| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6482 | Relay (1.0) Calculated Property | |
| ΔfG° | -231.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -423.33 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 25.34 | kJ/mol | Influence of the aromatic ring substituents on phase equilibria of vanillins in binary systems with CO2 |
| ΔvapH° | 73.05 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.57 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.77 | Aq. Solubility Prediction | |
| logPoct/wat | 1.603 | Crippen Calculated Property | |
| McVol | 127.220 | ml/mol | McGowan Calculated Property |
| Pc | 4109.14 | kPa | Joback Calculated Property |
| Inp | [1433.00; 1453.00] |
|
|
| Inp | Outlier 1433.00 | NIST | |
| Inp | 1452.00 | NIST | |
| Inp | 1446.00 | NIST | |
| Inp | 1453.00 | NIST | |
| Inp | 1448.00 | NIST | |
| Inp | 1448.00 | NIST | |
| Inp | 1448.00 | NIST | |
| I | [2414.00; 2514.00] |
|
|
| I | 2514.00 | NIST | |
| I | 2414.00 | NIST | |
| I | 2514.00 | NIST | |
| Tboil | 546.13 | K | Relay (1.0) Calculated Property |
| Tc | 785.33 | K | Relay (1.0) Calculated Property |
| Tfus | [350.40; 352.98] | K |
|
| Tfus | 350.40 | K | Aq. Solubility Prediction |
| Tfus | 352.98 | K | Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents |
| Tfus | 351.00 | K | Determination and Correlation of Ethyl Vanillin Solubility in Different Binary Solvents at Temperatures from 273.15 to 313.15 K |
| Vc | 0.451 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [304.26; 359.35] | J/mol×K | [588.68; 812.18] | |
| Cp,gas | 304.26 | J/mol×K | 588.68 | Joback Calculated Property |
| Cp,gas | 314.95 | J/mol×K | 625.93 | Joback Calculated Property |
| Cp,gas | 324.97 | J/mol×K | 663.18 | Joback Calculated Property |
| Cp,gas | 334.37 | J/mol×K | 700.43 | Joback Calculated Property |
| Cp,gas | 343.20 | J/mol×K | 737.68 | Joback Calculated Property |
| Cp,gas | 351.51 | J/mol×K | 774.93 | Joback Calculated Property |
| Cp,gas | 359.35 | J/mol×K | 812.18 | Joback Calculated Property |
| η | [0.0000432; 0.0008942] | Pa×s | [406.08; 588.68] | |
| η | 0.0008942 | Pa×s | 406.08 | Joback Calculated Property |
| η | 0.0004525 | Pa×s | 436.51 | Joback Calculated Property |
| η | 0.0002502 | Pa×s | 466.95 | Joback Calculated Property |
| η | 0.0001488 | Pa×s | 497.38 | Joback Calculated Property |
| η | 0.0000939 | Pa×s | 527.81 | Joback Calculated Property |
| η | 0.0000623 | Pa×s | 558.25 | Joback Calculated Property |
| η | 0.0000432 | Pa×s | 588.68 | Joback Calculated Property |
| ΔfusH | 23.10 | kJ/mol | 349.80 | NIST |
| ΔsubH | 101.50 | kJ/mol | 317.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.57e-03; 3234.93] | kPa | [350.65; 748.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.75341e+02 | |||
| Coefficient B | -1.86800e+04 | |||
| Coefficient C | -2.20762e+01 | |||
| Coefficient D | 6.79415e-06 | |||
| Temperature range, min. | 350.65 | |||
| Temperature range, max. | 748.00 | |||
| Pvap | 1.57e-03 | kPa | 350.65 | Calculated Property |
| Pvap | 0.06 | kPa | 394.80 | Calculated Property |
| Pvap | 0.80 | kPa | 438.95 | Calculated Property |
| Pvap | 6.19 | kPa | 483.10 | Calculated Property |
| Pvap | 31.00 | kPa | 527.25 | Calculated Property |
| Pvap | 112.81 | kPa | 571.40 | Calculated Property |
| Pvap | 324.90 | kPa | 615.55 | Calculated Property |
| Pvap | 786.65 | kPa | 659.70 | Calculated Property |
| Pvap | 1673.79 | kPa | 703.85 | Calculated Property |
| Pvap | 3234.93 | kPa | 748.00 | Calculated Property |
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