| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-7840.00; -7820.70] | kJ/mol |
|
| ΔcH°solid | -7840.00 ± 1.70 | kJ/mol | NIST |
| ΔcH°solid | -7820.70 ± 1.70 | kJ/mol | NIST |
| ΔfH°gas | -198.44 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | [-368.60; -349.40] | kJ/mol |
|
| ΔfH°solid | -349.40 ± 1.70 | kJ/mol | NIST |
| ΔfH°solid | -368.60 ± 1.80 | kJ/mol | NIST |
| ΔfusH° | 30.70 | kJ/mol | Solubility of Bisphenol A in Supercritical Carbon Dioxide |
| ΔvapH° | 117.23 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 7.88 | eV | Relay (1.0) Calculated Property |
| log10WS | -2.82 | Aq. Solubility Prediction | |
| logPoct/wat | 3.424 | Crippen Calculated Property | |
| McVol | 186.430 | ml/mol | McGowan Calculated Property |
| Pc | 3547.31 | kPa | Joback Calculated Property |
| Inp | [359.41; 2108.00] |
|
|
| Inp | 2108.00 | NIST | |
| Inp | 2108.00 | NIST | |
| Inp | 2108.00 | NIST | |
| Inp | 359.41 | NIST | |
| Inp | 2108.00 | NIST | |
| S°solid,1 bar | 287.70 | J/mol×K | NIST |
| Tboil | 601.12 | K | Relay (1.0) Calculated Property |
| Tc | 905.20 | K | Relay (1.0) Calculated Property |
| Tfus | [427.65; 431.00] | K |
|
| Tfus | 427.65 | K | Aq. Solubility Prediction |
| Tfus | 431.00 ± 4.00 | K | NIST |
| Ttriple | [433.00; 433.00] | K |
|
| Ttriple | 433.00 ± 1.00 | K | NIST |
| Ttriple | 433.00 ± 1.00 | K | NIST |
Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor 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 |
|---|---|---|---|---|
| Cp,gas | [528.97; 608.03] | J/mol×K | [753.97; 1018.62] | |
| Cp,gas | 528.97 | J/mol×K | 753.97 | Joback Calculated Property |
| Cp,gas | 543.20 | J/mol×K | 798.08 | Joback Calculated Property |
| Cp,gas | 556.63 | J/mol×K | 842.19 | Joback Calculated Property |
| Cp,gas | 569.54 | J/mol×K | 886.29 | Joback Calculated Property |
| Cp,gas | 582.22 | J/mol×K | 930.40 | Joback Calculated Property |
| Cp,gas | 594.96 | J/mol×K | 974.51 | Joback Calculated Property |
| Cp,gas | 608.03 | J/mol×K | 1018.62 | Joback Calculated Property |
| Cp,solid | 287.72 | J/mol×K | 298.15 | NIST |
| η | [0.0000007; 0.0000313] | Pa×s | [537.51; 753.97] | |
| η | 0.0000313 | Pa×s | 537.51 | Joback Calculated Property |
| η | 0.0000137 | Pa×s | 573.59 | Joback Calculated Property |
| η | 0.0000066 | Pa×s | 609.66 | Joback Calculated Property |
| η | 0.0000035 | Pa×s | 645.74 | Joback Calculated Property |
| η | 0.0000019 | Pa×s | 681.82 | Joback Calculated Property |
| η | 0.0000012 | Pa×s | 717.89 | Joback Calculated Property |
| η | 0.0000007 | Pa×s | 753.97 | Joback Calculated Property |
| ΔfusH | [30.10; 30.10] | kJ/mol | [433.00; 433.00] | |
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔvapH | 102.20 | kJ/mol | 550.00 | NIST |
| ΔfusS | [69.60; 69.60] | J/mol×K | [433.00; 433.00] | |
| ΔfusS | 69.60 | J/mol×K | 433.00 | NIST |
| ΔfusS | 69.60 | J/mol×K | 433.00 | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [493.20; 524.00] | K | [0.50; 1.70] |
|
| Tboilr | 493.20 | K | 0.50 | NIST |
| Tboilr | 524.00 ± 1.00 | K | 1.70 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [507.33; 665.02] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44248e+01 | |||
| Coefficient B | -4.04412e+03 | |||
| Coefficient C | -2.21266e+02 | |||
| Temperature range, min. | 507.33 | |||
| Temperature range, max. | 665.02 | |||
| Pvap | 1.33 | kPa | 507.33 | Calculated Property |
| Pvap | 3.01 | kPa | 524.85 | Calculated Property |
| Pvap | 6.24 | kPa | 542.37 | Calculated Property |
| Pvap | 11.97 | kPa | 559.89 | Calculated Property |
| Pvap | 21.53 | kPa | 577.41 | Calculated Property |
| Pvap | 36.67 | kPa | 594.94 | Calculated Property |
| Pvap | 59.55 | kPa | 612.46 | Calculated Property |
| Pvap | 92.76 | kPa | 629.98 | Calculated Property |
| Pvap | 139.32 | kPa | 647.50 | Calculated Property |
| Pvap | 202.63 | kPa | 665.02 | Calculated Property |
| Pvap | [4.93e-03; 3034.89] | kPa | [426.15; 849.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.95077e+02 | |||
| Coefficient B | -3.04193e+04 | |||
| Coefficient C | -3.80451e+01 | |||
| Coefficient D | 7.42083e-06 | |||
| Temperature range, min. | 426.15 | |||
| Temperature range, max. | 849.00 | |||
| Pvap | 4.93e-03 | kPa | 426.15 | Calculated Property |
| Pvap | 0.15 | kPa | 473.13 | Calculated Property |
| Pvap | 1.94 | kPa | 520.12 | Calculated Property |
| Pvap | 13.42 | kPa | 567.10 | Calculated Property |
| Pvap | 59.43 | kPa | 614.08 | Calculated Property |
| Pvap | 189.64 | kPa | 661.07 | Calculated Property |
| Pvap | 475.17 | kPa | 708.05 | Calculated Property |
| Pvap | 995.15 | kPa | 755.03 | Calculated Property |
| Pvap | 1824.84 | kPa | 802.02 | Calculated Property |
| Pvap | 3034.89 | kPa | 849.00 | Calculated Property |
Find more compounds similar to Phenol, 4,4'-(1-methylethylidene)bis-.
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