Pvap | 2252.29 | kPa | 635.79 | Calculated Property |
| Pvap | 3776.09 | kPa | 686.00 | Calculated Property |
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