| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3335 | Relay (1.0) Calculated Property | |
| PAff | 808.20 | kJ/mol | NIST |
| BasG | 777.50 | kJ/mol | NIST |
| ΔcH°liquid | [-2433.00; -2429.40] | kJ/mol |
|
| ΔcH°liquid | -2429.40 ± 0.71 | kJ/mol | NIST |
| ΔcH°liquid | -2433.00 | kJ/mol | NIST |
| ΔfG° | 176.73 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [180.60; 182.70] | kJ/mol |
|
| ΔfH°gas | 182.70 ± 0.70 | kJ/mol | NIST |
| ΔfH°gas | 180.60 | kJ/mol | NIST |
| ΔfH°liquid | 140.80 | kJ/mol | NIST |
| ΔfusH° | 5.76 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [39.80; 41.97] | kJ/mol |
|
| ΔvapH° | 41.97 | kJ/mol | NIST |
| ΔvapH° | 41.94 ± 0.11 | kJ/mol | NIST |
| ΔvapH° | 41.90 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 39.80 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 39.80 | kJ/mol | NIST |
| ΔvapH° | 39.80 | kJ/mol | NIST |
| IE | [10.25; 11.20] | eV |
|
| IE | 10.25 | eV | NIST |
| IE | 11.20 ± 0.20 | eV | NIST |
| log10WS | -0.96 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.920 | Crippen Calculated Property | |
| McVol | 57.740 | ml/mol | McGowan Calculated Property |
| Pc | 4462.28 | kPa | Joback Calculated Property |
| Inp | [644.00; 684.00] |
|
|
| Inp | 684.00 | NIST | |
| Inp | 645.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 684.00 | NIST | |
| Tboil | [404.90; 408.20] | K |
|
| Tboil | 408.20 | K | NIST |
| Tboil | 407.50 ± 0.50 | K | NIST |
| Tboil | 408.20 | K | NIST |
| Tboil | 404.90 ± 3.00 | K | NIST |
| Tc | 584.81 | K | Relay (1.0) Calculated Property |
| Tfus | 272.25 | K | Relay (1.0) Calculated Property |
| Vc | 0.220 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [100.75; 139.13] | J/mol×K | [399.74; 609.13] | |
| Cp,gas | 100.75 | J/mol×K | 399.74 | Joback Calculated Property |
| Cp,gas | 108.34 | J/mol×K | 434.64 | Joback Calculated Property |
| Cp,gas | 115.41 | J/mol×K | 469.54 | Joback Calculated Property |
| Cp,gas | 122.00 | J/mol×K | 504.44 | Joback Calculated Property |
| Cp,gas | 128.12 | J/mol×K | 539.33 | Joback Calculated Property |
| Cp,gas | 133.82 | J/mol×K | 574.23 | Joback Calculated Property |
| Cp,gas | 139.13 | J/mol×K | 609.13 | Joback Calculated Property |
| Cp,liquid | 115.40 | J/mol×K | 297.00 | NIST |
| ΔvapH | [35.55; 39.40] | kJ/mol | [350.50; 408.20] | |
| ΔvapH | 39.40 | kJ/mol | 350.50 | NIST |
| ΔvapH | 35.55 | kJ/mol | 408.20 | NIST |
| Pvap | [35.20; 102.20] | kPa | [373.10; 408.15] | |
| Pvap | 35.20 | kPa | 373.10 | Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water |
| Pvap | 102.20 | kPa | 408.15 | Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water |
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