| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4491 | Relay (1.0) Calculated Property | |
| ΔcH°solid | [-7526.10; -7524.10] | kJ/mol |
|
| ΔcH°solid | -7526.10 ± 2.30 | kJ/mol | NIST |
| ΔcH°solid | -7524.10 ± 7.50 | kJ/mol | NIST |
| ΔfG° | 272.56 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 111.30 ± 3.60 | kJ/mol | NIST |
| ΔfH°solid | 16.20 ± 2.90 | kJ/mol | NIST |
| ΔfusH° | 19.32 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [95.10; 95.10] | kJ/mol |
|
| ΔsubH° | 95.10 ± 2.00 | kJ/mol | NIST |
| ΔsubH° | 95.10 ± 2.00 | kJ/mol | NIST |
| ΔsubH° | 95.10 | kJ/mol | NIST |
| ΔvapH° | 77.05 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.50 | eV | NIST |
| log10WS | -5.45 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.970 | Crippen Calculated Property | |
| McVol | 160.600 | ml/mol | McGowan Calculated Property |
| Pc | 2684.64 | kPa | Joback Calculated Property |
| Inp | [274.08; 1619.00] |
|
|
| Inp | 1583.00 | NIST | |
| Inp | 1619.00 | NIST | |
| Inp | 1596.80 | NIST | |
| Inp | 1607.60 | NIST | |
| Inp | 1614.20 | NIST | |
| Inp | 1596.80 | NIST | |
| Inp | 1607.60 | NIST | |
| Inp | 1614.20 | NIST | |
| Inp | 1616.00 | NIST | |
| Inp | 1590.00 | NIST | |
| Inp | 1594.00 | NIST | |
| Inp | 1583.00 | NIST | |
| Inp | 277.49 | NIST | |
| Inp | 274.50 | NIST | |
| Inp | 274.50 | NIST | |
| Inp | 274.08 | NIST | |
| Inp | 274.59 | NIST | |
| Inp | 277.00 | NIST | |
| Inp | 274.44 | NIST | |
| Inp | 274.59 | NIST | |
| Inp | 1583.00 | NIST | |
| Inp | 1596.80 | NIST | |
| Inp | 1614.20 | NIST | |
| Inp | 1594.00 | NIST | |
| Inp | 277.00 | NIST | |
| I | [2221.00; 2281.00] |
|
|
| I | 2281.00 | NIST | |
| I | 2236.00 | NIST | |
| I | 2221.00 | NIST | |
| I | 2281.00 | NIST | |
| Tboil | [559.00; 569.00] | K |
|
| Tboil | 568.20 | K | NIST |
| Tboil | 562.00 ± 4.00 | K | NIST |
| Tboil | 568.00 ± 4.00 | K | NIST |
| Tboil | 569.00 ± 4.00 | K | NIST |
| Tboil | 559.00 ± 5.00 | K | NIST |
| Tc | 779.89 | K | Relay (1.0) Calculated Property |
| Tfus | [355.00; 398.00] | K |
|
| Tfus | 395.00 ± 4.00 | K | NIST |
| Tfus | 394.30 ± 1.50 | K | NIST |
| Tfus | 395.00 ± 3.00 | K | NIST |
| Tfus | 394.00 ± 2.00 | K | NIST |
| Tfus | Outlier 355.00 ± 20.00 | K | NIST |
| Tfus | 393.00 ± 3.00 | K | NIST |
| Tfus | 394.10 ± 1.00 | K | NIST |
| Tfus | 392.70 ± 2.00 | K | NIST |
| Tfus | 394.00 ± 1.00 | K | NIST |
| Tfus | 392.90 ± 1.00 | K | NIST |
| Tfus | 394.00 ± 1.00 | K | NIST |
| Tfus | 394.00 ± 1.00 | K | NIST |
| Tfus | 396.00 ± 2.00 | K | NIST |
| Tfus | 393.00 ± 1.00 | K | NIST |
| Tfus | 391.70 ± 3.00 | K | NIST |
| Tfus | 394.70 ± 1.00 | K | NIST |
| Tfus | 393.70 ± 1.00 | K | NIST |
| Tfus | 395.00 ± 1.00 | K | NIST |
| Tfus | 394.70 ± 1.00 | K | NIST |
| Tfus | 391.00 ± 2.00 | K | NIST |
| Tfus | 391.00 ± 3.00 | K | NIST |
| Tfus | 392.70 ± 2.00 | K | NIST |
| Tfus | 394.00 ± 1.00 | K | NIST |
| Tfus | 394.00 ± 2.00 | K | NIST |
| Tfus | 398.00 ± 2.00 | K | NIST |
| Tfus | 398.00 ± 2.00 | K | NIST |
| Tfus | 394.00 ± 2.00 | K | NIST |
| Tfus | 394.00 ± 2.00 | K | NIST |
| Tfus | 394.00 ± 2.00 | K | NIST |
| Tfus | 395.00 ± 2.00 | K | NIST |
| Tfus | 395.70 ± 3.00 | K | NIST |
| Tfus | 394.00 ± 3.00 | K | NIST |
| Tfus | 394.00 ± 3.00 | K | NIST |
| Tfus | 394.00 ± 3.00 | K | NIST |
| Tfus | 394.00 ± 3.00 | K | NIST |
| Vc | 0.613 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [371.85; 457.50] | J/mol×K | [583.04; 824.77] | |
| Cp,gas | 371.85 | J/mol×K | 583.04 | Joback Calculated Property |
| Cp,gas | 388.95 | J/mol×K | 623.33 | Joback Calculated Property |
| Cp,gas | 404.83 | J/mol×K | 663.62 | Joback Calculated Property |
| Cp,gas | 419.57 | J/mol×K | 703.90 | Joback Calculated Property |
| Cp,gas | 433.22 | J/mol×K | 744.19 | Joback Calculated Property |
| Cp,gas | 445.84 | J/mol×K | 784.48 | Joback Calculated Property |
| Cp,gas | 457.50 | J/mol×K | 824.77 | Joback Calculated Property |
| η | [0.0001716; 0.0014925] | Pa×s | [325.42; 583.04] | |
| η | 0.0014925 | Pa×s | 325.42 | Joback Calculated Property |
| η | 0.0008435 | Pa×s | 368.36 | Joback Calculated Property |
| η | 0.0005371 | Pa×s | 411.29 | Joback Calculated Property |
| η | 0.0003724 | Pa×s | 454.23 | Joback Calculated Property |
| η | 0.0002751 | Pa×s | 497.17 | Joback Calculated Property |
| η | 0.0002132 | Pa×s | 540.10 | Joback Calculated Property |
| η | 0.0001716 | Pa×s | 583.04 | Joback Calculated Property |
| ΔvapH | 95.17 | kJ/mol | 298.15 | Vapour pressures and enthalpies of vaporization of a series of the alkylbiphenyls |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [422.92; 604.47] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42880e+01 | |||
| Coefficient B | -4.54144e+03 | |||
| Coefficient C | -9.85400e+01 | |||
| Temperature range, min. | 422.92 | |||
| Temperature range, max. | 604.47 | |||
| Pvap | 1.33 | kPa | 422.92 | Calculated Property |
| Pvap | 3.03 | kPa | 443.09 | Calculated Property |
| Pvap | 6.27 | kPa | 463.26 | Calculated Property |
| Pvap | 12.05 | kPa | 483.44 | Calculated Property |
| Pvap | 21.68 | kPa | 503.61 | Calculated Property |
| Pvap | 36.90 | kPa | 523.78 | Calculated Property |
| Pvap | 59.86 | kPa | 543.95 | Calculated Property |
| Pvap | 93.10 | kPa | 564.13 | Calculated Property |
| Pvap | 139.60 | kPa | 584.30 | Calculated Property |
| Pvap | 202.66 | kPa | 604.47 | Calculated Property |
Find more compounds similar to 4,4'-Dimethylbiphenyl.
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