| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3620 | KDB | |
| PAff | 811.50 | kJ/mol | NIST |
| BasG | 780.90 | kJ/mol | NIST |
| ΔcH°liquid | [-3632.30; -3632.30] | kJ/mol |
|
| ΔcH°liquid | -3632.30 ± 1.50 | kJ/mol | NIST |
| ΔcH°liquid | -3632.30 | kJ/mol | NIST |
| Cp,liquid | 166.41 | J/mol×K | Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile) |
| μ | 3.50 | debye | KDB |
| EA | [0.26; 0.26] | eV |
|
| EA | 0.26 ± 0.10 | eV | NIST |
| EA | 0.26 ± 0.02 | eV | NIST |
| Tflash,oc | 348.15 | K | KDB |
| ΔfG° | 261.00 | kJ/mol | KDB |
| ΔfH°gas | [219.00; 219.00] | kJ/mol |
|
| ΔfH°gas | 219.00 | kJ/mol | KDB |
| ΔfH°gas | 219.00 | kJ/mol | NIST |
| ΔfH°gas | 219.00 | kJ/mol | NIST |
| ΔfH°liquid | [163.20; 163.20] | kJ/mol |
|
| ΔfH°liquid | 163.20 ± 1.50 | kJ/mol | NIST |
| ΔfH°liquid | 163.20 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 9.43 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [55.48; 55.80] | kJ/mol |
|
| ΔvapH° | 55.48 | kJ/mol | NIST |
| ΔvapH° | 55.80 | kJ/mol | NIST |
| IE | [9.60; 10.13] | eV |
|
| IE | 9.73 ± 0.01 | eV | NIST |
| IE | 9.73 ± 0.00 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | Outlier 10.13 ± 0.03 | eV | NIST |
| IE | 9.69 | eV | NIST |
| IE | 9.62 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.77 | eV | NIST |
| IE | 9.71 ± 0.01 | eV | NIST |
| IE | 9.79 | eV | NIST |
| IE | 9.80 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.72 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | Outlier 10.02 | eV | NIST |
| log10WS | [-1.00; -1.00] |
|
|
| log10WS | -1.00 | Aq. Solubility Prediction | |
| log10WS | -1.00 | Estimated Solubility | |
| logPoct/wat | 1.558 | Crippen Calculated Property | |
| McVol | 87.110 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | [4210.00; 4220.00] | kPa |
|
| Pc | 4210.00 | kPa | KDB |
| Pc | 4215.00 ± 4.00 | kPa | NIST |
| Pc | 4220.00 ± 101.32 | kPa | NIST |
| Pc | 4215.12 ± 151.99 | kPa | NIST |
| Pc | 4215.12 ± 151.99 | kPa | NIST |
| ρc | 313.18 ± 3.09 | kg/m3 | NIST |
| Inp | [150.10; 1003.00] |
|
|
| Inp | 953.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 937.30 | NIST | |
| Inp | 987.90 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 940.10 | NIST | |
| Inp | 983.40 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 989.90 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | Outlier 150.10 | NIST | |
| Inp | Outlier 150.40 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 987.00 | NIST | |
| I | [1570.00; 1629.00] |
|
|
| I | 1583.00 | NIST | |
| I | Outlier 1629.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1570.00 | NIST | |
| I | 1614.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1583.00 | NIST | |
| S°liquid | [209.10; 209.10] | J/mol×K |
|
| S°liquid | 209.10 | J/mol×K | NIST |
| S°liquid | 209.10 | J/mol×K | NIST |
| S°liquid | 209.10 | J/mol×K | NIST |
| Tboil | [461.90; 464.50] | K |
|
| Tboil | 464.30 | K | KDB |
| Tboil | 462.70 | K | NIST |
| Tboil | 463.90 | K | NIST |
| Tboil | 464.00 | K | NIST |
| Tboil | 463.80 | K | NIST |
| Tboil | 464.15 ± 0.30 | K | NIST |
| Tboil | 463.85 ± 0.60 | K | NIST |
| Tboil | Outlier 461.90 ± 1.00 | K | NIST |
| Tboil | 464.10 ± 0.60 | K | NIST |
| Tboil | 464.00 ± 0.40 | K | NIST |
| Tboil | 464.30 ± 0.70 | K | NIST |
| Tboil | 464.25 ± 0.30 | K | NIST |
| Tboil | 464.50 ± 0.30 | K | NIST |
| Tboil | 464.45 ± 0.30 | K | NIST |
| Tboil | 463.85 ± 0.50 | K | NIST |
| Tc | [699.20; 705.25] | K |
|
| Tc | 699.40 | K | KDB |
| Tc | 699.40 ± 1.00 | K | NIST |
| Tc | 699.20 ± 3.00 | K | NIST |
| Tc | 701.25 ± 2.50 | K | NIST |
| Tc | 699.35 ± 2.50 | K | NIST |
| Tc | 700.45 ± 2.50 | K | NIST |
| Tc | Outlier 705.25 ± 2.50 | K | NIST |
| Tfus | [259.15; 286.15] | K |
|
| Tfus | 260.22 | K | Aq. Solubility Prediction |
| Tfus | 260.40 | K | KDB |
| Tfus | 260.00 | K | NIST |
| Tfus | Outlier 286.15 ± 1.00 | K | NIST |
| Tfus | 259.15 ± 0.00 | K | NIST |
| Tfus | 260.28 ± 0.25 | K | NIST |
| Tfus | 260.40 ± 0.15 | K | NIST |
| Tfus | 259.35 ± 0.50 | K | NIST |
| Tfus | 259.35 ± 0.40 | K | NIST |
| Tfus | 260.05 ± 0.30 | K | NIST |
| Ttriple | [260.33; 260.33] | K |
|
| Ttriple | 260.33 ± 0.02 | K | NIST |
| Ttriple | 260.33 ± 0.02 | K | NIST |
| Ttriple | 260.33 ± 0.02 | K | NIST |
| Vc | 0.316 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 342.00 | K | 1.30 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [341.12; 493.91] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49604e+01 | |||
| Coefficient B | -4.30561e+03 | |||
| Coefficient C | -4.76780e+01 | |||
| Temperature range, min. | 341.12 | |||
| Temperature range, max. | 493.91 | |||
| Pvap | 1.33 | kPa | 341.12 | Calculated Property |
| Pvap | 2.97 | kPa | 358.10 | Calculated Property |
| Pvap | 6.11 | kPa | 375.07 | Calculated Property |
| Pvap | 11.68 | kPa | 392.05 | Calculated Property |
| Pvap | 21.01 | kPa | 409.03 | Calculated Property |
| Pvap | 35.86 | kPa | 426.00 | Calculated Property |
| Pvap | 58.46 | kPa | 442.98 | Calculated Property |
| Pvap | 91.55 | kPa | 459.96 | Calculated Property |
| Pvap | 138.37 | kPa | 476.93 | Calculated Property |
| Pvap | 202.66 | kPa | 493.91 | Calculated Property |
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