| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3118 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ΔcH°liquid | [-5358.91; -5358.80] | kJ/mol |
|
| ΔcH°liquid | -5358.91 ± 0.68 | kJ/mol | NIST |
| ΔcH°liquid | -5358.80 ± 1.60 | kJ/mol | NIST |
| ΔfH°gas | [145.70; 146.73] | kJ/mol |
|
| ΔfH°gas | 146.73 ± 0.89 | kJ/mol | NIST |
| ΔfH°gas | 145.70 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | [102.20; 102.34] | kJ/mol |
|
| ΔfH°liquid | 102.34 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | 102.20 ± 1.70 | kJ/mol | NIST |
| ΔfusH° | 14.78 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [43.50; 44.40] | kJ/mol |
|
| ΔvapH° | 44.39 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 44.40 | kJ/mol | NIST |
| ΔvapH° | 44.30 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | Outlier 43.50 | kJ/mol | NIST |
| ΔvapH° | 44.39 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 44.40 | kJ/mol | NIST |
| IE | 8.46 | eV | Relay (1.0) Calculated Property |
| logPoct/wat | 2.529 | Crippen Calculated Property | |
| McVol | 107.350 | ml/mol | McGowan Calculated Property |
| Pc | [3400.00; 3400.00] | kPa |
|
| Pc | 3400.00 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3400.00 ± 400.00 | kPa | NIST |
| Pc | 3400.00 ± 400.00 | kPa | NIST |
| ρc | [294.47; 294.47] | kg/m3 |
|
| ρc | 294.47 ± 14.42 | kg/m3 | NIST |
| ρc | 294.47 ± 14.42 | kg/m3 | NIST |
| Inp | [891.80; 934.80] |
|
|
| Inp | 915.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 895.40 | NIST | |
| Inp | 891.80 | NIST | |
| Inp | 928.40 | NIST | |
| Inp | 922.60 | NIST | |
| Inp | 906.50 | NIST | |
| Inp | 900.60 | NIST | |
| Inp | 934.80 | NIST | |
| Inp | 928.50 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 891.80 | NIST | |
| Inp | 934.80 | NIST | |
| Tboil | 417.66 | K | Relay (1.0) Calculated Property |
| Tc | [629.00; 629.00] | K |
|
| Tc | 629.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 629.00 ± 8.00 | K | NIST |
| Tc | 629.00 ± 8.00 | K | NIST |
| Vc | 0.294 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
Cheméo can also estimate Normal melting (fusion) point, Standard Gibbs free energy of formation, Log10 of Water solubility in mol/l 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.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [35.20; 43.00] | kJ/mol | [388.50; 388.50] | |
| ΔvapH | 43.00 ± 0.30 | kJ/mol | 388.50 | NIST |
| ΔvapH | 40.50 ± 0.30 | kJ/mol | 388.50 | NIST |
| ΔvapH | 38.00 ± 0.30 | kJ/mol | 388.50 | NIST |
| ΔvapH | 35.20 ± 0.50 | kJ/mol | 388.50 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [130.47; 379.62] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -9.20200e+01 | |||
| Coefficient B | 1.01752e+00 | |||
| Coefficient C | -8.15580e-04 | |||
| Coefficient D | 2.69700e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 130.47 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 177.82 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 218.27 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 252.66 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 281.85 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 306.69 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 328.03 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 346.74 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 363.65 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 379.62 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0006149; 0.0004721] | Pa×s | [234.67; 440.30] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -7.95988e+00 | |||
| Coefficient B | 1.32790e+02 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 234.67 | |||
| Temperature range, max. | 440.30 | |||
| η | 0.0006149 | Pa×s | 234.67 | Calculated Property |
| η | 0.0005848 | Pa×s | 257.52 | Calculated Property |
| η | 0.0005607 | Pa×s | 280.37 | Calculated Property |
| η | 0.0005411 | Pa×s | 303.21 | Calculated Property |
| η | 0.0005247 | Pa×s | 326.06 | Calculated Property |
| η | 0.0005109 | Pa×s | 348.91 | Calculated Property |
| η | 0.0004991 | Pa×s | 371.76 | Calculated Property |
| η | 0.0004889 | Pa×s | 394.60 | Calculated Property |
| η | 0.0004800 | Pa×s | 417.45 | Calculated Property |
| η | 0.0004721 | Pa×s | 440.30 | Calculated Property |
Find more compounds similar to 5-Ethylidene-2-norbornene, trans.
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