| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.1048 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -7397.30 ± 3.30 | kJ/mol | NIST |
| ΔfG° | -472.90 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -984.11 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 49.40 | kJ/mol | Vaporization, fusion and sublimation enthalpies of the dicarboxylic acids from C4 to C14 and C16 |
| ΔvapH° | 137.74 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.76 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.55 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.447 | Crippen Calculated Property | |
| McVol | 208.910 | ml/mol | McGowan Calculated Property |
| Pc | 2151.31 | kPa | Joback Calculated Property |
| Tboil | 580.31 | K | Relay (1.0) Calculated Property |
| Tc | 801.56 | K | Relay (1.0) Calculated Property |
| Tfus | [386.21; 387.50] | K |
|
| Tfus | 386.21 | K | Solubility of tridecanedioic acid in pure solvent systems: An experimental and computational study |
| Tfus | 387.50 ± 0.50 | K | NIST |
| Vc | 0.797 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [634.46; 696.66] | J/mol×K | [788.94; 968.90] | |
| Cp,gas | 634.46 | J/mol×K | 788.94 | Joback Calculated Property |
| Cp,gas | 646.32 | J/mol×K | 818.93 | Joback Calculated Property |
| Cp,gas | 657.56 | J/mol×K | 848.93 | Joback Calculated Property |
| Cp,gas | 668.18 | J/mol×K | 878.92 | Joback Calculated Property |
| Cp,gas | 678.23 | J/mol×K | 908.91 | Joback Calculated Property |
| Cp,gas | 687.71 | J/mol×K | 938.90 | Joback Calculated Property |
| Cp,gas | 696.66 | J/mol×K | 968.90 | Joback Calculated Property |
| η | [0.0000077; 0.0011525] | Pa×s | [457.77; 788.94] | |
| η | 0.0011525 | Pa×s | 457.77 | Joback Calculated Property |
| η | 0.0003189 | Pa×s | 512.96 | Joback Calculated Property |
| η | 0.0001133 | Pa×s | 568.16 | Joback Calculated Property |
| η | 0.0000483 | Pa×s | 623.36 | Joback Calculated Property |
| η | 0.0000237 | Pa×s | 678.55 | Joback Calculated Property |
| η | 0.0000129 | Pa×s | 733.74 | Joback Calculated Property |
| η | 0.0000077 | Pa×s | 788.94 | Joback Calculated Property |
| ΔfusH | [45.30; 49.40] | kJ/mol | [386.30; 387.50] | |
| ΔfusH | 49.40 | kJ/mol | 386.30 | NIST |
| ΔfusH | 45.30 | kJ/mol | 387.50 | NIST |
| ΔfusS | 116.90 | J/mol×K | 387.50 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [526.87; 727.52] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53406e+01 | |||
| Coefficient B | -6.02945e+03 | |||
| Coefficient C | -1.26323e+02 | |||
| Temperature range, min. | 526.87 | |||
| Temperature range, max. | 727.52 | |||
| Pvap | 1.33 | kPa | 526.87 | Calculated Property |
| Pvap | 2.95 | kPa | 549.16 | Calculated Property |
| Pvap | 6.02 | kPa | 571.46 | Calculated Property |
| Pvap | 11.49 | kPa | 593.75 | Calculated Property |
| Pvap | 20.67 | kPa | 616.05 | Calculated Property |
| Pvap | 35.33 | kPa | 638.34 | Calculated Property |
| Pvap | 57.75 | kPa | 660.64 | Calculated Property |
| Pvap | 90.75 | kPa | 682.93 | Calculated Property |
| Pvap | 137.72 | kPa | 705.23 | Calculated Property |
| Pvap | 202.65 | kPa | 727.52 | Calculated Property |
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