| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5598 | Relay (1.0) Calculated Property | |
| ΔcH°solid | [-6828.70; -6760.00] | kJ/mol |
|
| ΔcH°solid | -6784.00 ± 3.00 | kJ/mol | NIST |
| ΔcH°solid | -6760.00 ± 3.00 | kJ/mol | NIST |
| ΔcH°solid | -6784.80 | kJ/mol | NIST |
| ΔcH°solid | -6828.70 | kJ/mol | NIST |
| ΔfG° | 33.98 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -55.14 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | [-179.00; 138.00] | kJ/mol |
|
| ΔfH°solid | -154.00 | kJ/mol | NIST |
| ΔfH°solid | -179.00 | kJ/mol | NIST |
| ΔfH°solid | 138.00 | kJ/mol | NIST |
| ΔfusH° | 23.30 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 87.40 | kJ/mol | NIST |
| ΔvapH° | 84.17 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [8.68; 9.10] | eV |
|
| IE | 8.68 ± 0.05 | eV | NIST |
| IE | 8.72 | eV | NIST |
| IE | 8.86 ± 0.15 | eV | NIST |
| IE | 8.78 ± 0.05 | eV | NIST |
| IE | 8.90 ± 0.05 | eV | NIST |
| IE | 9.10 | eV | NIST |
| log10WS | -3.08 | Aq. Solubility Prediction | |
| logPoct/wat | 2.752 | Crippen Calculated Property | |
| McVol | 163.740 | ml/mol | McGowan Calculated Property |
| Pc | 3177.55 | kPa | Joback Calculated Property |
| Inp | 1768.00 | NIST | |
| S°gas | 480.18 | J/mol×K | NIST |
| S°solid,1 bar | 292.08 | J/mol×K | NIST |
| Tboil | 620.00 ± 1.00 | K | NIST |
| Tc | 869.69 | K | Relay (1.0) Calculated Property |
| Tfus | [367.00; 369.30] | K |
|
| Tfus | 368.01 | K | Aq. Solubility Prediction |
| Tfus | 368.50 | K | Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements |
| Tfus | 368.00 | K | The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters |
| Tfus | Outlier 369.30 ± 0.60 | K | NIST |
| Tfus | 368.15 ± 1.00 | K | NIST |
| Tfus | 368.25 ± 0.20 | K | NIST |
| Tfus | 368.00 | K | NIST |
| Tfus | 368.05 ± 0.20 | K | NIST |
| Tfus | Outlier 367.00 ± 1.00 | K | NIST |
| Tfus | 368.00 ± 2.00 | K | NIST |
| Tfus | 368.25 ± 1.00 | K | NIST |
| Tfus | 368.15 ± 2.00 | K | NIST |
| Ttriple | [368.00; 368.02] | K |
|
| Ttriple | 368.02 ± 0.01 | K | NIST |
| Ttriple | 368.00 ± 0.00 | K | NIST |
| Vc | 0.609 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [405.45; 471.08] | J/mol×K | [680.82; 933.59] | |
| Cp,gas | 405.45 | J/mol×K | 680.82 | Joback Calculated Property |
| Cp,gas | 419.25 | J/mol×K | 722.95 | Joback Calculated Property |
| Cp,gas | 431.79 | J/mol×K | 765.08 | Joback Calculated Property |
| Cp,gas | 443.16 | J/mol×K | 807.21 | Joback Calculated Property |
| Cp,gas | 453.44 | J/mol×K | 849.33 | Joback Calculated Property |
| Cp,gas | 462.72 | J/mol×K | 891.46 | Joback Calculated Property |
| Cp,gas | 471.08 | J/mol×K | 933.59 | Joback Calculated Property |
| Cp,solid | 245.70 | J/mol×K | 298.15 | NIST |
| η | [0.0001962; 0.0018672] | Pa×s | [400.24; 680.82] | |
| η | 0.0018672 | Pa×s | 400.24 | Joback Calculated Property |
| η | 0.0010540 | Pa×s | 447.00 | Joback Calculated Property |
| η | 0.0006630 | Pa×s | 493.77 | Joback Calculated Property |
| η | 0.0004519 | Pa×s | 540.53 | Joback Calculated Property |
| η | 0.0003274 | Pa×s | 587.29 | Joback Calculated Property |
| η | 0.0002487 | Pa×s | 634.06 | Joback Calculated Property |
| η | 0.0001962 | Pa×s | 680.82 | Joback Calculated Property |
| ΔfusH | [0.04; 23.80] | kJ/mol | [84.00; 369.20] | |
| ΔfusH | 0.04 | kJ/mol | 84.00 | NIST |
| ΔfusH | 23.56 | kJ/mol | 368.00 | NIST |
| ΔfusH | 23.56 | kJ/mol | 368.00 | NIST |
| ΔfusH | 22.69 | kJ/mol | 368.05 | NIST |
| ΔfusH | 22.88 | kJ/mol | 368.10 | NIST |
| ΔfusH | 23.80 | kJ/mol | 369.20 | NIST |
| ΔsubH | [82.80; 98.40] | kJ/mol | [311.00; 368.50] | |
| ΔsubH | 82.80 ± 0.80 | kJ/mol | 311.00 | NIST |
| ΔsubH | 98.40 ± 1.10 | kJ/mol | 329.50 | NIST |
| ΔsubH | 98.40 ± 1.10 | kJ/mol | 368.50 | NIST |
| ΔvapH | 69.20 | kJ/mol | 510.50 | NIST |
| ΔfusS | [0.50; 64.02] | J/mol×K | [84.00; 368.05] | |
| ΔfusS | 0.50 | J/mol×K | 84.00 | NIST |
| ΔfusS | 64.02 | J/mol×K | 368.00 | NIST |
| ΔfusS | 61.65 | J/mol×K | 368.05 | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 461.00 | K | 1.60 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [456.25; 658.97] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.56292e+01 | |||
| Coefficient B | -6.38708e+03 | |||
| Coefficient C | -3.99290e+01 | |||
| Temperature range, min. | 456.25 | |||
| Temperature range, max. | 658.97 | |||
| Pvap | 1.33 | kPa | 456.25 | Calculated Property |
| Pvap | 2.93 | kPa | 478.77 | Calculated Property |
| Pvap | 5.96 | kPa | 501.30 | Calculated Property |
| Pvap | 11.36 | kPa | 523.82 | Calculated Property |
| Pvap | 20.43 | kPa | 546.35 | Calculated Property |
| Pvap | 34.95 | kPa | 568.87 | Calculated Property |
| Pvap | 57.24 | kPa | 591.40 | Calculated Property |
| Pvap | 90.17 | kPa | 613.92 | Calculated Property |
| Pvap | 137.26 | kPa | 636.45 | Calculated Property |
| Pvap | 202.65 | kPa | 658.97 | Calculated Property |
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