| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6341 | Relay (1.0) Calculated Property | |
| PAff | 843.20 | kJ/mol | NIST |
| BasG | 812.30 | kJ/mol | NIST |
| ΔcH°solid | -4631.66 ± 0.88 | kJ/mol | NIST |
| EA | [0.64; 0.82] | eV |
|
| EA | 0.82 ± 0.09 | eV | NIST |
| EA | 0.82 ± 0.09 | eV | NIST |
| EA | 0.64 | eV | NIST |
| ΔfH°gas | -629.35 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | [-732.60; -710.00] | kJ/mol |
|
| ΔfH°solid | -710.00 | kJ/mol | NIST |
| ΔfH°solid | -732.60 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | [33.01; 35.50] | kJ/mol |
|
| ΔfusH° | 35.50 | kJ/mol | New aspects of relationship between the enthalpies of fusion of aromatic compounds at the melting temperature and the enthalpies of solution in benzene at 298.15 K. Part II |
| ΔfusH° | 33.01 | kJ/mol | Thermal analysis of phase change materials in the temperature range 120.150 .C |
| ΔsubH° | [104.60; 104.60] | kJ/mol |
|
| ΔsubH° | 104.60 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 104.60 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 83.31 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.78 ± 0.03 | eV | NIST |
| log10WS | -3.72 | Aq. Solubility Prediction | |
| logPoct/wat | 1.260 | Crippen Calculated Property | |
| McVol | 142.880 | ml/mol | McGowan Calculated Property |
| Pc | 2915.53 | kPa | Joback Calculated Property |
| Inp | [1461.00; 1512.00] |
|
|
| Inp | 1461.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1480.00 | NIST | |
| Inp | 1492.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1469.00 | NIST | |
| Inp | Outlier 1512.00 | NIST | |
| Inp | 1468.00 | NIST | |
| Inp | 1473.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Inp | Outlier 1512.00 | NIST | |
| Inp | 1469.00 | NIST | |
| Inp | 1475.00 | NIST | |
| Tboil | 550.85 | K | Relay (1.0) Calculated Property |
| Tc | 779.00 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tfus | [413.00; 415.20] | K |
|
| Tfus | 414.40 | K | Aq. Solubility Prediction |
| Tfus | Outlier 415.20 ± 0.20 | K | NIST |
| Tfus | 413.80 ± 0.01 | K | NIST |
| Tfus | 413.80 ± 0.20 | K | NIST |
| Tfus | 413.00 ± 4.00 | K | NIST |
| Tfus | 413.00 ± 1.50 | K | NIST |
| Tfus | 413.80 ± 0.01 | K | NIST |
| Tfus | 413.80 ± 0.20 | K | NIST |
| Ttriple | 413.88 | K | Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions |
| Vc | 0.536 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [332.72; 395.80] | J/mol×K | [576.50; 791.05] | |
| Cp,gas | 332.72 | J/mol×K | 576.50 | Joback Calculated Property |
| Cp,gas | 345.19 | J/mol×K | 612.26 | Joback Calculated Property |
| Cp,gas | 356.88 | J/mol×K | 648.02 | Joback Calculated Property |
| Cp,gas | 367.79 | J/mol×K | 683.78 | Joback Calculated Property |
| Cp,gas | 377.91 | J/mol×K | 719.54 | Joback Calculated Property |
| Cp,gas | 387.25 | J/mol×K | 755.29 | Joback Calculated Property |
| Cp,gas | 395.80 | J/mol×K | 791.05 | Joback Calculated Property |
| Cp,solid | [261.10; 276.10] | J/mol×K | [298.15; 353.00] | |
| Cp,solid | 261.10 | J/mol×K | 298.15 | NIST |
| Cp,solid | 276.10 | J/mol×K | 353.00 | NIST |
| η | [0.0001516; 0.0022172] | Pa×s | [326.06; 576.50] | |
| η | 0.0022172 | Pa×s | 326.06 | Joback Calculated Property |
| η | 0.0011001 | Pa×s | 367.80 | Joback Calculated Property |
| η | 0.0006296 | Pa×s | 409.54 | Joback Calculated Property |
| η | 0.0003996 | Pa×s | 451.28 | Joback Calculated Property |
| η | 0.0002739 | Pa×s | 493.02 | Joback Calculated Property |
| η | 0.0001991 | Pa×s | 534.76 | Joback Calculated Property |
| η | 0.0001516 | Pa×s | 576.50 | Joback Calculated Property |
| ΔfusH | [31.63; 32.10] | kJ/mol | [413.79; 415.40] | |
| ΔfusH | 31.63 | kJ/mol | 413.79 | NIST |
| ΔfusH | 31.63 | kJ/mol | 413.79 | NIST |
| ΔfusH | 32.10 | kJ/mol | 413.80 | NIST |
| ΔfusH | 32.09 | kJ/mol | 413.80 | NIST |
| ΔfusH | 32.10 | kJ/mol | 413.80 | NIST |
| ΔfusH | 32.00 | kJ/mol | 415.40 | NIST |
| ΔsubH | [88.30; 103.80] | kJ/mol | [320.50; 393.00] | |
| ΔsubH | 103.80 ± 0.30 | kJ/mol | 320.50 | NIST |
| ΔsubH | 94.40 | kJ/mol | 393.00 | NIST |
| ΔsubH | 88.30 | kJ/mol | 393.00 | NIST |
| ΔvapH | 62.00 | kJ/mol | 468.00 | NIST |
| ΔfusS | [76.44; 77.60] | J/mol×K | [413.79; 415.40] | |
| ΔfusS | 76.44 | J/mol×K | 413.79 | NIST |
| ΔfusS | 76.44 | J/mol×K | 413.79 | NIST |
| ΔfusS | 77.60 | J/mol×K | 413.80 | NIST |
| ΔfusS | 77.60 | J/mol×K | 413.80 | NIST |
| ΔfusS | 77.00 | J/mol×K | 415.40 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [430.99; 587.72] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50856e+01 | |||
| Coefficient B | -4.51226e+03 | |||
| Coefficient C | -1.26067e+02 | |||
| Temperature range, min. | 430.99 | |||
| Temperature range, max. | 587.72 | |||
| Pvap | 1.33 | kPa | 430.99 | Calculated Property |
| Pvap | 2.97 | kPa | 448.40 | Calculated Property |
| Pvap | 6.08 | kPa | 465.82 | Calculated Property |
| Pvap | 11.61 | kPa | 483.23 | Calculated Property |
| Pvap | 20.89 | kPa | 500.65 | Calculated Property |
| Pvap | 35.68 | kPa | 518.06 | Calculated Property |
| Pvap | 58.22 | kPa | 535.48 | Calculated Property |
| Pvap | 91.27 | kPa | 552.89 | Calculated Property |
| Pvap | 138.14 | kPa | 570.31 | Calculated Property |
| Pvap | 202.64 | kPa | 587.72 | Calculated Property |
| Pvap | [0.82; 2774.43] | kPa | [403.80; 772.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.91810e+01 | |||
| Coefficient B | -9.27175e+03 | |||
| Coefficient C | -6.14065e+00 | |||
| Coefficient D | 2.66169e-06 | |||
| Temperature range, min. | 403.80 | |||
| Temperature range, max. | 772.00 | |||
| Pvap | 0.82 | kPa | 403.80 | Calculated Property |
| Pvap | 4.12 | kPa | 444.71 | Calculated Property |
| Pvap | 15.39 | kPa | 485.62 | Calculated Property |
| Pvap | 46.09 | kPa | 526.53 | Calculated Property |
| Pvap | 116.73 | kPa | 567.44 | Calculated Property |
| Pvap | 259.61 | kPa | 608.36 | Calculated Property |
| Pvap | 521.55 | kPa | 649.27 | Calculated Property |
| Pvap | 966.72 | kPa | 690.18 | Calculated Property |
| Pvap | 1680.44 | kPa | 731.09 | Calculated Property |
| Pvap | 2774.43 | kPa | 772.00 | Calculated Property |
Find more compounds similar to 1,4-Benzenedicarboxylic acid, dimethyl ester.
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