Property | Value | Unit | Source |
---|---|---|---|
PAff | 861.10 | kJ/mol | NIST |
BasG | 832.60 | kJ/mol | NIST |
ΔcH°solid | [-6058.00; -6052.20] | kJ/mol |
![]() |
ΔcH°solid | -6058.00 ± 4.00 | kJ/mol | NIST |
ΔcH°solid | -6052.20 ± 4.60 | kJ/mol | NIST |
EA | 0.40 ± 0.03 | eV | NIST |
ΔfG° | 360.48 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [258.00; 264.00] | kJ/mol |
![]() |
ΔfH°gas | 263.20 ± 3.70 | kJ/mol | NIST |
ΔfH°gas | 264.00 | kJ/mol | NIST |
ΔfH°gas | 258.00 ± 5.90 | kJ/mol | NIST |
ΔfH°solid | [187.00; 193.00] | kJ/mol |
![]() |
ΔfH°solid | 190.80 ± 3.50 | kJ/mol | NIST |
ΔfH°solid | 193.00 ± 4.00 | kJ/mol | NIST |
ΔfH°solid | 187.00 ± 4.60 | kJ/mol | NIST |
ΔfusH° | 11.73 | kJ/mol | Recomme... |
ΔsubH° | [70.00; 73.00] | kJ/mol |
![]() |
ΔsubH° | 72.50 ± 1.20 | kJ/mol | NIST |
ΔsubH° | 70.00 | kJ/mol | NIST |
ΔsubH° | 73.00 ± 0.30 | kJ/mol | NIST |
ΔsubH° | 73.00 ± 0.40 | kJ/mol | NIST |
ΔsubH° | 71.00 ± 1.00 | kJ/mol | NIST |
ΔsubH° | 71.00 | kJ/mol | NIST |
ΔvapH° | [64.60; 69.10] | kJ/mol |
![]() |
ΔvapH° | 64.60 ± 5.80 | kJ/mol | NIST |
ΔvapH° | 69.10 ± 2.20 | kJ/mol | NIST |
IE | [8.02; 8.22] | eV |
![]() |
IE | 8.12 ± 0.10 | eV | NIST |
IE | 8.22 ± 0.04 | eV | NIST |
IE | 8.02 ± 0.01 | eV | NIST |
log10WS | [-3.96; -3.96] |
![]() |
|
log10WS | -3.96 | Aq. Sol... | |
log10WS | -3.96 | Estimat... | |
logPoct/wat | 3.324 | Crippen Calculated Property | |
McVol | 121.560 | ml/mol | McGowan Calculated Property |
Pc | 3673.09 | kPa | Joback Calculated Property |
Inp | [240.45; 1495.00] |
![]() |
|
Inp | 1424.62 | NIST | |
Inp | 1457.55 | NIST | |
Inp | 1495.00 | NIST | |
Inp | 1460.00 | NIST | |
Inp | 1408.90 | NIST | |
Inp | 1409.00 | NIST | |
Inp | 1456.00 | NIST | |
Inp | 1426.00 | NIST | |
Inp | 1425.03 | NIST | |
Inp | 1413.00 | NIST | |
Inp | 1418.54 | NIST | |
Inp | 1453.37 | NIST | |
Inp | 1470.00 | NIST | |
Inp | 1419.00 | NIST | |
Inp | 1428.00 | NIST | |
Inp | 1470.00 | NIST | |
Inp | 1454.00 | NIST | |
Inp | 1450.70 | NIST | |
Inp | 1453.00 | NIST | |
Inp | 1455.00 | NIST | |
Inp | 1422.00 | NIST | |
Inp | 1447.00 | NIST | |
Inp | 1403.00 | NIST | |
Inp | 1438.00 | NIST | |
Inp | 1460.00 | NIST | |
Inp | 1466.00 | NIST | |
Inp | 1433.00 | NIST | |
Inp | 1434.00 | NIST | |
Inp | 1434.00 | NIST | |
Inp | 1483.00 | NIST | |
Inp | 1445.00 | NIST | |
Inp | 247.80 | NIST | |
Inp | 244.63 | NIST | |
Inp | 247.40 | NIST | |
Inp | 248.47 | NIST | |
Inp | 248.88 | NIST | |
Inp | 248.48 | NIST | |
Inp | 248.29 | NIST | |
Inp | 247.93 | NIST | |
Inp | 245.40 | NIST | |
Inp | 245.40 | NIST | |
Inp | 249.00 | NIST | |
Inp | 249.04 | NIST | |
Inp | 245.83 | NIST | |
Inp | 245.36 | NIST | |
Inp | 249.19 | NIST | |
Inp | 248.90 | NIST | |
Inp | 247.82 | NIST | |
Inp | 244.79 | NIST | |
Inp | 247.65 | NIST | |
Inp | 244.63 | NIST | |
Inp | 248.75 | NIST | |
Inp | 243.59 | NIST | |
Inp | 242.46 | NIST | |
Inp | 246.92 | NIST | |
Inp | 244.63 | NIST | |
Inp | 249.20 | NIST | |
Inp | 248.27 | NIST | |
Inp | 247.65 | NIST | |
Inp | 248.27 | NIST | |
Inp | 249.20 | NIST | |
Inp | 240.45 | NIST | |
Inp | 240.53 | NIST | |
Inp | 244.60 | NIST | |
Inp | 247.40 | NIST | |
Inp | 247.70 | NIST | |
Inp | 247.40 | NIST | |
Inp | 240.52 | NIST | |
Inp | 240.53 | NIST | |
Inp | 244.63 | NIST | |
Inp | 244.63 | NIST | |
Inp | 253.15 | NIST | |
Inp | 249.50 | NIST | |
Inp | 244.00 | NIST | |
Inp | 244.63 | NIST | |
Inp | 247.80 | NIST | |
Inp | 248.48 | NIST | |
Inp | 249.00 | NIST | |
Inp | 248.90 | NIST | |
Inp | 248.75 | NIST | |
Inp | 249.20 | NIST | |
Inp | 240.45 | NIST | |
Inp | 247.40 | NIST | |
Inp | 253.15 | NIST | |
Inp | 1470.00 | NIST | |
Inp | 1422.00 | NIST | |
Inp | 1428.00 | NIST | |
Inp | 1418.54 | NIST | |
Inp | 1460.00 | NIST | |
Inp | 1483.00 | NIST | |
Inp | 1425.03 | NIST | |
I | [249.77; 2193.00] |
![]() |
|
I | 2193.00 | NIST | |
I | 2188.00 | NIST | |
I | 249.77 | NIST | |
Tboil | [543.00; 553.20] | K |
![]() |
Tboil | 553.20 | K | NIST |
Tboil | 543.00 ± 5.00 | K | NIST |
Tc | 779.55 | K | Joback Calculated Property |
Tfus | [362.60; 366.40] | K |
![]() |
Tfus | 364.90 | K | Aq. Sol... |
Tfus | 365.50 ± 0.50 | K | NIST |
Tfus | 362.60 ± 0.20 | K | NIST |
Tfus | 366.40 ± 0.30 | K | NIST |
Tfus | 365.70 ± 2.00 | K | NIST |
Vc | 0.473 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [261.76; 323.61] | J/mol×K | [535.88; 779.55] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 260 270 280 290 300 310 320 600 700 | ||||
Cp,gas | 261.76 | J/mol×K | 535.88 | Joback Calculated Property |
Cp,gas | 274.62 | J/mol×K | 576.49 | Joback Calculated Property |
Cp,gas | 286.28 | J/mol×K | 617.10 | Joback Calculated Property |
Cp,gas | 296.86 | J/mol×K | 657.72 | Joback Calculated Property |
Cp,gas | 306.52 | J/mol×K | 698.33 | Joback Calculated Property |
Cp,gas | 315.39 | J/mol×K | 738.94 | Joback Calculated Property |
Cp,gas | 323.61 | J/mol×K | 779.55 | Joback Calculated Property |
Cp,solid | 166.40 | J/mol×K | 298.00 | NIST |
η | [0.0007329; 0.0012738] | Pa×s | [335.62; 535.88] | ![]() |
T(K) Dynamic viscosity (Pa×s) 7.00e-4 8.00e-4 9.00e-4 1.00e-3 1.10e-3 1.20e-3 1.30e-3 350 400 450 500 | ||||
η | 0.0012738 | Pa×s | 335.62 | Joback Calculated Property |
η | 0.0011143 | Pa×s | 369.00 | Joback Calculated Property |
η | 0.0009967 | Pa×s | 402.37 | Joback Calculated Property |
η | 0.0009068 | Pa×s | 435.75 | Joback Calculated Property |
η | 0.0008362 | Pa×s | 469.13 | Joback Calculated Property |
η | 0.0007794 | Pa×s | 502.50 | Joback Calculated Property |
η | 0.0007329 | Pa×s | 535.88 | Joback Calculated Property |
ΔfusH | [6.94; 10.96] | kJ/mol | [362.00; 362.60] | ![]() |
ΔfusH | 10.96 | kJ/mol | 362.00 | NIST |
ΔfusH | 6.94 | kJ/mol | 362.60 | NIST |
ΔsubH | [71.10; 77.20] | kJ/mol | [280.50; 383.00] | ![]() |
ΔsubH | 73.20 ± 0.50 | kJ/mol | 280.50 | NIST |
ΔsubH | 71.10 ± 1.30 | kJ/mol | 302.00 | NIST |
ΔsubH | 77.20 | kJ/mol | 383.00 | NIST |
Psub | [4.88e-04; 4.14e-03] | kPa | [297.40; 319.70] | ![]() |
T(K) Sublimation pressure (kPa) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 300 310 320 | ||||
Psub | 4.88e-04 | kPa | 297.40 | Vapor P... |
Psub | 5.31e-04 | kPa | 297.60 | Vapor P... |
Psub | 1.05e-03 | kPa | 304.60 | Vapor P... |
Psub | 1.08e-03 | kPa | 304.70 | Vapor P... |
Psub | 1.14e-03 | kPa | 306.70 | Vapor P... |
Psub | 1.82e-03 | kPa | 311.90 | Vapor P... |
Psub | 3.45e-03 | kPa | 314.80 | Vapor P... |
Psub | 3.45e-03 | kPa | 318.50 | Vapor P... |
Psub | 3.47e-03 | kPa | 318.60 | Vapor P... |
Psub | 4.14e-03 | kPa | 319.70 | Vapor P... |
ΔfusS | 19.14 | J/mol×K | 362.60 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 431.00 ± 2.00 | K | 3.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [403.50; 499.38] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.17908e+01 | |||
Coefficient B | -6.76309e+03 | |||
Coefficient C | -8.89840e+01 | |||
Temperature range, min. | 403.50 | |||
Temperature range, max. | 499.38 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 | ||||
Pvap | 1.33 | kPa | 403.50 | Calculated Property |
Pvap | 2.70 | kPa | 414.15 | Calculated Property |
Pvap | 5.22 | kPa | 424.81 | Calculated Property |
Pvap | 9.69 | kPa | 435.46 | Calculated Property |
Pvap | 17.35 | kPa | 446.11 | Calculated Property |
Pvap | 30.02 | kPa | 456.77 | Calculated Property |
Pvap | 50.38 | kPa | 467.42 | Calculated Property |
Pvap | 82.18 | kPa | 478.07 | Calculated Property |
Pvap | 130.61 | kPa | 488.73 | Calculated Property |
Pvap | 202.63 | kPa | 499.38 | Calculated Property |
Find more compounds similar to Acenaphthylene.
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.