Chemical Properties of Diphenyl carbonate (CAS 102-09-0)

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

• ω : Acentric Factor.
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_sub : Sublimation pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_fus : Melting point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.6313		Relay (1.0) Calculated Property
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	-4.01		Relay (1.0) 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	822.83	K	Relay (1.0) Calculated Property
Tfus	[353.96; 355.95]	K
Tfus	353.96	K	Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
Tfus	353.96	K	Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
Tfus	355.95	K	Solubility of Diphenyl Carbonate in Pure Alcohols from (283 to 333) K
Vc	0.597	m3/kmol	Relay (1.0) 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 pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.22e-05	kPa	302.18	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.20e-05	kPa	302.18	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.28e-05	kPa	302.18	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.27e-05	kPa	302.18	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.27e-05	kPa	302.18	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.22e-05	kPa	302.18	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.17e-05	kPa	308.17	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.01e-05	kPa	308.17	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.00e-05	kPa	308.17	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.17e-05	kPa	308.17	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.01e-05	kPa	308.17	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.05e-05	kPa	308.17	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.09e-05	kPa	308.17	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.13e-04	kPa	314.32	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.13e-04	kPa	314.32	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.14e-04	kPa	314.32	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.16e-04	kPa	314.32	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.16e-04	kPa	314.32	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.15e-04	kPa	314.32	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.14e-04	kPa	314.32	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.40e-04	kPa	320.25	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.42e-04	kPa	320.25	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.39e-04	kPa	320.25	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.50e-04	kPa	320.25	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.46e-04	kPa	320.25	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.47e-04	kPa	320.25	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	2.42e-04	kPa	320.25	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.05e-04	kPa	326.23	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.08e-04	kPa	326.23	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	4.99e-04	kPa	326.23	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.18e-04	kPa	326.23	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.12e-04	kPa	326.23	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.17e-04	kPa	326.23	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	5.07e-04	kPa	326.23	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.04e-03	kPa	332.24	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.04e-03	kPa	332.24	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	9.92e-04	kPa	332.24	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.06e-03	kPa	332.24	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.03e-03	kPa	332.24	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
Psub	1.07e-03	kPa	332.24	Vapour pressures of selected organic compounds down to 1 mPa, using mass-loss Knudsen effusion method
ρl	1113.14	kg/m3	358.15	Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures

Pressure Dependent Properties

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

• Cheméo Relay (1.0)
• 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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