| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.9797 | Relay (1.0) Calculated Property | |
| ΔfG° | 44.08 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -507.38 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 46.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 119.30 | kJ/mol | NIST |
| IE | 9.15 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.50 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.016 | Crippen Calculated Property | |
| McVol | 266.050 | ml/mol | McGowan Calculated Property |
| Pc | 1273.69 | kPa | Joback Calculated Property |
| Inp | [2060.00; 2068.80] |
|
|
| Inp | 2068.80 | NIST | |
| Inp | 2060.00 | NIST | |
| Inp | 2060.00 | NIST | |
| Inp | 2066.00 | NIST | |
| I | [2116.00; 2116.00] |
|
|
| I | 2116.00 | NIST | |
| I | 2116.00 | NIST | |
| Tboil | 605.26 | K | Relay (1.0) Calculated Property |
| Tc | 782.26 | K | Relay (1.0) Calculated Property |
| Tfus | [272.15; 309.00] | K |
|
| Tfus | 272.15 | K | The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect |
| Tfus | 309.00 ± 2.00 | K | NIST |
| Tfus | 273.15 ± 3.00 | K | NIST |
| Vc | 1.012 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [785.17; 879.39] | J/mol×K | [707.58; 874.01] | |
| Cp,gas | 785.17 | J/mol×K | 707.58 | Joback Calculated Property |
| Cp,gas | 802.67 | J/mol×K | 735.32 | Joback Calculated Property |
| Cp,gas | 819.41 | J/mol×K | 763.06 | Joback Calculated Property |
| Cp,gas | 835.41 | J/mol×K | 790.79 | Joback Calculated Property |
| Cp,gas | 850.72 | J/mol×K | 818.53 | Joback Calculated Property |
| Cp,gas | 865.37 | J/mol×K | 846.27 | Joback Calculated Property |
| Cp,gas | 879.39 | J/mol×K | 874.01 | Joback Calculated Property |
| η | [0.0000243; 0.0053551] | Pa×s | [348.36; 707.58] | |
| η | 0.0053551 | Pa×s | 348.36 | Joback Calculated Property |
| η | 0.0011274 | Pa×s | 408.23 | Joback Calculated Property |
| η | 0.0003536 | Pa×s | 468.10 | Joback Calculated Property |
| η | 0.0001442 | Pa×s | 527.97 | Joback Calculated Property |
| η | 0.0000706 | Pa×s | 587.84 | Joback Calculated Property |
| η | 0.0000395 | Pa×s | 647.71 | Joback Calculated Property |
| η | 0.0000243 | Pa×s | 707.58 | Joback Calculated Property |
| Pvap | 2.00 | kPa | 480.05 | Phase equilibria of liquid (water + butyric acid + oleyl alcohol) ternary system |
| n0 | [1.46010; 1.46030] | [293.15; 293.15] | ||
| n0 | 1.46030 | 293.15 | Liquid phase equilibria of (water + propionic acid + oleyl alcohol) ternary system at several temperatures | |
| n0 | 1.46010 | 293.15 | Distribution of Butyric Acid between Water and Several Solvents | |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [480.00; 480.70] | K | [1.70; 2.00] |
|
| Tboilr | 480.20 | K | 1.70 | NIST |
| Tboilr | 480.00 | K | 1.70 | NIST |
| Tboilr | 480.70 | K | 2.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [493.72; 687.67] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50364e+01 | |||
| Coefficient B | -5.53733e+03 | |||
| Coefficient C | -1.18278e+02 | |||
| Temperature range, min. | 493.72 | |||
| Temperature range, max. | 687.67 | |||
| Pvap | 1.33 | kPa | 493.72 | Calculated Property |
| Pvap | 2.97 | kPa | 515.27 | Calculated Property |
| Pvap | 6.09 | kPa | 536.82 | Calculated Property |
| Pvap | 11.64 | kPa | 558.37 | Calculated Property |
| Pvap | 20.94 | kPa | 579.92 | Calculated Property |
| Pvap | 35.75 | kPa | 601.47 | Calculated Property |
| Pvap | 58.31 | kPa | 623.02 | Calculated Property |
| Pvap | 91.38 | kPa | 644.57 | Calculated Property |
| Pvap | 138.22 | kPa | 666.12 | Calculated Property |
| Pvap | 202.64 | kPa | 687.67 | Calculated Property |
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