| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6540 | Relay (1.0) Calculated Property | |
| PAff | 838.80 | kJ/mol | NIST |
| BasG | 807.80 | kJ/mol | NIST |
| ΔcH°solid | [-3875.00; -3858.00] | kJ/mol |
|
| ΔcH°solid | -3874.90 ± 0.80 | kJ/mol | NIST |
| ΔcH°solid | -3874.40 ± 4.60 | kJ/mol | NIST |
| ΔcH°solid | -3875.00 ± 0.75 | kJ/mol | NIST |
| ΔcH°solid | -3864.00 | kJ/mol | NIST |
| ΔcH°solid | -3858.00 | kJ/mol | NIST |
| ΔfG° | -146.48 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-331.20; -320.60] | kJ/mol |
|
| ΔfH°gas | -320.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | -320.60 | kJ/mol | NIST |
| ΔfH°gas | -331.20 | kJ/mol | NIST |
| ΔfH°solid | [-427.10; -416.50] | kJ/mol |
|
| ΔfH°solid | -416.50 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | -416.50 ± 0.92 | kJ/mol | NIST |
| ΔfH°solid | -427.10 ± 3.80 | kJ/mol | NIST |
| ΔfusH° | 15.81 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [95.90; 95.90] | kJ/mol |
|
| ΔsubH° | 95.90 ± 0.10 | kJ/mol | NIST |
| ΔsubH° | 95.90 ± 0.10 | kJ/mol | NIST |
| ΔsubH° | 95.90 | kJ/mol | NIST |
| ΔvapH° | 80.79 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [9.10; 9.40] | eV |
|
| IE | 9.10 | eV | NIST |
| IE | 9.40 | eV | NIST |
| log10WS | -2.06 | Aq. Solubility Prediction | |
| logPoct/wat | 1.693 | Crippen Calculated Property | |
| McVol | 107.260 | ml/mol | McGowan Calculated Property |
| Pc | 4356.87 | kPa | Joback Calculated Property |
| Tboil | 531.70 | K | NIST |
| Tc | 763.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tfus | [376.50; 380.00] | K |
|
| Tfus | 377.63 | K | Aq. Solubility Prediction |
| Tfus | 380.00 ± 1.50 | K | NIST |
| Tfus | 376.50 ± 0.05 | K | NIST |
| Tfus | 377.65 ± 2.00 | K | NIST |
| Tfus | 376.90 ± 0.30 | K | NIST |
| Vc | 0.377 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.24; 202.63] | kPa | [376.85; 561.58] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54533e+01 | |||
| Coefficient B | -4.69014e+03 | |||
| Coefficient C | -9.91310e+01 | |||
| Temperature range, min. | 376.85 | |||
| Temperature range, max. | 561.58 | |||
| Pvap | 0.24 | kPa | 376.85 | Calculated Property |
| Pvap | 0.76 | kPa | 397.38 | Calculated Property |
| Pvap | 2.10 | kPa | 417.90 | Calculated Property |
| Pvap | 5.10 | kPa | 438.43 | Calculated Property |
| Pvap | 11.23 | kPa | 458.95 | Calculated Property |
| Pvap | 22.69 | kPa | 479.48 | Calculated Property |
| Pvap | 42.67 | kPa | 500.00 | Calculated Property |
| Pvap | 75.44 | kPa | 520.53 | Calculated Property |
| Pvap | 126.51 | kPa | 541.05 | Calculated Property |
| Pvap | 202.63 | kPa | 561.58 | Calculated Property |
| Pvap | [0.24; 3834.56] | kPa | [376.85; 751.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.31614e+02 | |||
| Coefficient B | -1.40488e+04 | |||
| Coefficient C | -1.62792e+01 | |||
| Coefficient D | 5.55990e-06 | |||
| Temperature range, min. | 376.85 | |||
| Temperature range, max. | 751.00 | |||
| Pvap | 0.24 | kPa | 376.85 | Calculated Property |
| Pvap | 2.10 | kPa | 418.42 | Calculated Property |
| Pvap | 11.45 | kPa | 459.99 | Calculated Property |
| Pvap | 43.95 | kPa | 501.57 | Calculated Property |
| Pvap | 130.60 | kPa | 543.14 | Calculated Property |
| Pvap | 320.94 | kPa | 584.71 | Calculated Property |
| Pvap | 683.97 | kPa | 626.28 | Calculated Property |
| Pvap | 1309.13 | kPa | 667.86 | Calculated Property |
| Pvap | 2310.21 | kPa | 709.43 | Calculated Property |
| Pvap | 3834.56 | kPa | 751.00 | Calculated Property |
Find more compounds similar to Benzoic acid, 2-methyl-.
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