| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5363 | Relay (1.0) Calculated Property | |
| ΔcH°solid | [-4983.00; -4951.10] | kJ/mol |
|
| ΔcH°solid | -4951.10 ± 4.90 | kJ/mol | NIST |
| ΔcH°solid | -4956.40 ± 0.80 | kJ/mol | NIST |
| ΔcH°solid | -4957.33 ± 0.88 | kJ/mol | NIST |
| ΔcH°solid | Outlier -4983.00 | kJ/mol | NIST |
| ΔcH°solid | -4965.60 ± 2.10 | kJ/mol | NIST |
| ΔcH°solid | -4959.70 | kJ/mol | NIST |
| ΔfG° | 97.76 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-30.80; -4.30] | kJ/mol |
|
| ΔfH°gas | -30.80 ± 1.60 | kJ/mol | NIST |
| ΔfH°gas | -29.90 ± 1.10 | kJ/mol | NIST |
| ΔfH°gas | -4.30 | kJ/mol | NIST |
| ΔfH°solid | [-122.00; -95.40] | kJ/mol |
|
| ΔfH°solid | -122.00 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | -121.00 ± 1.00 | kJ/mol | NIST |
| ΔfH°solid | -95.40 | kJ/mol | NIST |
| ΔfusH° | 18.50 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [91.10; 91.50] | kJ/mol |
|
| ΔsubH° | 91.20 | kJ/mol | NIST |
| ΔsubH° | 91.17 ± 0.42 | kJ/mol | NIST |
| ΔsubH° | 91.10 | kJ/mol | NIST |
| ΔsubH° | 91.50 ± 3.80 | kJ/mol | NIST |
| ΔsubH° | 91.17 ± 0.42 | kJ/mol | NIST |
| ΔsubH° | 91.10 | kJ/mol | NIST |
| ΔsubH° | 91.50 ± 3.80 | kJ/mol | NIST |
| ΔvapH° | 75.00 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [7.76; 7.78] | eV |
|
| IE | 7.76 ± 0.03 | eV | NIST |
| IE | 7.76 ± 0.03 | eV | NIST |
| IE | 7.78 | eV | NIST |
| log10WS | [-2.22; -2.08] |
|
|
| log10WS | -2.08 | Aq. Solubility Prediction | |
| log10WS | -2.22 | Estimated Solubility | |
| logPoct/wat | 2.545 | Crippen Calculated Property | |
| McVol | 114.410 | ml/mol | McGowan Calculated Property |
| Pc | 4736.62 | kPa | Joback Calculated Property |
| Inp | [258.48; 1525.00] |
|
|
| Inp | 1517.00 | NIST | |
| Inp | 1487.00 | NIST | |
| Inp | 1484.00 | NIST | |
| Inp | 1517.00 | NIST | |
| Inp | 1494.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1517.00 | NIST | |
| Inp | 1473.70 | NIST | |
| Inp | 1494.90 | NIST | |
| Inp | 1516.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1525.00 | NIST | |
| Inp | 1464.00 | NIST | |
| Inp | 1514.00 | NIST | |
| Inp | 1516.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 259.66 | NIST | |
| Inp | 258.48 | NIST | |
| Inp | 258.50 | NIST | |
| Inp | 258.80 | NIST | |
| Inp | 259.66 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1494.00 | NIST | |
| Inp | 1514.00 | NIST | |
| Tboil | [552.20; 561.16] | K |
|
| Tboil | 552.20 | K | NIST |
| Tboil | 553.15 | K | NIST |
| Tboil | 561.16 ± 0.15 | K | NIST |
| Tc | 833.93 | K | Relay (1.0) Calculated Property |
| Tfus | [367.15; 370.54] | K |
|
| Tfus | 367.90 | K | The fusion thermochemistry of self-associated aromatic compounds at 298.15 K studied by solution calorimetry |
| Tfus | Outlier 370.54 | K | Thermodynamic Data for Processing Naphthol with Supercritical Carbon Dioxide |
| Tfus | 368.65 | K | Aq. Solubility Prediction |
| Tfus | 368.02 ± 0.20 | K | NIST |
| Tfus | 367.15 ± 1.50 | K | NIST |
| Tfus | 369.15 | K | NIST |
| Tfus | 369.00 ± 2.00 | K | NIST |
| Tfus | 368.35 ± 0.25 | K | NIST |
| Tfus | 368.50 ± 0.20 | K | NIST |
| Tfus | 369.00 ± 1.50 | K | NIST |
| Tfus | 369.05 ± 0.20 | K | NIST |
| Tfus | 367.15 ± 2.00 | K | NIST |
| Tfus | 367.15 ± 1.50 | K | NIST |
| Ttriple | [368.20; 368.49] | K |
|
| Ttriple | 368.49 | K | Thermodynamic properties of 1-naphthol: Mutual validation of experimental and computational results |
| Ttriple | 368.20 ± 0.30 | K | NIST |
| Ttriple | 368.20 ± 0.30 | K | NIST |
| Vc | 0.397 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | [166.90; 285.00] | J/mol×K | [298.00; 393.00] | |
| Cp,solid | 166.90 | J/mol×K | 298.00 | NIST |
| Cp,solid | 285.00 | J/mol×K | 393.00 | NIST |
| ΔfusH | [23.01; 24.40] | kJ/mol | [368.20; 369.70] | |
| ΔfusH | 23.47 | kJ/mol | 368.20 | NIST |
| ΔfusH | 23.47 | kJ/mol | 368.20 | NIST |
| ΔfusH | 23.47 | kJ/mol | 368.20 | NIST |
| ΔfusH | 23.47 | kJ/mol | 368.20 | NIST |
| ΔfusH | 23.30 | kJ/mol | 368.70 | NIST |
| ΔfusH | 23.01 | kJ/mol | 369.00 | NIST |
| ΔfusH | 23.22 | kJ/mol | 369.00 | NIST |
| ΔfusH | 24.40 | kJ/mol | 369.70 | NIST |
| ΔsubH | [71.50; 93.30] | kJ/mol | [303.50; 561.01] | |
| ΔsubH | 89.10 ± 1.70 | kJ/mol | 303.50 | NIST |
| ΔsubH | 91.20 ± 0.40 | kJ/mol | 304.50 | NIST |
| ΔsubH | 91.20 ± 0.40 | kJ/mol | 304.50 | NIST |
| ΔsubH | 93.30 | kJ/mol | 305.00 | NIST |
| ΔsubH | 84.30 | kJ/mol | 319.00 | NIST |
| ΔsubH | 84.30 | kJ/mol | 319.00 | NIST |
| ΔsubH | 71.50 | kJ/mol | 561.01 | NIST |
| ΔvapH | [58.50; 60.80] | kJ/mol | [477.50; 493.00] | |
| ΔvapH | 58.50 | kJ/mol | 477.50 | NIST |
| ΔvapH | 60.80 | kJ/mol | 493.00 | NIST |
| ΔfusS | [62.90; 63.60] | J/mol×K | [368.20; 369.00] | |
| ΔfusS | 63.60 | J/mol×K | 368.20 | NIST |
| ΔfusS | 63.60 | J/mol×K | 368.20 | NIST |
| ΔfusS | 62.90 | J/mol×K | 369.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [136.25; 348.35] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -8.04700e+01 | |||
| Coefficient B | 1.02580e+00 | |||
| Coefficient C | -9.44480e-04 | |||
| Coefficient D | 3.47500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 136.25 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 179.61 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 215.46 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 244.89 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 269.01 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 288.91 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 305.70 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 320.47 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 334.32 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 348.35 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0019955; 0.0000737] | Pa×s | [368.26; 563.95] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.57230e+01 | |||
| Coefficient B | 3.50068e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 368.26 | |||
| Temperature range, max. | 563.95 | |||
| η | 0.0019955 | Pa×s | 368.26 | Calculated Property |
| η | 0.0011746 | Pa×s | 390.00 | Calculated Property |
| η | 0.0007312 | Pa×s | 411.74 | Calculated Property |
| η | 0.0004773 | Pa×s | 433.49 | Calculated Property |
| η | 0.0003246 | Pa×s | 455.23 | Calculated Property |
| η | 0.0002286 | Pa×s | 476.97 | Calculated Property |
| η | 0.0001660 | Pa×s | 498.72 | Calculated Property |
| η | 0.0001238 | Pa×s | 520.46 | Calculated Property |
| η | 0.0000945 | Pa×s | 542.20 | Calculated Property |
| η | 0.0000737 | Pa×s | 563.95 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.99; 202.63] | kPa | [410.35; 586.46] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39840e+01 | |||
| Coefficient B | -4.01524e+03 | |||
| Coefficient C | -1.23482e+02 | |||
| Temperature range, min. | 410.35 | |||
| Temperature range, max. | 586.46 | |||
| Pvap | 0.99 | kPa | 410.35 | Calculated Property |
| Pvap | 2.41 | kPa | 429.92 | Calculated Property |
| Pvap | 5.30 | kPa | 449.49 | Calculated Property |
| Pvap | 10.64 | kPa | 469.05 | Calculated Property |
| Pvap | 19.84 | kPa | 488.62 | Calculated Property |
| Pvap | 34.71 | kPa | 508.19 | Calculated Property |
| Pvap | 57.52 | kPa | 527.76 | Calculated Property |
| Pvap | 90.98 | kPa | 547.32 | Calculated Property |
| Pvap | 138.20 | kPa | 566.89 | Calculated Property |
| Pvap | 202.63 | kPa | 586.46 | Calculated Property |
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