| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3997 | Relay (1.0) Calculated Property | |
| ΔfG° | 175.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -120.40 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | -188.90 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 8.21 | kJ/mol | Thermodynamic properties of tert-butylbenzene and 1,4-di-tert-butylbenzene |
| ΔsubH° | 82.80 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | [61.40; 63.00] | kJ/mol |
|
| ΔvapH° | 63.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 61.40 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 63.00 ± 0.60 | kJ/mol | NIST |
| IE | [8.11; 8.74] | eV |
|
| IE | 8.24 ± 0.02 | eV | NIST |
| IE | 8.11 | eV | NIST |
| IE | 8.30 | eV | NIST |
| IE | Outlier 8.74 ± 0.07 | eV | NIST |
| IE | 8.31 | eV | NIST |
| IE | 8.28 | eV | NIST |
| IE | 8.40 | eV | NIST |
| log10WS | -6.02 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.282 | Crippen Calculated Property | |
| McVol | 184.360 | ml/mol | McGowan Calculated Property |
| Pc | 2300.00 ± 200.00 | kPa | NIST |
| ρc | 260.74 ± 15.04 | kg/m3 | NIST |
| Inp | [1264.00; 1319.00] |
|
|
| Inp | 1281.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1314.00 | NIST | |
| Inp | 1319.00 | NIST | |
| Inp | 1264.00 | NIST | |
| Inp | 1281.00 | NIST | |
| I | [1488.00; 1552.00] |
|
|
| I | 1495.10 | NIST | |
| I | 1515.00 | NIST | |
| I | 1516.00 | NIST | |
| I | 1528.00 | NIST | |
| I | 1540.00 | NIST | |
| I | 1552.00 | NIST | |
| I | 1504.00 | NIST | |
| I | 1488.00 | NIST | |
| I | 1488.00 | NIST | |
| Tboil | 508.15 ± 2.00 | K | NIST |
| Tc | 708.00 ± 2.00 | K | NIST |
| Tfus | 318.69 | K | Relay (1.0) Calculated Property |
| Ttriple | 350.80 ± 0.30 | K | NIST |
| Vc | 0.705 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [448.22; 550.95] | J/mol×K | [544.92; 764.89] | |
| Cp,gas | 448.22 | J/mol×K | 544.92 | Joback Calculated Property |
| Cp,gas | 468.56 | J/mol×K | 581.58 | Joback Calculated Property |
| Cp,gas | 487.49 | J/mol×K | 618.24 | Joback Calculated Property |
| Cp,gas | 505.11 | J/mol×K | 654.91 | Joback Calculated Property |
| Cp,gas | 521.50 | J/mol×K | 691.57 | Joback Calculated Property |
| Cp,gas | 536.75 | J/mol×K | 728.23 | Joback Calculated Property |
| Cp,gas | 550.95 | J/mol×K | 764.89 | Joback Calculated Property |
| η | [0.0001510; 0.0042689] | Pa×s | [291.32; 544.92] | |
| η | 0.0042689 | Pa×s | 291.32 | Joback Calculated Property |
| η | 0.0017186 | Pa×s | 333.59 | Joback Calculated Property |
| η | 0.0008490 | Pa×s | 375.85 | Joback Calculated Property |
| η | 0.0004837 | Pa×s | 418.12 | Joback Calculated Property |
| η | 0.0003055 | Pa×s | 460.39 | Joback Calculated Property |
| η | 0.0002085 | Pa×s | 502.65 | Joback Calculated Property |
| η | 0.0001510 | Pa×s | 544.92 | Joback Calculated Property |
| ΔfusH | [8.20; 22.48] | kJ/mol | [341.50; 350.80] | |
| ΔfusH | 22.48 | kJ/mol | 341.50 | NIST |
| ΔfusH | 8.20 | kJ/mol | 350.80 | NIST |
| ΔsubH | [82.10; 82.80] | kJ/mol | [305.00; 310.50] | |
| ΔsubH | 82.80 | kJ/mol | 305.00 | NIST |
| ΔsubH | 82.10 ± 0.40 | kJ/mol | 310.50 | NIST |
| ΔvapH | [44.60; 61.40] | kJ/mol | [439.00; 439.00] | |
| ΔvapH | 55.80 ± 0.10 | kJ/mol | 439.00 | NIST |
| ΔvapH | 54.60 ± 0.10 | kJ/mol | 439.00 | NIST |
| ΔvapH | 61.40 ± 0.10 | kJ/mol | 439.00 | NIST |
| ΔvapH | 46.40 ± 0.20 | kJ/mol | 439.00 | NIST |
| ΔvapH | 44.60 ± 0.30 | kJ/mol | 439.00 | NIST |
| Pvap | [0.38; 1.65] | kPa | [354.15; 383.25] | |
| Pvap | 0.38 | kPa | 354.15 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.43 | kPa | 356.45 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.49 | kPa | 358.95 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.57 | kPa | 361.75 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.65 | kPa | 364.25 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.72 | kPa | 366.45 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.72 | kPa | 366.55 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.81 | kPa | 369.15 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 0.94 | kPa | 372.05 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 1.04 | kPa | 374.15 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 1.17 | kPa | 376.45 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 1.38 | kPa | 379.75 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 1.51 | kPa | 381.75 | Study and prediction of alkylbenzenes vapour pressures |
| Pvap | 1.65 | kPa | 383.25 | Study and prediction of alkylbenzenes vapour pressures |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [383.07; 538.55] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49987e+01 | |||
| Coefficient B | -4.41062e+03 | |||
| Coefficient C | -8.32500e+01 | |||
| Temperature range, min. | 383.07 | |||
| Temperature range, max. | 538.55 | |||
| Pvap | 1.33 | kPa | 383.07 | Calculated Property |
| Pvap | 2.97 | kPa | 400.35 | Calculated Property |
| Pvap | 6.10 | kPa | 417.62 | Calculated Property |
| Pvap | 11.66 | kPa | 434.90 | Calculated Property |
| Pvap | 20.97 | kPa | 452.17 | Calculated Property |
| Pvap | 35.80 | kPa | 469.45 | Calculated Property |
| Pvap | 58.39 | kPa | 486.72 | Calculated Property |
| Pvap | 91.46 | kPa | 504.00 | Calculated Property |
| Pvap | 138.29 | kPa | 521.27 | Calculated Property |
| Pvap | 202.64 | kPa | 538.55 | Calculated Property |
Find more compounds similar to Benzene, 1,4-bis(1,1-dimethylethyl)-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.