- InChI
- InChI=1S/C14H8O2/c15-13-9-5-1-2-6-10(9)14(16)12-8-4-3-7-11(12)13/h1-8H
- InChI Key
- RZVHIXYEVGDQDX-UHFFFAOYSA-N
- Formula
- C14H8O2
- SMILES
- O=C1c2ccccc2C(=O)c2ccccc21
- Molecular Weight1
- 208.21
- CAS
- 84-65-1
- Other Names
-
- 9,10(9H,10H)-anthracenedione
- 9,10-Anthrachinon
- 9,10-Anthraquinone
- 9,10-Dioxoanthracene
- 9,10-anthracenequinone
- Anthracene, 9,10-dihydro-9,10-dioxo-
- Anthracene-9,10-quinone
- Anthradione
- Anthraquinone
- Corbit
- Hoelite
- Morkit
- NSC 7957
- anthracene-9,10-dione
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Psub : Sublimation pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-6468.90; -6444.52] | kJ/mol |
|
| ΔcH°solid | -6464.00 ± 2.10 | kJ/mol | NIST |
| ΔcH°solid | -6444.52 | kJ/mol | NIST |
| ΔcH°solid | -6468.90 | kJ/mol | NIST |
| ΔcH°solid | -6462.20 | kJ/mol | NIST |
| EA | [1.15; 1.59] | eV |
|
| EA | 1.59 ± 0.06 | eV | NIST |
| EA | 1.15 ± 0.10 | eV | NIST |
| ΔfG° | 107.94 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -75.70 ± 2.90 | kJ/mol | NIST |
| ΔfH°solid | -188.50 ± 2.80 | kJ/mol | NIST |
| ΔfusH° | 36.30 | kJ/mol | Thermod... |
| ΔvapH° | 61.18 | kJ/mol | Joback Calculated Property |
| IE | [9.00; 9.40] | eV |
|
| IE | 9.25 ± 0.12 | eV | NIST |
| IE | Outlier 9.00 | eV | NIST |
| IE | 9.25 | eV | NIST |
| IE | 9.40 ± 0.08 | eV | NIST |
| IE | 9.25 ± 0.03 | eV | NIST |
| IE | 9.30 | eV | NIST |
| log10WS | [-5.19; -5.19] |
|
|
| log10WS | -5.19 | Aq. Sol... | |
| log10WS | -5.19 | Estimat... | |
| logPoct/wat | 2.462 | Crippen Calculated Property | |
| McVol | 152.880 | ml/mol | McGowan Calculated Property |
| Pc | 3372.36 | kPa | Joback Calculated Property |
| Inp | [329.00; 1950.00] |
|
|
| Inp | 1898.00 | NIST | |
| Inp | 1950.00 | NIST | |
| Inp | 1880.00 | NIST | |
| Inp | 1904.00 | NIST | |
| Inp | 1921.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 331.22 | NIST | |
| Inp | 330.26 | NIST | |
| Inp | 330.50 | NIST | |
| Inp | 330.70 | NIST | |
| Inp | 331.38 | NIST | |
| Inp | 331.09 | NIST | |
| Inp | 329.60 | NIST | |
| Inp | 330.00 | NIST | |
| Inp | 331.32 | NIST | |
| Inp | 331.91 | NIST | |
| Inp | 333.00 | NIST | |
| Inp | 329.00 | NIST | |
| Inp | 330.90 | NIST | |
| Inp | 337.40 | NIST | |
| Inp | 331.22 | NIST | |
| Inp | 331.09 | NIST | |
| Tboil | [650.00; 653.20] | K |
|
| Tboil | 653.20 | K | NIST |
| Tboil | 650.00 ± 0.30 | K | NIST |
| Tc | 1001.05 | K | Joback Calculated Property |
| Tfus | [555.00; 558.35] | K |
|
| Tfus | 557.96 ± 0.20 | K | NIST |
| Tfus | 558.15 ± 1.00 | K | NIST |
| Tfus | 558.35 ± 0.40 | K | NIST |
| Tfus | 557.78 ± 0.30 | K | NIST |
| Tfus | 557.85 ± 0.20 | K | NIST |
| Tfus | 558.07 ± 0.20 | K | NIST |
| Tfus | 557.75 ± 0.30 | K | NIST |
| Tfus | 557.97 ± 0.35 | K | NIST |
| Tfus | 557.75 ± 0.50 | K | NIST |
| Tfus | Outlier 555.00 ± 1.00 | K | NIST |
| Vc | 0.584 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [401.54; 468.21] | J/mol×K | [725.82; 1001.05] |
|
| Cp,gas | 401.54 | J/mol×K | 725.82 | Joback Calculated Property |
| Cp,gas | 415.60 | J/mol×K | 771.69 | Joback Calculated Property |
| Cp,gas | 428.41 | J/mol×K | 817.56 | Joback Calculated Property |
| Cp,gas | 440.03 | J/mol×K | 863.44 | Joback Calculated Property |
| Cp,gas | 450.50 | J/mol×K | 909.31 | Joback Calculated Property |
| Cp,gas | 459.88 | J/mol×K | 955.18 | Joback Calculated Property |
| Cp,gas | 468.21 | J/mol×K | 1001.05 | Joback Calculated Property |
| Cp,solid | 240.20 | J/mol×K | 298.15 | NIST |
| ΔfusH | [32.57; 32.57] | kJ/mol | [555.00; 558.00] |
|
| ΔfusH | 32.57 | kJ/mol | 555.00 | NIST |
| ΔfusH | 32.57 | kJ/mol | 555.00 | NIST |
| ΔfusH | 32.57 | kJ/mol | 558.00 | NIST |
| ΔsubH | [98.30; 127.00] | kJ/mol | [367.00; 530.00] |
|
| ΔsubH | 104.60 | kJ/mol | 367.00 | NIST |
| ΔsubH | 126.40 | kJ/mol | 373.00 | NIST |
| ΔsubH | 98.30 | kJ/mol | 413.00 | NIST |
| ΔsubH | 107.50 ± 0.80 | kJ/mol | 434.00 | NIST |
| ΔsubH | 107.90 ± 0.80 | kJ/mol | 434.00 | NIST |
| ΔsubH | 127.00 ± 3.00 | kJ/mol | 530.00 | NIST |
| ΔvapH | 64.30 | kJ/mol | 609.50 | NIST |
| Psub | [4.49e-06; 0.49] | kPa | [346.00; 478.50] |
|
| Psub | 4.49e-06 | kPa | 346.00 | Vapor p... |
| Psub | 2.09e-05 | kPa | 359.90 | Vapor p... |
| Psub | 2.20e-05 | kPa | 360.90 | Vapor p... |
| Psub | 2.52e-05 | kPa | 362.70 | Vapor p... |
| Psub | 4.10e-05 | kPa | 367.40 | Vapor p... |
| Psub | 5.42e-05 | kPa | 369.90 | Vapor p... |
| Psub | 1.19e-04 | kPa | 377.60 | Vapor p... |
| Psub | 1.44e-04 | kPa | 379.20 | Vapor p... |
| Psub | 1.49e-04 | kPa | 380.10 | Vapor p... |
| Psub | 2.67e-04 | kPa | 385.40 | Vapor p... |
| Psub | 2.63e-04 | kPa | 385.80 | Vapor p... |
| Psub | 3.05e-04 | kPa | 386.80 | Vapor p... |
| Psub | 4.93e-04 | kPa | 392.70 | Vapor p... |
| Psub | 4.94e-04 | kPa | 392.80 | Vapor p... |
| Psub | 5.19e-04 | kPa | 393.40 | Vapor p... |
| Psub | 8.72e-04 | kPa | 399.20 | Vapor p... |
| Psub | 9.48e-04 | kPa | 399.90 | Vapor p... |
| Psub | 0.01 | kPa | 422.80 | Fast sc... |
| Psub | 0.02 | kPa | 427.70 | Fast sc... |
| Psub | 0.02 | kPa | 429.20 | Fast sc... |
| Psub | 0.02 | kPa | 432.20 | Fast sc... |
| Psub | 0.03 | kPa | 437.40 | Fast sc... |
| Psub | 0.04 | kPa | 439.10 | Fast sc... |
| Psub | 0.04 | kPa | 441.60 | Fast sc... |
| Psub | 0.05 | kPa | 447.20 | Fast sc... |
| Psub | 0.07 | kPa | 448.90 | Fast sc... |
| Psub | 0.08 | kPa | 451.00 | Fast sc... |
| Psub | 0.10 | kPa | 457.00 | Fast sc... |
| Psub | 0.15 | kPa | 458.80 | Fast sc... |
| Psub | 0.17 | kPa | 460.40 | Fast sc... |
| Psub | 0.20 | kPa | 466.70 | Fast sc... |
| Psub | 0.27 | kPa | 468.70 | Fast sc... |
| Psub | 0.25 | kPa | 469.80 | Fast sc... |
| Psub | 0.32 | kPa | 476.50 | Fast sc... |
| Psub | 0.49 | kPa | 478.50 | Fast sc... |
| ΔfusS | 58.70 | J/mol×K | 555.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [481.92; 691.90] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.75139e+01 | |||
| Coefficient B | -8.78545e+03 | |||
| Coefficient C | 2.80780e+01 | |||
| Temperature range, min. | 481.92 | |||
| Temperature range, max. | 691.90 | |||
| Pvap | 1.33 | kPa | 481.92 | Calculated Property |
| Pvap | 2.83 | kPa | 505.25 | Calculated Property |
| Pvap | 5.65 | kPa | 528.58 | Calculated Property |
| Pvap | 10.66 | kPa | 551.91 | Calculated Property |
| Pvap | 19.15 | kPa | 575.24 | Calculated Property |
| Pvap | 32.93 | kPa | 598.58 | Calculated Property |
| Pvap | 54.46 | kPa | 621.91 | Calculated Property |
| Pvap | 86.99 | kPa | 645.24 | Calculated Property |
| Pvap | 134.67 | kPa | 668.57 | Calculated Property |
| Pvap | 202.65 | kPa | 691.90 | Calculated Property |
Similar Compounds
Find more compounds similar to 9,10-Anthracenedione.
Mixtures
Sources
- Crippen Method
- Vapor pressures and sublimation enthalpies of seven heteroatomic aromatic hydrocarbons measured using the Knudsen effusion technique
- Fast scanning calorimetry: Sublimation thermodynamics of low volatile and thermally unstable compounds
- Thermodynamic Study on the Sublimation of Anthracene-Like Compounds
- Solubilities of Oxygenated Aromatic Solids in Pressurized Hot Water
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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