| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4430 | KDB | |
| EA | 0.25 ± 0.08 | eV | NIST |
| ΔfG° | 249.96 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 94.57 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 10.60 | kJ/mol | Solid-Liquid Equilibria of Binary Mixtures of Dimethylnaphthalene Isomers |
| ΔvapH° | 66.85 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [7.78; 7.82] | eV |
|
| IE | 7.78 ± 0.03 | eV | NIST |
| IE | 7.82 ± 0.03 | eV | NIST |
| log10WS | [-4.14; -4.14] |
|
|
| log10WS | -4.14 | Aq. Solubility Prediction | |
| log10WS | -4.14 | Estimated Solubility | |
| logPoct/wat | 3.457 | Crippen Calculated Property | |
| McVol | 136.720 | ml/mol | McGowan Calculated Property |
| Pc | 3010.00 | kPa | KDB |
| Inp | [243.02; 1447.00] |
|
|
| Inp | 1410.60 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1439.00 | NIST | |
| Inp | 1442.80 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1431.00 | NIST | |
| Inp | 1425.90 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1424.20 | NIST | |
| Inp | 1436.30 | NIST | |
| Inp | 1443.20 | NIST | |
| Inp | 1424.20 | NIST | |
| Inp | 1436.30 | NIST | |
| Inp | 1443.20 | NIST | |
| Inp | 1415.00 | NIST | |
| Inp | 1447.00 | NIST | |
| Inp | 1399.47 | NIST | |
| Inp | 1411.24 | NIST | |
| Inp | 1419.17 | NIST | |
| Inp | 1436.73 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1435.00 | NIST | |
| Inp | 1426.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1415.00 | NIST | |
| Inp | 1420.00 | NIST | |
| Inp | 1443.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 246.51 | NIST | |
| Inp | 243.57 | NIST | |
| Inp | 246.55 | NIST | |
| Inp | 246.42 | NIST | |
| Inp | 243.02 | NIST | |
| Inp | 245.70 | NIST | |
| Inp | 246.20 | NIST | |
| Inp | 247.15 | NIST | |
| Inp | 246.03 | NIST | |
| Inp | 243.57 | NIST | |
| Inp | 245.40 | NIST | |
| Inp | 246.50 | NIST | |
| Inp | 243.60 | NIST | |
| Inp | 247.02 | NIST | |
| Inp | 243.98 | NIST | |
| Inp | 246.00 | NIST | |
| Inp | 246.30 | NIST | |
| Inp | 1443.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 246.51 | NIST | |
| Inp | 245.70 | NIST | |
| Inp | 1410.60 | NIST | |
| Inp | 1442.80 | NIST | |
| Inp | 1397.00 | NIST | |
| I | [2041.00; 2041.00] |
|
|
| I | 2041.00 | NIST | |
| I | 2041.00 | NIST | |
| Tboil | [536.00; 541.60] | K |
|
| Tboil | 538.30 | K | Critical properties of some alkylnaphthalenes |
| Tboil | 540.50 | K | KDB |
| Tboil | 541.60 ± 1.00 | K | NIST |
| Tboil | 536.00 ± 4.00 | K | NIST |
| Tboil | 539.00 ± 5.00 | K | NIST |
| Tboil | 537.00 ± 4.00 | K | NIST |
| Tc | 776.80 | K | KDB |
| Tfus | [253.00; 289.45] | K |
|
| Tfus | 281.00 | K | KDB |
| Tfus | 280.75 | K | Aq. Solubility Prediction |
| Tfus | 279.90 ± 0.20 | K | NIST |
| Tfus | 281.00 ± 0.15 | K | NIST |
| Tfus | 281.02 ± 0.06 | K | NIST |
| Tfus | 289.45 ± 0.70 | K | NIST |
| Tfus | 280.73 ± 0.15 | K | NIST |
| Tfus | 280.81 ± 0.06 | K | NIST |
| Tfus | 279.00 ± 4.00 | K | NIST |
| Tfus | 271.00 ± 5.00 | K | NIST |
| Tfus | 279.20 ± 5.00 | K | NIST |
| Tfus | 289.00 ± 6.00 | K | NIST |
| Tfus | 289.00 ± 6.00 | K | NIST |
| Tfus | Outlier 253.00 ± 30.00 | K | NIST |
| Vc | 0.521 | m3/kmol | KDB |
| Zc | 0.2430380 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [296.31; 371.48] | J/mol×K | [529.58; 761.14] | |
| Cp,gas | 296.31 | J/mol×K | 529.58 | Joback Calculated Property |
| Cp,gas | 311.16 | J/mol×K | 568.17 | Joback Calculated Property |
| Cp,gas | 325.00 | J/mol×K | 606.77 | Joback Calculated Property |
| Cp,gas | 337.89 | J/mol×K | 645.36 | Joback Calculated Property |
| Cp,gas | 349.89 | J/mol×K | 683.95 | Joback Calculated Property |
| Cp,gas | 361.06 | J/mol×K | 722.55 | Joback Calculated Property |
| Cp,gas | 371.48 | J/mol×K | 761.14 | Joback Calculated Property |
| η | [0.0002960; 0.0012561] | Pa×s | [309.16; 529.58] | |
| η | 0.0012561 | Pa×s | 309.16 | Joback Calculated Property |
| η | 0.0008686 | Pa×s | 345.90 | Joback Calculated Property |
| η | 0.0006448 | Pa×s | 382.63 | Joback Calculated Property |
| η | 0.0005043 | Pa×s | 419.37 | Joback Calculated Property |
| η | 0.0004103 | Pa×s | 456.11 | Joback Calculated Property |
| η | 0.0003443 | Pa×s | 492.84 | Joback Calculated Property |
| η | 0.0002960 | Pa×s | 529.58 | Joback Calculated Property |
| ΔfusH | [10.60; 10.60] | kJ/mol | [279.20; 279.90] | |
| ΔfusH | 10.60 | kJ/mol | 279.20 | NIST |
| ΔfusH | 10.60 | kJ/mol | 279.90 | NIST |
| ΔfusH | 10.60 | kJ/mol | 279.90 | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 536.20 | K | 100.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [392.66; 577.39] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53305e+01 | |||
| Coefficient B | -5.54175e+03 | |||
| Coefficient C | -2.42690e+01 | |||
| Temperature range, min. | 392.66 | |||
| Temperature range, max. | 577.39 | |||
| Pvap | 1.33 | kPa | 392.66 | Calculated Property |
| Pvap | 2.95 | kPa | 413.19 | Calculated Property |
| Pvap | 6.02 | kPa | 433.71 | Calculated Property |
| Pvap | 11.49 | kPa | 454.24 | Calculated Property |
| Pvap | 20.68 | kPa | 474.76 | Calculated Property |
| Pvap | 35.34 | kPa | 495.29 | Calculated Property |
| Pvap | 57.76 | kPa | 515.81 | Calculated Property |
| Pvap | 90.77 | kPa | 536.34 | Calculated Property |
| Pvap | 137.74 | kPa | 556.86 | Calculated Property |
| Pvap | 202.65 | kPa | 577.39 | Calculated Property |
| Pvap | [6.16e-04; 2974.77] | kPa | [283.15; 776.78] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.54930e+01 | |||
| Coefficient B | -1.06126e+04 | |||
| Coefficient C | -9.85429e+00 | |||
| Coefficient D | 2.89872e-06 | |||
| Temperature range, min. | 283.15 | |||
| Temperature range, max. | 776.78 | |||
| Pvap | 6.16e-04 | kPa | 283.15 | Calculated Property |
| Pvap | 0.05 | kPa | 338.00 | Calculated Property |
| Pvap | 1.06 | kPa | 392.85 | Calculated Property |
| Pvap | 9.18 | kPa | 447.69 | Calculated Property |
| Pvap | 45.46 | kPa | 502.54 | Calculated Property |
| Pvap | 154.86 | kPa | 557.39 | Calculated Property |
| Pvap | 407.19 | kPa | 612.24 | Calculated Property |
| Pvap | 891.06 | kPa | 667.08 | Calculated Property |
| Pvap | 1708.32 | kPa | 721.93 | Calculated Property |
| Pvap | 2974.77 | kPa | 776.78 | Calculated Property |
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