| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6445 | Relay (1.0) Calculated Property | |
| ΔfG° | -442.94 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -869.28 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 24.64 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 66.25 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.62 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.33 | Aq. Solubility Prediction | |
| logPoct/wat | 1.283 | Crippen Calculated Property | |
| McVol | 152.550 | ml/mol | McGowan Calculated Property |
| Pc | 2525.19 | kPa | Joback Calculated Property |
| Inp | [1247.00; 1292.00] |
|
|
| Inp | 1280.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1282.10 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1284.00 | NIST | |
| Inp | Outlier 1247.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | 1284.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1280.00 | NIST | |
| I | [1763.00; 1780.00] |
|
|
| I | 1780.00 | NIST | |
| I | 1768.00 | NIST | |
| I | 1774.00 | NIST | |
| I | 1768.00 | NIST | |
| I | 1780.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1774.00 | NIST | |
| I | 1780.00 | NIST | |
| I | 1774.00 | NIST | |
| I | 1768.00 | NIST | |
| Tboil | [506.83; 510.20] | K |
|
| Tboil | 506.83 | K | KDB |
| Tboil | 509.60 | K | Liquid-liquid equilibria of (water + butyric acid + diethyl succinate or diethyl glutarate or diethyl adipate) ternary systems |
| Tboil | 509.60 | K | (Liquid + liquid) equilibria of (water + propionic acid + diethyl succinate or diethyl glutarate or diethyl adipate) ternary systems |
| Tboil | 509.65 | K | Liquid-Liquid Equilibria of (Water + Acetic Acid + Diethyl Succinate or Diethyl Glutarate or Diethyl Adipate) Ternary Systems |
| Tboil | 510.20 | K | NIST |
| Tc | 682.00 | K | Vapor-liquid critical temperatures and pressures of dicarboxylic acid diethyl esters |
| Tfus | 249.05 | K | Aq. Solubility Prediction |
| Vc | 0.595 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [382.63; 534.27] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.76176e+01 | |||
| Coefficient B | -6.43695e+03 | |||
| Coefficient C | -1.11990e+01 | |||
| Temperature range, min. | 382.63 | |||
| Temperature range, max. | 534.27 | |||
| Pvap | 1.33 | kPa | 382.63 | Calculated Property |
| Pvap | 2.83 | kPa | 399.48 | Calculated Property |
| Pvap | 5.63 | kPa | 416.33 | Calculated Property |
| Pvap | 10.63 | kPa | 433.18 | Calculated Property |
| Pvap | 19.09 | kPa | 450.03 | Calculated Property |
| Pvap | 32.83 | kPa | 466.87 | Calculated Property |
| Pvap | 54.33 | kPa | 483.72 | Calculated Property |
| Pvap | 86.85 | kPa | 500.57 | Calculated Property |
| Pvap | 134.55 | kPa | 517.42 | Calculated Property |
| Pvap | 202.67 | kPa | 534.27 | Calculated Property |
| Pvap | [0.13; 101.31] | kPa | [338.15; 510.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.84059e+01 | |||
| Coefficient B | -7.19382e+03 | |||
| Coefficient C | -1.58556e+00 | |||
| Coefficient D | 7.65275e-07 | |||
| Temperature range, min. | 338.15 | |||
| Temperature range, max. | 510.15 | |||
| Pvap | 0.13 | kPa | 338.15 | Calculated Property |
| Pvap | 0.39 | kPa | 357.26 | Calculated Property |
| Pvap | 1.00 | kPa | 376.37 | Calculated Property |
| Pvap | 2.35 | kPa | 395.48 | Calculated Property |
| Pvap | 5.10 | kPa | 414.59 | Calculated Property |
| Pvap | 10.33 | kPa | 433.71 | Calculated Property |
| Pvap | 19.68 | kPa | 452.82 | Calculated Property |
| Pvap | 35.55 | kPa | 471.93 | Calculated Property |
| Pvap | 61.27 | kPa | 491.04 | Calculated Property |
| Pvap | 101.31 | kPa | 510.15 | Calculated Property |
Find more compounds similar to Pentanedioic acid, diethyl ester.
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