Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -6226.52 | kJ/mol | NIST |
ΔfG° | 106.42 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -128.77 | kJ/mol | Joback Calculated Property |
ΔfusH° | 9.53 | kJ/mol | Joback Calculated Property |
ΔvapH° | 38.37 | kJ/mol | Joback Calculated Property |
IE | [9.14; 9.35] | eV |
![]() |
IE | 9.14 | eV | NIST |
IE | 9.35 | eV | NIST |
log10WS | -5.19 | Estimat... | |
logPoct/wat | 3.367 | Crippen Calculated Property | |
McVol | 130.040 | ml/mol | McGowan Calculated Property |
Pc | 2080.00 ± 151.99 | kPa | NIST |
Inp | [173.01; 1089.00] |
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|
Inp | 1042.00 | NIST | |
Inp | 1054.00 | NIST | |
Inp | 1066.00 | NIST | |
Inp | 1063.00 | NIST | |
Inp | 1056.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | 1055.00 | NIST | |
Inp | 1054.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1064.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | Outlier 173.01 | NIST | |
Inp | Outlier 173.31 | NIST | |
Inp | 1055.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | Outlier 173.01 | NIST | |
S°liquid | 265.01 | J/mol×K | NIST |
Tboil | [445.00; 465.00] | K |
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Tboil | 464.25 | K | Excess ... |
Tboil | 463.20 | K | NIST |
Tboil | 465.00 ± 5.00 | K | NIST |
Tboil | 465.00 ± 2.00 | K | NIST |
Tboil | Outlier 445.00 ± 10.00 | K | NIST |
Tboil | 461.00 ± 6.00 | K | NIST |
Tc | 645.00 ± 2.00 | K | NIST |
Tfus | 149.00 ± 2.50 | K | NIST |
Vc | 0.477 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [286.16; 401.24] | J/mol×K | [458.76; 680.81] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 280 300 320 340 360 380 400 500 550 600 650 | ||||
Cp,gas | 286.16 | J/mol×K | 458.76 | Joback Calculated Property |
Cp,gas | 308.56 | J/mol×K | 495.77 | Joback Calculated Property |
Cp,gas | 329.59 | J/mol×K | 532.78 | Joback Calculated Property |
Cp,gas | 349.32 | J/mol×K | 569.78 | Joback Calculated Property |
Cp,gas | 367.80 | J/mol×K | 606.79 | Joback Calculated Property |
Cp,gas | 385.09 | J/mol×K | 643.80 | Joback Calculated Property |
Cp,gas | 401.24 | J/mol×K | 680.81 | Joback Calculated Property |
Cp,liquid | [219.20; 251.00] | J/mol×K | [298.00; 313.00] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 220 225 230 235 240 245 250 300 305 310 | ||||
Cp,liquid | 233.51 | J/mol×K | 298.00 | NIST |
Cp,liquid | 232.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 232.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 232.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 232.08 | J/mol×K | 298.15 | NIST |
Cp,liquid | 220.06 | J/mol×K | 298.15 | NIST |
Cp,liquid | 219.20 | J/mol×K | 311.00 | NIST |
Cp,liquid | 251.00 | J/mol×K | 313.00 | NIST |
η | [0.0004040; 0.0046703] | Pa×s | [224.26; 458.76] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 400 | ||||
η | 0.0046703 | Pa×s | 224.26 | Joback Calculated Property |
η | 0.0022946 | Pa×s | 263.34 | Joback Calculated Property |
η | 0.0013547 | Pa×s | 302.43 | Joback Calculated Property |
η | 0.0009023 | Pa×s | 341.51 | Joback Calculated Property |
η | 0.0006533 | Pa×s | 380.59 | Joback Calculated Property |
η | 0.0005024 | Pa×s | 419.68 | Joback Calculated Property |
η | 0.0004040 | Pa×s | 458.76 | Joback Calculated Property |
ΔfusH | [2.21; 14.41] | kJ/mol | [230.10; 242.78] | ![]() |
ΔfusH | 2.21 | kJ/mol | 230.10 | NIST |
ΔfusH | 14.41 | kJ/mol | 242.78 | NIST |
ρl | [826.61; 880.46] | kg/m3 | [293.15; 363.15] | ![]() |
T(K) Liquid Density (kg/m3) 830 840 850 860 870 880 300 320 340 360 | ||||
ρl | 880.46 | kg/m3 | 293.15 | Density... |
ρl | 876.72 | kg/m3 | 298.15 | Density... |
ρl | 872.96 | kg/m3 | 303.15 | Density... |
ρl | 865.43 | kg/m3 | 313.15 | Density... |
ρl | 857.01 | kg/m3 | 323.15 | Density... |
ρl | 849.45 | kg/m3 | 333.15 | Density... |
ρl | 841.87 | kg/m3 | 343.15 | Density... |
ρl | 834.26 | kg/m3 | 353.15 | Density... |
ρl | 826.61 | kg/m3 | 363.15 | Density... |
ΔfusS | [9.60; 59.37] | J/mol×K | [230.10; 242.78] | ![]() |
ΔfusS | 9.60 | J/mol×K | 230.10 | NIST |
ΔfusS | 59.37 | J/mol×K | 242.78 | NIST |
Find more compounds similar to Naphthalene, decahydro-.
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