- InChI
- InChI=1S/C13H10O/c14-13(11-7-3-1-4-8-11)12-9-5-2-6-10-12/h1-10H
- InChI Key
- RWCCWEUUXYIKHB-UHFFFAOYSA-N
- Formula
- C13H10O
- SMILES
- O=C(c1ccccc1)c1ccccc1
- Molecular Weight1
- 182.22
- CAS
- 119-61-9
- Other Names
-
- 1-Benzophenone
- ALPHA-OXODIPHENYLMETHANE
- Adjutan 6016
- Benzene, benzoyl-
- Benzoylbenzene
- Cinnarizine M (benzophenone)
- Cyclizine M (Benzophenone)
- DIPHENYL METHANONE
- Diphenyl ketone
- Diphenyl-methanon
- Diphenylmethanone
- Kayacure BP
- Ketone, diphenyl
- Methanone, diphenyl-
- NSC 8077
- PHENYL KETONE
- alpha-Oxoditane
- «alpha»-Oxodiphenylmethane
- «alpha»-Oxoditane
- «alpha»-Oxodiphenylmethane
- «alpha»-Oxoditane
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- ρc : Critical density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 |
|---|---|---|---|
| PAff | 882.30 | kJ/mol | NIST |
| BasG | 852.50 | kJ/mol | NIST |
| ΔcH°solid | [-6512.40; -6498.00] | kJ/mol |
|
| ΔcH°solid | -6510.30 ± 2.10 | kJ/mol | NIST |
| ΔcH°solid | -6510.00 ± 2.00 | kJ/mol | NIST |
| ΔcH°solid | -6512.00 | kJ/mol | NIST |
| ΔcH°solid | -6512.40 ± 3.20 | kJ/mol | NIST |
| ΔcH°solid | -6504.00 | kJ/mol | NIST |
| ΔcH°solid | -6498.00 | kJ/mol | NIST |
| EA | [0.62; 1.11] | eV |
|
| EA | 0.62 ± 0.10 | eV | NIST |
| EA | 1.11 ± 0.04 | eV | NIST |
| EA | 0.66 ± 0.09 | eV | NIST |
| EA | 0.69 ± 0.05 | eV | NIST |
| EA | 0.64 ± 0.05 | eV | NIST |
| ΔfG° | 154.48 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 49.90 ± 3.00 | kJ/mol | NIST |
| ΔfH°solid | [-50.84; -32.30] | kJ/mol |
|
| ΔfH°solid | -34.00 | kJ/mol | NIST |
| ΔfH°solid | -33.00 | kJ/mol | NIST |
| ΔfH°solid | -32.30 ± 3.30 | kJ/mol | NIST |
| ΔfH°solid | -50.84 | kJ/mol | NIST |
| ΔfusH° | 19.11 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 94.98 | kJ/mol | NIST |
| IE | [9.05; 9.50] | eV |
|
| IE | 9.08 ± 0.04 | eV | NIST |
| IE | 9.40 ± 0.10 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.50 ± 0.10 | eV | NIST |
| IE | 9.50 ± 0.10 | eV | NIST |
| IE | 9.46 | eV | NIST |
| IE | 9.14 ± 0.03 | eV | NIST |
| IE | 9.46 ± 0.05 | eV | NIST |
| IE | 9.35 ± 0.04 | eV | NIST |
| IE | 9.40 | eV | NIST |
| IE | 9.05 ± 0.05 | eV | NIST |
| IE | 9.05 | eV | NIST |
| log10WS | [-3.12; -3.12] |
|
|
| log10WS | -3.12 | Aq. Sol... | |
| log10WS | -3.12 | Estimat... | |
| logPoct/wat | 2.918 | Crippen Calculated Property | |
| McVol | 148.080 | ml/mol | McGowan Calculated Property |
| Pc | 3352.00 ± 4.00 | kPa | NIST |
| ρc | 321.07 ± 3.64 | kg/m3 | NIST |
| Inp | [1572.00; 1664.00] |
|
|
| Inp | 1606.40 | NIST | |
| Inp | 1625.00 | NIST | |
| Inp | 1664.00 | NIST | |
| Inp | 1611.00 | NIST | |
| Inp | 1621.00 | NIST | |
| Inp | 1621.00 | NIST | |
| Inp | 1644.00 | NIST | |
| Inp | 1610.40 | NIST | |
| Inp | 1621.00 | NIST | |
| Inp | 1611.00 | NIST | |
| Inp | 1623.00 | NIST | |
| Inp | 1636.00 | NIST | |
| Inp | 1637.00 | NIST | |
| Inp | 1635.00 | NIST | |
| Inp | 1634.00 | NIST | |
| Inp | 1631.00 | NIST | |
| Inp | 1644.00 | NIST | |
| Inp | 1660.00 | NIST | |
| Inp | 1585.00 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1655.00 | NIST | |
| Inp | 1635.10 | NIST | |
| Inp | 1628.00 | NIST | |
| Inp | Outlier 1573.00 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1612.00 | NIST | |
| Inp | 1612.00 | NIST | |
| Inp | Outlier 1572.00 | NIST | |
| Inp | 1610.00 | NIST | |
| Inp | 1610.00 | NIST | |
| Inp | 1640.00 | NIST | |
| Inp | 1627.00 | NIST | |
| Inp | 1645.00 | NIST | |
| Inp | 1628.00 | NIST | |
| Inp | 1612.00 | NIST | |
| Inp | 1635.00 | NIST | |
| Inp | 1644.00 | NIST | |
| Inp | 1604.00 | NIST | |
| Inp | 1655.00 | NIST | |
| Inp | 1590.00 | NIST | |
| Inp | 1594.00 | NIST | |
| Inp | 1603.00 | NIST | |
| Inp | 1603.00 | NIST | |
| Inp | 1610.00 | NIST | |
| Inp | 1610.00 | NIST | |
| I | [2410.00; 2505.00] |
|
|
| I | 2443.00 | NIST | |
| I | 2427.00 | NIST | |
| I | 2505.00 | NIST | |
| I | 2462.00 | NIST | |
| I | 2470.00 | NIST | |
| I | 2410.00 | NIST | |
| I | 2457.00 | NIST | |
| I | 2427.00 | NIST | |
| Tboil | 578.97 | K | KDB |
| Tc | 830.00 ± 2.00 | K | NIST |
| Tfus | [321.15; 321.43] | K |
|
| Tfus | 321.15 | K | KDB |
| Tfus | 321.43 | K | Aq. Sol... |
| Ttriple | [321.03; 323.40] | K |
|
| Ttriple | 323.40 | K | Determi... |
| Ttriple | 321.03 ± 0.02 | K | NIST |
| Vc | 0.553 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [342.27; 415.64] | J/mol×K | [604.07; 856.45] |
|
| Cp,gas | 342.27 | J/mol×K | 604.07 | Joback Calculated Property |
| Cp,gas | 357.47 | J/mol×K | 646.13 | Joback Calculated Property |
| Cp,gas | 371.37 | J/mol×K | 688.20 | Joback Calculated Property |
| Cp,gas | 384.06 | J/mol×K | 730.26 | Joback Calculated Property |
| Cp,gas | 395.61 | J/mol×K | 772.32 | Joback Calculated Property |
| Cp,gas | 406.11 | J/mol×K | 814.39 | Joback Calculated Property |
| Cp,gas | 415.64 | J/mol×K | 856.45 | Joback Calculated Property |
| Cp,liquid | [265.30; 311.00] | J/mol×K | [245.00; 345.00] |
|
| Cp,liquid | 265.30 | J/mol×K | 245.00 | Applica... |
| Cp,liquid | 269.90 | J/mol×K | 255.00 | Applica... |
| Cp,liquid | 274.50 | J/mol×K | 265.00 | Applica... |
| Cp,liquid | 279.00 | J/mol×K | 275.00 | Applica... |
| Cp,liquid | 283.60 | J/mol×K | 285.00 | Applica... |
| Cp,liquid | 288.10 | J/mol×K | 295.00 | Applica... |
| Cp,liquid | 292.70 | J/mol×K | 305.00 | Applica... |
| Cp,liquid | 297.30 | J/mol×K | 315.00 | Applica... |
| Cp,liquid | 301.80 | J/mol×K | 325.00 | Applica... |
| Cp,liquid | 306.40 | J/mol×K | 335.00 | Applica... |
| Cp,liquid | 311.00 | J/mol×K | 345.00 | Applica... |
| Cp,solid | 224.80 | J/mol×K | 300.00 | NIST |
| η | [0.0002067; 0.0022577] | Pa×s | [339.04; 604.07] |
|
| η | 0.0022577 | Pa×s | 339.04 | Joback Calculated Property |
| η | 0.0012047 | Pa×s | 383.21 | Joback Calculated Property |
| η | 0.0007319 | Pa×s | 427.38 | Joback Calculated Property |
| η | 0.0004882 | Pa×s | 471.55 | Joback Calculated Property |
| η | 0.0003490 | Pa×s | 515.73 | Joback Calculated Property |
| η | 0.0002631 | Pa×s | 559.90 | Joback Calculated Property |
| η | 0.0002067 | Pa×s | 604.07 | Joback Calculated Property |
| ΔfusH | [17.67; 18.81] | kJ/mol | [222.50; 324.20] |
|
| ΔfusH | 18.81 | kJ/mol | 222.50 | NIST |
| ΔfusH | 18.19 | kJ/mol | 321.00 | NIST |
| ΔfusH | 18.19 | kJ/mol | 321.03 | NIST |
| ΔfusH | 17.67 | kJ/mol | 321.20 | NIST |
| ΔfusH | 18.47 | kJ/mol | 321.30 | NIST |
| ΔfusH | 18.19 | kJ/mol | 324.20 | NIST |
| ΔsubH | [78.20; 96.10] | kJ/mol | [302.50; 321.00] |
|
| ΔsubH | 78.20 ± 1.20 | kJ/mol | 302.50 | NIST |
| ΔsubH | 95.00 ± 0.20 | kJ/mol | 304.00 | NIST |
| ΔsubH | 95.00 ± 1.50 | kJ/mol | 305.50 | NIST |
| ΔsubH | 92.90 ± 0.80 | kJ/mol | 306.00 | NIST |
| ΔsubH | 96.10 | kJ/mol | 306.00 | NIST |
| ΔsubH | 93.90 ± 0.50 | kJ/mol | 307.00 | NIST |
| ΔsubH | 89.96 | kJ/mol | 308.00 | NIST |
| ΔsubH | 78.20 ± 0.80 | kJ/mol | 313.00 | NIST |
| ΔsubH | 95.00 ± 1.00 | kJ/mol | 321.00 | NIST |
| ΔvapH | [59.00; 65.10] | kJ/mol | [526.00; 553.00] |
|
| ΔvapH | 62.20 | kJ/mol | 526.00 | NIST |
| ΔvapH | 59.00 | kJ/mol | 552.50 | NIST |
| ΔvapH | 65.10 | kJ/mol | 553.00 | NIST |
| Psub | [1.19e-04; 1.24e-03] | kPa | [300.37; 320.23] |
|
| Psub | 1.19e-04 | kPa | 300.37 | Vapor p... |
| Psub | 1.61e-04 | kPa | 302.88 | Vapor p... |
| Psub | 2.20e-04 | kPa | 305.39 | Vapor p... |
| Psub | 3.02e-04 | kPa | 307.90 | Vapor p... |
| Psub | 4.01e-04 | kPa | 310.26 | Vapor p... |
| Psub | 5.35e-04 | kPa | 312.75 | Vapor p... |
| Psub | 7.08e-04 | kPa | 315.24 | Vapor p... |
| Psub | 9.39e-04 | kPa | 317.73 | Vapor p... |
| Psub | 1.24e-03 | kPa | 320.23 | Vapor p... |
| ΔfusS | [55.00; 56.67] | J/mol×K | [321.03; 321.20] |
|
| ΔfusS | 56.67 | J/mol×K | 321.03 | NIST |
| ΔfusS | 55.00 | J/mol×K | 321.20 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [430.70; 497.00] | K | [1.30; 13.30] |
|
| Tboilr | 430.70 | K | 1.30 | NIST |
| Tboilr | 497.00 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [429.53; 613.48] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.56649e+01 | |||
| Coefficient B | -5.82958e+03 | |||
| Coefficient C | -5.04230e+01 | |||
| Temperature range, min. | 429.53 | |||
| Temperature range, max. | 613.48 | |||
| Pvap | 1.33 | kPa | 429.53 | Calculated Property |
| Pvap | 2.93 | kPa | 449.97 | Calculated Property |
| Pvap | 5.96 | kPa | 470.41 | Calculated Property |
| Pvap | 11.34 | kPa | 490.85 | Calculated Property |
| Pvap | 20.40 | kPa | 511.29 | Calculated Property |
| Pvap | 34.91 | kPa | 531.72 | Calculated Property |
| Pvap | 57.18 | kPa | 552.16 | Calculated Property |
| Pvap | 90.10 | kPa | 572.60 | Calculated Property |
| Pvap | 137.20 | kPa | 593.04 | Calculated Property |
| Pvap | 202.65 | kPa | 613.48 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzophenone.
Mixtures
- Benzophenone + Water
- 1-Propanol, 2-methyl- + Benzophenone
- Ethanol + Benzophenone
- 1-Octanol + Benzophenone
- Benzophenone + Methyl Alcohol
- Acetonitrile + Benzophenone
- 1-Propanol + Benzophenone
- Acetone + Benzophenone
- Isopropyl Alcohol + Benzophenone
- Benzophenone + Ethyl Acetate
- 1-Butanol + Benzophenone
- Benzophenone + Acetic acid, methyl ester
- Dodecane + Benzophenone
- Benzophenone + Carbon Tetrachloride
- Decane + Benzophenone
- Benzophenone + Nonane
- Octane + Benzophenone
- Benzophenone + Heptane
- n-Hexane + Benzophenone
- Dodecane + Benzophenone + Carbon Tetrachloride
Find more mixtures with Benzophenone.
Sources
- Crippen Method
- Vapor pressures and vaporization enthalpies of 5-nonanone, linalool and 6-methyl-5-hepten-2-one. Data evaluation
- Application of fast scanning calorimetry to the fusion thermochemistry of low-molecular-weight organic compounds: Fast-crystallizing m-terphenyl heat capacities in a deeply supercooled liquid state
- Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
- Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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