| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.9213 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -4110.90 ± 1.30 | kJ/mol | NIST |
| ΔfG° | -515.00 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -885.76 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | [2.00; 30.52] | kJ/mol |
|
| ΔfusH° | 2.00 | kJ/mol | Vaporization, fusion and sublimation enthalpies of the dicarboxylic acids from C4 to C14 and C16 |
| ΔfusH° | 30.52 | kJ/mol | Solid Liquid Equilibria for Six Binary Mixtures of Pentanedioic Acid, Octanedioic Acid, 3-Methylheptanedioic Acid, 2,2-Dimethylbutanedioic Acid, and 2,3-Dimethylbutanedioic Acid |
| ΔsubH° | [143.00; 147.80] | kJ/mol |
|
| ΔsubH° | 147.80 ± 3.80 | kJ/mol | NIST |
| ΔsubH° | 143.00 ± 4.00 | kJ/mol | NIST |
| ΔvapH° | 116.70 ± 0.80 | kJ/mol | NIST |
| IE | 9.96 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.96 | Aq. Solubility Prediction | |
| logPoct/wat | 1.496 | Crippen Calculated Property | |
| McVol | 138.460 | ml/mol | McGowan Calculated Property |
| Pc | 2970.00 | kPa | Critical Temperatures and Pressures of Straight-Chain Saturated Dicarboxylic Acids (C4 to C14) |
| Tboil | 545.30 | K | Relay (1.0) Calculated Property |
| Tc | 761.02 | K | Relay (1.0) Calculated Property |
| Tfus | [410.00; 417.00] | K |
|
| Tfus | 416.65 | K | Aq. Solubility Prediction |
| Tfus | 415.50 ± 0.40 | K | NIST |
| Tfus | 415.50 ± 0.30 | K | NIST |
| Tfus | 417.00 ± 1.50 | K | NIST |
| Tfus | 415.50 ± 0.50 | K | NIST |
| Tfus | 413.00 ± 4.00 | K | NIST |
| Tfus | Outlier 410.00 ± 3.00 | K | NIST |
| Vc | 0.518 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [372.64; 418.19] | J/mol×K | [674.54; 847.61] | |
| Cp,gas | 372.64 | J/mol×K | 674.54 | Joback Calculated Property |
| Cp,gas | 381.25 | J/mol×K | 703.39 | Joback Calculated Property |
| Cp,gas | 389.43 | J/mol×K | 732.23 | Joback Calculated Property |
| Cp,gas | 397.21 | J/mol×K | 761.08 | Joback Calculated Property |
| Cp,gas | 404.58 | J/mol×K | 789.92 | Joback Calculated Property |
| Cp,gas | 411.58 | J/mol×K | 818.77 | Joback Calculated Property |
| Cp,gas | 418.19 | J/mol×K | 847.61 | Joback Calculated Property |
| η | [0.0000238; 0.0036765] | Pa×s | [401.42; 674.54] | |
| η | 0.0036765 | Pa×s | 401.42 | Joback Calculated Property |
| η | 0.0010352 | Pa×s | 446.94 | Joback Calculated Property |
| η | 0.0003684 | Pa×s | 492.46 | Joback Calculated Property |
| η | 0.0001562 | Pa×s | 537.98 | Joback Calculated Property |
| η | 0.0000757 | Pa×s | 583.50 | Joback Calculated Property |
| η | 0.0000407 | Pa×s | 629.02 | Joback Calculated Property |
| η | 0.0000238 | Pa×s | 674.54 | Joback Calculated Property |
| ΔfusH | [28.82; 30.70] | kJ/mol | [413.20; 415.30] | |
| ΔfusH | 30.70 | kJ/mol | 413.20 | NIST |
| ΔfusH | 28.82 | kJ/mol | 415.30 | NIST |
| ΔfusH | 28.82 | kJ/mol | 415.30 | NIST |
| ΔsubH | [143.10; 168.00] | kJ/mol | [315.00; 393.00] | |
| ΔsubH | 148.00 | kJ/mol | 315.00 | NIST |
| ΔsubH | 168.00 ± 7.00 | kJ/mol | 363.00 | NIST |
| ΔsubH | 143.10 ± 3.80 | kJ/mol | 393.00 | NIST |
| ΔvapH | 91.40 | kJ/mol | 532.00 | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 503.20 | K | 2.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [493.40; 646.40] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.77470e+01 | |||
| Coefficient B | -6.61200e+03 | |||
| Coefficient C | -1.14691e+02 | |||
| Temperature range, min. | 493.40 | |||
| Temperature range, max. | 646.40 | |||
| Pvap | 1.33 | kPa | 493.40 | Calculated Property |
| Pvap | 2.82 | kPa | 510.40 | Calculated Property |
| Pvap | 5.62 | kPa | 527.40 | Calculated Property |
| Pvap | 10.59 | kPa | 544.40 | Calculated Property |
| Pvap | 19.02 | kPa | 561.40 | Calculated Property |
| Pvap | 32.72 | kPa | 578.40 | Calculated Property |
| Pvap | 54.18 | kPa | 595.40 | Calculated Property |
| Pvap | 86.67 | kPa | 612.40 | Calculated Property |
| Pvap | 134.40 | kPa | 629.40 | Calculated Property |
| Pvap | 202.67 | kPa | 646.40 | Calculated Property |
| Pvap | [2.20e-04; 110.52] | kPa | [379.15; 619.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.35392e+03 | |||
| Coefficient B | -8.05167e+04 | |||
| Coefficient C | -1.96409e+02 | |||
| Coefficient D | 1.13237e-04 | |||
| Temperature range, min. | 379.15 | |||
| Temperature range, max. | 619.15 | |||
| Pvap | 2.20e-04 | kPa | 379.15 | Calculated Property |
| Pvap | 4.32e-03 | kPa | 405.82 | Calculated Property |
| Pvap | 0.04 | kPa | 432.48 | Calculated Property |
| Pvap | 0.24 | kPa | 459.15 | Calculated Property |
| Pvap | 0.96 | kPa | 485.82 | Calculated Property |
| Pvap | 3.02 | kPa | 512.48 | Calculated Property |
| Pvap | 8.09 | kPa | 539.15 | Calculated Property |
| Pvap | 19.75 | kPa | 565.82 | Calculated Property |
| Pvap | 46.54 | kPa | 592.48 | Calculated Property |
| Pvap | 110.52 | kPa | 619.15 | Calculated Property |
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