| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.1558 | Relay (1.0) Calculated Property | |
| ΔfG° | -213.86 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -902.40 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 57.14 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 109.02 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.24 | eV | Relay (1.0) Calculated Property |
| log10WS | [-5.12; -5.11] |
|
|
| log10WS | -5.11 | Aq. Solubility Prediction | |
| log10WS | -5.12 | Estimated Solubility | |
| logPoct/wat | 6.721 | Crippen Calculated Property | |
| McVol | 340.140 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| Pc | 1080.00 | kPa | Critical Temperatures and Pressures of 12 Phthalates Using the Pulse-Heating Method |
| Inp | [420.40; 2741.00] |
|
|
| Inp | 420.40 | NIST | |
| Inp | 2682.00 | NIST | |
| Inp | 2741.00 | NIST | |
| Inp | 2686.00 | NIST | |
| Inp | 2687.00 | NIST | |
| Tboil | 660.10 | K | Relay (1.0) Calculated Property |
| Tc | 860.89 | K | Relay (1.0) Calculated Property |
| Tfus | 255.82 | K | Aq. Solubility Prediction |
| Vc | 1.293 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [1119.44; 1201.88] | J/mol×K | [932.76; 1142.45] | |
| Cp,gas | 1119.44 | J/mol×K | 932.76 | Joback Calculated Property |
| Cp,gas | 1136.46 | J/mol×K | 967.71 | Joback Calculated Property |
| Cp,gas | 1152.13 | J/mol×K | 1002.66 | Joback Calculated Property |
| Cp,gas | 1166.46 | J/mol×K | 1037.60 | Joback Calculated Property |
| Cp,gas | 1179.51 | J/mol×K | 1072.55 | Joback Calculated Property |
| Cp,gas | 1191.30 | J/mol×K | 1107.50 | Joback Calculated Property |
| Cp,gas | 1201.88 | J/mol×K | 1142.45 | Joback Calculated Property |
| η | [0.0000308; 0.0003848] | Pa×s | [543.50; 932.76] | |
| η | 0.0003848 | Pa×s | 543.50 | Joback Calculated Property |
| η | 0.0002018 | Pa×s | 608.38 | Joback Calculated Property |
| η | 0.0001199 | Pa×s | 673.25 | Joback Calculated Property |
| η | 0.0000780 | Pa×s | 738.13 | Joback Calculated Property |
| η | 0.0000544 | Pa×s | 803.01 | Joback Calculated Property |
| η | 0.0000401 | Pa×s | 867.88 | Joback Calculated Property |
| η | 0.0000308 | Pa×s | 932.76 | Joback Calculated Property |
| ΔvapH | 122.70 | kJ/mol | 298.00 | A Comparison of Results by Correlation Gas Chromatography with Another Gas Chromatographic Retention Time Technique. The Effects of Retention Time Coincidence on Vaporization Enthalpy and Vapor Pressure |
| n0 | [1.48100; 1.48500] | [298.15; 308.15] | ||
| n0 | 1.48500 | 298.15 | Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K | |
| n0 | 1.48310 | 303.15 | Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K | |
| n0 | 1.48100 | 308.15 | Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K | |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [508.80; 761.92] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.29723e+01 | |||
| Coefficient B | -4.89620e+03 | |||
| Coefficient C | -1.22804e+02 | |||
| Temperature range, min. | 508.80 | |||
| Temperature range, max. | 761.92 | |||
| Pvap | 1.33 | kPa | 508.80 | Calculated Property |
| Pvap | 3.16 | kPa | 536.92 | Calculated Property |
| Pvap | 6.69 | kPa | 565.05 | Calculated Property |
| Pvap | 12.98 | kPa | 593.17 | Calculated Property |
| Pvap | 23.34 | kPa | 621.30 | Calculated Property |
| Pvap | 39.44 | kPa | 649.42 | Calculated Property |
| Pvap | 63.20 | kPa | 677.55 | Calculated Property |
| Pvap | 96.75 | kPa | 705.67 | Calculated Property |
| Pvap | 142.42 | kPa | 733.80 | Calculated Property |
| Pvap | 202.64 | kPa | 761.92 | Calculated Property |
| Pvap | [4.11e-03; 0.92] | kPa | [423.15; 523.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.27880e+01 | |||
| Coefficient B | -1.19674e+04 | |||
| Coefficient C | 1.07854e-04 | |||
| Coefficient D | -9.54457e-11 | |||
| Temperature range, min. | 423.15 | |||
| Temperature range, max. | 523.15 | |||
| Pvap | 4.11e-03 | kPa | 423.15 | Calculated Property |
| Pvap | 8.48e-03 | kPa | 434.26 | Calculated Property |
| Pvap | 0.02 | kPa | 445.37 | Calculated Property |
| Pvap | 0.03 | kPa | 456.48 | Calculated Property |
| Pvap | 0.06 | kPa | 467.59 | Calculated Property |
| Pvap | 0.11 | kPa | 478.71 | Calculated Property |
| Pvap | 0.19 | kPa | 489.82 | Calculated Property |
| Pvap | 0.33 | kPa | 500.93 | Calculated Property |
| Pvap | 0.56 | kPa | 512.04 | Calculated Property |
| Pvap | 0.92 | kPa | 523.15 | Calculated Property |
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