- InChI
- InChI=1S/C13H10O3/c14-13(15-11-7-3-1-4-8-11)16-12-9-5-2-6-10-12/h1-10H
- InChI Key
- ROORDVPLFPIABK-UHFFFAOYSA-N
- Formula
- C13H10O3
- SMILES
- O=C(Oc1ccccc1)Oc1ccccc1
- Molecular Weight1
- 214.22
- CAS
- 102-09-0
- Other Names
-
- Carbonic acid, diphenyl ester
- PHENYL CARBONATE
- Phenol carbonate
- 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).
- η : Dynamic viscosity (Pa×s).
- 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 standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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).
- ρl : Liquid Density (kg/m3).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Tfus : Melting 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 | -6143.60 ± 1.90 | kJ/mol | NIST |
| ΔfG° | -55.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -311.00 ± 8.80 | kJ/mol | NIST |
| ΔfH°solid | -401.40 ± 1.90 | kJ/mol | NIST |
| ΔfusH° | 21.48 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [90.00; 90.00] | kJ/mol |
|
| ΔsubH° | 90.00 ± 8.40 | kJ/mol | NIST |
| ΔsubH° | 90.00 ± 8.40 | kJ/mol | NIST |
| ΔvapH° | 80.90 ± 0.60 | kJ/mol | NIST |
| IE | 9.01 ± 0.05 | eV | NIST |
| log10WS | -3.69 | Crippen Calculated Property | |
| logPoct/wat | 3.264 | Crippen Calculated Property | |
| McVol | 159.820 | ml/mol | McGowan Calculated Property |
| Pc | 3173.97 | kPa | Joback Calculated Property |
| S°solid,1 bar | 278.40 | J/mol×K | NIST |
| Tboil | [574.70; 579.20] | K |
|
| Tboil | 574.70 | K | NIST |
| Tboil | 579.20 | K | NIST |
| Tc | 893.05 | K | Joback Calculated Property |
| Tfus | [353.96; 355.95] | K |
|
| Tfus | 353.96 | K | Solid-l... |
| Tfus | 353.96 | K | Solid-L... |
| Tfus | 355.95 | K | Solubil... |
| Vc | 0.590 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [390.94; 460.31] | J/mol×K | [648.91; 893.05] |
|
| Cp,gas | 390.94 | J/mol×K | 648.91 | Joback Calculated Property |
| Cp,gas | 405.28 | J/mol×K | 689.60 | Joback Calculated Property |
| Cp,gas | 418.47 | J/mol×K | 730.29 | Joback Calculated Property |
| Cp,gas | 430.54 | J/mol×K | 770.98 | Joback Calculated Property |
| Cp,gas | 441.51 | J/mol×K | 811.67 | Joback Calculated Property |
| Cp,gas | 451.43 | J/mol×K | 852.36 | Joback Calculated Property |
| Cp,gas | 460.31 | J/mol×K | 893.05 | Joback Calculated Property |
| Cp,solid | 263.13 | J/mol×K | 298.15 | NIST |
| η | [0.0001324; 0.0012325] | Pa×s | [383.50; 648.91] |
|
| η | 0.0012325 | Pa×s | 383.50 | Joback Calculated Property |
| η | 0.0007012 | Pa×s | 427.74 | Joback Calculated Property |
| η | 0.0004434 | Pa×s | 471.97 | Joback Calculated Property |
| η | 0.0003033 | Pa×s | 516.20 | Joback Calculated Property |
| η | 0.0002203 | Pa×s | 560.44 | Joback Calculated Property |
| η | 0.0001676 | Pa×s | 604.67 | Joback Calculated Property |
| η | 0.0001324 | Pa×s | 648.91 | Joback Calculated Property |
| ΔfusH | 23.43 | kJ/mol | 355.00 | NIST |
| Psub | [2.14e-05; 1.07e-03] | kPa | [302.18; 332.24] |
|
| Psub | 2.14e-05 | kPa | 302.18 | Vapour ... |
| Psub | 2.22e-05 | kPa | 302.18 | Vapour ... |
| Psub | 2.20e-05 | kPa | 302.18 | Vapour ... |
| Psub | 2.28e-05 | kPa | 302.18 | Vapour ... |
| Psub | 2.27e-05 | kPa | 302.18 | Vapour ... |
| Psub | 2.27e-05 | kPa | 302.18 | Vapour ... |
| Psub | 2.22e-05 | kPa | 302.18 | Vapour ... |
| Psub | 5.09e-05 | kPa | 308.17 | Vapour ... |
| Psub | 5.01e-05 | kPa | 308.17 | Vapour ... |
| Psub | 5.00e-05 | kPa | 308.17 | Vapour ... |
| Psub | 5.17e-05 | kPa | 308.17 | Vapour ... |
| Psub | 5.01e-05 | kPa | 308.17 | Vapour ... |
| Psub | 5.05e-05 | kPa | 308.17 | Vapour ... |
| Psub | 5.17e-05 | kPa | 308.17 | Vapour ... |
| Psub | 1.13e-04 | kPa | 314.32 | Vapour ... |
| Psub | 1.13e-04 | kPa | 314.32 | Vapour ... |
| Psub | 1.14e-04 | kPa | 314.32 | Vapour ... |
| Psub | 1.16e-04 | kPa | 314.32 | Vapour ... |
| Psub | 1.16e-04 | kPa | 314.32 | Vapour ... |
| Psub | 1.15e-04 | kPa | 314.32 | Vapour ... |
| Psub | 1.14e-04 | kPa | 314.32 | Vapour ... |
| Psub | 2.40e-04 | kPa | 320.25 | Vapour ... |
| Psub | 2.42e-04 | kPa | 320.25 | Vapour ... |
| Psub | 2.39e-04 | kPa | 320.25 | Vapour ... |
| Psub | 2.50e-04 | kPa | 320.25 | Vapour ... |
| Psub | 2.46e-04 | kPa | 320.25 | Vapour ... |
| Psub | 2.47e-04 | kPa | 320.25 | Vapour ... |
| Psub | 2.42e-04 | kPa | 320.25 | Vapour ... |
| Psub | 5.07e-04 | kPa | 326.23 | Vapour ... |
| Psub | 5.08e-04 | kPa | 326.23 | Vapour ... |
| Psub | 4.99e-04 | kPa | 326.23 | Vapour ... |
| Psub | 5.05e-04 | kPa | 326.23 | Vapour ... |
| Psub | 5.12e-04 | kPa | 326.23 | Vapour ... |
| Psub | 5.17e-04 | kPa | 326.23 | Vapour ... |
| Psub | 5.18e-04 | kPa | 326.23 | Vapour ... |
| Psub | 1.07e-03 | kPa | 332.24 | Vapour ... |
| Psub | 1.04e-03 | kPa | 332.24 | Vapour ... |
| Psub | 9.92e-04 | kPa | 332.24 | Vapour ... |
| Psub | 1.06e-03 | kPa | 332.24 | Vapour ... |
| Psub | 1.03e-03 | kPa | 332.24 | Vapour ... |
| Psub | 1.04e-03 | kPa | 332.24 | Vapour ... |
| ρl | 1113.14 | kg/m3 | 358.15 | Liquid ... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tfus | 352.70 | K | 101.00 | Solid-l... |
Similar Compounds
Find more compounds similar to Diphenyl carbonate.
Mixtures
- Carbonic acid, dimethyl ester + Diphenyl carbonate
- Diphenyl carbonate + Methyl Alcohol
- Carbonic acid, methyl phenyl ester + Diphenyl carbonate
- Ethanol + Diphenyl carbonate
- 1-Propanol + Diphenyl carbonate
- Isopropyl Alcohol + Diphenyl carbonate
- Diethyl carbonate + Diphenyl carbonate
- Diphenyl carbonate + Carbonic acid, dipropyl ester
- Diphenyl carbonate + Ethyl Acetate
- Acetic acid, phenyl ester + Diphenyl carbonate
- Diphenyl carbonate + Phenol
- Carbonic acid, methyl phenyl ester + Diphenyl carbonate + Water
- 1-Butanol + Diphenyl carbonate
- 1-Propanol, 2-methyl- + Diphenyl carbonate
- Carbonic acid, dimethyl ester + Diphenyl carbonate + Water
- Diphenyl carbonate + Phenol + Water
Sources
- Crippen Method
- Crippen Method
- Liquid-liquid equilibria of ternary mixtures of dimethyl carbonate, diphenyl carbonate, phenol and water at 358.15 K
- Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
- Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
- Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
- Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
- Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
- Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures
- Solubility of Diphenyl Carbonate in Pure Alcohols from (283 to 333) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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