Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 97.76 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-30.00; -13.80] | kJ/mol | |
ΔfH°gas | -29.90 ± 1.70 | kJ/mol | NIST |
ΔfH°gas | -30.00 ± 1.10 | kJ/mol | NIST |
ΔfH°gas | -13.80 | kJ/mol | NIST |
ΔfH°solid | [-124.20; -108.00] | kJ/mol | |
ΔfH°solid | -124.10 ± 1.60 | kJ/mol | NIST |
ΔfH°solid | -124.20 ± 1.00 | kJ/mol | NIST |
ΔfH°solid | -108.00 | kJ/mol | NIST |
ΔfusH° | 21.07 | kJ/mol | Phase E... |
ΔsubH° | [78.70; 94.20] | kJ/mol | |
ΔsubH° | 85.50 ± 1.20 | kJ/mol | NIST |
ΔsubH° | 94.20 | kJ/mol | NIST |
ΔsubH° | 94.18 ± 0.50 | kJ/mol | NIST |
ΔsubH° | 94.20 | kJ/mol | NIST |
ΔsubH° | 78.70 ± 0.80 | kJ/mol | NIST |
ΔsubH° | 83.00 ± 3.80 | kJ/mol | NIST |
ΔvapH° | 76.20 | kJ/mol | NIST |
IE | [7.85; 7.90] | eV | |
IE | 7.87 ± 0.02 | eV | NIST |
IE | 7.89 ± 0.06 | eV | NIST |
IE | 7.85 ± 0.05 | eV | NIST |
IE | 7.90 | eV | NIST |
log10WS | [-2.28; -2.16] | ||
log10WS | -2.27 | Aq. Sol... | |
log10WS | -2.28 | Estimat... | |
log10WS | -2.16 | Rytting... | |
logPoct/wat | 2.545 | Crippen Calculated Property | |
McVol | 114.410 | ml/mol | McGowan Calculated Property |
Pc | 4736.62 | kPa | Joback Calculated Property |
Inp | [259.70; 1560.10] | ||
Inp | 1517.00 | NIST | |
Inp | 1531.00 | NIST | |
Inp | 1520.50 | NIST | |
Inp | 1520.10 | NIST | |
Inp | 1514.50 | NIST | |
Inp | 1520.50 | NIST | |
Inp | 1523.80 | NIST | |
Inp | 1560.10 | NIST | |
Inp | 1514.50 | NIST | |
Inp | 1520.50 | NIST | |
Inp | 1523.80 | NIST | |
Inp | 1520.50 | NIST | |
Inp | 1520.10 | NIST | |
Inp | 1525.00 | NIST | |
Inp | 1497.00 | NIST | |
Inp | 1536.00 | NIST | |
Inp | 1524.00 | NIST | |
Inp | 1471.00 | NIST | |
Inp | 1522.00 | NIST | |
Inp | 1525.00 | NIST | |
Inp | Outlier 260.22 | NIST | |
Inp | Outlier 259.70 | NIST | |
Inp | Outlier 260.22 | NIST | |
Inp | Outlier 260.22 | NIST | |
Inp | 1522.00 | NIST | |
Inp | 1520.50 | NIST | |
Inp | 1560.10 | NIST | |
Inp | 1520.10 | NIST | |
Inp | 1517.00 | NIST | |
S°gas | 366.60 ± 3.90 | J/mol×K | NIST |
S°solid,1 bar | 179.00 | J/mol×K | NIST |
Tboil | [558.70; 568.00] | K | |
Tboil | 558.70 | K | NIST |
Tboil | 559.00 ± 0.40 | K | NIST |
Tboil | 568.00 ± 0.30 | K | NIST |
Tc | 805.35 | K | Joback Calculated Property |
Tfus | [390.00; 396.98] | K | |
Tfus | 395.55 | K | Aq. Sol... |
Tfus | 396.98 | K | Thermod... |
Tfus | 395.15 ± 2.00 | K | NIST |
Tfus | 394.00 ± 1.00 | K | NIST |
Tfus | 396.15 ± 1.00 | K | NIST |
Tfus | 394.55 ± 0.20 | K | NIST |
Tfus | 394.65 ± 0.15 | K | NIST |
Tfus | Outlier 390.00 ± 1.50 | K | NIST |
Tfus | 393.00 ± 3.00 | K | NIST |
Tfus | 395.25 ± 0.20 | K | NIST |
Tfus | 394.00 ± 0.30 | K | NIST |
Ttriple | 393.80 ± 1.25 | K | NIST |
Vc | 0.376 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [257.18; 314.59] | J/mol×K | [554.48; 805.35] | |
Cp,gas | 257.18 | J/mol×K | 554.48 | Joback Calculated Property |
Cp,gas | 269.06 | J/mol×K | 596.29 | Joback Calculated Property |
Cp,gas | 279.81 | J/mol×K | 638.10 | Joback Calculated Property |
Cp,gas | 289.59 | J/mol×K | 679.91 | Joback Calculated Property |
Cp,gas | 298.55 | J/mol×K | 721.72 | Joback Calculated Property |
Cp,gas | 306.83 | J/mol×K | 763.54 | Joback Calculated Property |
Cp,gas | 314.59 | J/mol×K | 805.35 | Joback Calculated Property |
Cp,solid | 172.80 | J/mol×K | 298.00 | NIST |
η | [0.0000819; 0.0017549] | Pa×s | [373.30; 554.48] | |
η | 0.0017549 | Pa×s | 373.30 | Joback Calculated Property |
η | 0.0008699 | Pa×s | 403.50 | Joback Calculated Property |
η | 0.0004755 | Pa×s | 433.69 | Joback Calculated Property |
η | 0.0002811 | Pa×s | 463.89 | Joback Calculated Property |
η | 0.0001773 | Pa×s | 494.09 | Joback Calculated Property |
η | 0.0001179 | Pa×s | 524.28 | Joback Calculated Property |
η | 0.0000819 | Pa×s | 554.48 | Joback Calculated Property |
ΔfusH | [18.79; 20.90] | kJ/mol | [388.00; 393.60] | |
ΔfusH | 20.90 | kJ/mol | 388.00 | NIST |
ΔfusH | 18.79 | kJ/mol | 393.60 | NIST |
ΔfusH | 18.79 | kJ/mol | 393.60 | NIST |
ΔsubH | [68.20; 97.80] | kJ/mol | [283.00; 567.85] | |
ΔsubH | 78.66 ± 0.84 | kJ/mol | 283.00 | NIST |
ΔsubH | 87.40 ± 2.50 | kJ/mol | 300.50 | NIST |
ΔsubH | 97.80 | kJ/mol | 305.00 | NIST |
ΔsubH | 94.20 ± 0.50 | kJ/mol | 314.00 | NIST |
ΔsubH | 87.80 | kJ/mol | 323.00 | NIST |
ΔsubH | 68.20 | kJ/mol | 567.85 | NIST |
ΔvapH | [59.70; 61.80] | kJ/mol | [481.00; 493.00] | |
ΔvapH | 59.70 | kJ/mol | 481.00 | NIST |
ΔvapH | 59.70 | kJ/mol | 489.00 | NIST |
ΔvapH | 61.80 | kJ/mol | 493.00 | NIST |
ΔfusS | 55.90 | J/mol×K | 393.60 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.00; 202.65] | kPa | [413.85; 591.27] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.59776e+01 | |||
Coefficient B | -5.69302e+03 | |||
Coefficient C | -5.75200e+01 | |||
Temperature range, min. | 413.85 | |||
Temperature range, max. | 591.27 | |||
Pvap | 1.00 | kPa | 413.85 | Calculated Property |
Pvap | 2.31 | kPa | 433.56 | Calculated Property |
Pvap | 4.92 | kPa | 453.28 | Calculated Property |
Pvap | 9.73 | kPa | 472.99 | Calculated Property |
Pvap | 18.10 | kPa | 492.70 | Calculated Property |
Pvap | 31.90 | kPa | 512.42 | Calculated Property |
Pvap | 53.65 | kPa | 532.13 | Calculated Property |
Pvap | 86.56 | kPa | 551.84 | Calculated Property |
Pvap | 134.62 | kPa | 571.56 | Calculated Property |
Pvap | 202.65 | kPa | 591.27 | Calculated Property |
Find more compounds similar to 2-Naphthalenol.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.