Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -13112.40 ± 2.90 | kJ/mol | NIST |
ΔfG° | 689.68 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 478.30 ± 7.40 | kJ/mol | NIST |
ΔfH°solid | 308.70 ± 4.50 | kJ/mol | NIST |
ΔfusH° | 38.09 | kJ/mol | Joback Calculated Property |
ΔsubH° | 169.60 ± 5.90 | kJ/mol | NIST |
ΔvapH° | 85.56 | kJ/mol | Joback Calculated Property |
log10WS | -10.29 | Crippen Calculated Property | |
logPoct/wat | 7.327 | Crippen Calculated Property | |
McVol | 267.000 | ml/mol | McGowan Calculated Property |
Pc | 1930.44 | kPa | Joback Calculated Property |
Inp | [484.33; 3000.00] |
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Inp | 3000.00 | NIST | |
Inp | 484.33 | NIST | |
Inp | 484.33 | NIST | |
Inp | 3000.00 | NIST | |
Tboil | 927.22 | K | Joback Calculated Property |
Tc | 1207.03 | K | Joback Calculated Property |
Tfus | 565.00 | K | Joback Calculated Property |
Vc | 1.012 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [789.72; 878.48] | J/mol×K | [927.22; 1207.03] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 800 820 840 860 880 1000 1100 1200 | ||||
Cp,gas | 789.72 | J/mol×K | 927.22 | Joback Calculated Property |
Cp,gas | 805.81 | J/mol×K | 973.85 | Joback Calculated Property |
Cp,gas | 821.02 | J/mol×K | 1020.49 | Joback Calculated Property |
Cp,gas | 835.60 | J/mol×K | 1067.12 | Joback Calculated Property |
Cp,gas | 849.86 | J/mol×K | 1113.76 | Joback Calculated Property |
Cp,gas | 864.05 | J/mol×K | 1160.39 | Joback Calculated Property |
Cp,gas | 878.48 | J/mol×K | 1207.03 | Joback Calculated Property |
η | [0.0002105; 0.0009054] | Pa×s | [565.00; 927.22] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-4 3.00e-4 4.00e-4 5.00e-4 6.00e-4 7.00e-4 8.00e-4 9.00e-4 600 700 800 900 | ||||
η | 0.0009054 | Pa×s | 565.00 | Joback Calculated Property |
η | 0.0006313 | Pa×s | 625.37 | Joback Calculated Property |
η | 0.0004691 | Pa×s | 685.74 | Joback Calculated Property |
η | 0.0003657 | Pa×s | 746.11 | Joback Calculated Property |
η | 0.0002959 | Pa×s | 806.48 | Joback Calculated Property |
η | 0.0002466 | Pa×s | 866.85 | Joback Calculated Property |
η | 0.0002105 | Pa×s | 927.22 | Joback Calculated Property |
ΔsubH | [134.00; 157.00] | kJ/mol | [293.00; 491.50] | ![]() |
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 135 140 145 150 155 300 350 400 450 | ||||
ΔsubH | 134.00 | kJ/mol | 293.00 | NIST |
ΔsubH | 137.50 | kJ/mol | 383.00 | NIST |
ΔsubH | 141.00 | kJ/mol | 393.00 | NIST |
ΔsubH | 143.60 | kJ/mol | 413.00 | NIST |
ΔsubH | 157.00 ± 4.20 | kJ/mol | 481.00 | NIST |
ΔsubH | 156.90 ± 4.20 | kJ/mol | 491.50 | NIST |
ΔvapH | 102.70 | kJ/mol | 398.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [547.39; 701.63] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.58079e+01 | |||
Coefficient B | -1.60597e+04 | |||
Coefficient C | 8.19030e+01 | |||
Temperature range, min. | 547.39 | |||
Temperature range, max. | 701.63 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 550 600 650 700 | ||||
Pvap | 1.33 | kPa | 547.39 | Calculated Property |
Pvap | 2.62 | kPa | 564.53 | Calculated Property |
Pvap | 4.98 | kPa | 581.67 | Calculated Property |
Pvap | 9.16 | kPa | 598.80 | Calculated Property |
Pvap | 16.36 | kPa | 615.94 | Calculated Property |
Pvap | 28.39 | kPa | 633.08 | Calculated Property |
Pvap | 48.04 | kPa | 650.22 | Calculated Property |
Pvap | 79.34 | kPa | 667.35 | Calculated Property |
Pvap | 128.13 | kPa | 684.49 | Calculated Property |
Pvap | 202.63 | kPa | 701.63 | Calculated Property |
Find more compounds similar to Anthracene, 9,10-diphenyl-.
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