Chemical Properties of Diethyl carbonate (CAS 105-58-8)

InChI

InChI=1S/C5H10O3/c1-3-7-5(6)8-4-2/h3-4H2,1-2H3

InChI Key

OIFBSDVPJOWBCH-UHFFFAOYSA-N

Formula

C5H10O3

SMILES

CCOC(=O)OCC

Molecular Weight¹

118.13

CAS

105-58-8

Other Names

• C2H5OC(O)OC2H5
• CARBONIC ACID,DIETHYL ESTER
• Carbonic acid, diethyl ester
• DEC
• Diaethylcarbonat
• Diatol
• Diethyl ester of carbonic acid
• Diethylester kyseliny uhlicite
• Diethylkarbonat
• Ethoxyformic anhydride
• Ethyl carbonate
• Ethyl carbonate ((EtO)2CO)
• Eufin
• NCI-C60899
• NSC 8849
• UN 2366

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.4531		Relay (1.0) Calculated Property
ΔcH°liquid	[-2715.17; -2672.50]	kJ/mol
ΔcH°liquid	-2715.17 ± 0.69	kJ/mol	NIST
ΔcH°liquid	-2672.50	kJ/mol	NIST
ΔfG°	-424.15	kJ/mol	Joback Calculated Property
ΔfH°gas	[-642.40; -637.90]	kJ/mol
ΔfH°gas	-637.90 ± 0.80	kJ/mol	NIST
ΔfH°gas	-642.40 ± 2.20	kJ/mol	NIST
ΔfH°liquid	[-724.17; -681.50]	kJ/mol
ΔfH°liquid	-681.50 ± 0.80	kJ/mol	NIST
ΔfH°liquid	-724.17	kJ/mol	NIST
ΔfusH°	14.26	kJ/mol	Joback Calculated Property
ΔvapH°	[39.10; 81.80]	kJ/mol
ΔvapH°	43.60	kJ/mol	NIST
ΔvapH°	44.40 ± 0.20	kJ/mol	NIST
ΔvapH°	43.60 ± 0.20	kJ/mol	NIST
ΔvapH°	43.60 ± 0.15	kJ/mol	NIST
ΔvapH°	43.60	kJ/mol	NIST
ΔvapH°	39.10	kJ/mol	NIST
ΔvapH°	Outlier 81.80	kJ/mol	NIST
IE	10.14	eV	Relay (1.0) Calculated Property
log10WS	-0.97		Relay (1.0) Calculated Property
logPoct/wat	1.179		Crippen Calculated Property
McVol	94.620	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Safety	1		KDB
Pc	3419.86	kPa	Joback Calculated Property
Inp	[747.00; 785.00]
Inp	747.00		NIST
Inp	747.00		NIST
Inp	761.00		NIST
Inp	784.00		NIST
Inp	765.00		NIST
Inp	769.00		NIST
Inp	769.00		NIST
Inp	768.00		NIST
Inp	785.00		NIST
Inp	765.00		NIST
Inp	765.00		NIST
Inp	768.00		NIST
Inp	747.00		NIST
I	[1083.00; 1116.00]
I	Outlier 1083.00		NIST
I	Outlier 1083.00		NIST
I	1100.00		NIST
I	1101.00		NIST
I	1116.00		NIST
I	1103.00		NIST
I	1104.00		NIST
I	1099.00		NIST
I	1102.00		NIST
I	1105.00		NIST
I	1105.00		NIST
I	1100.00		NIST
I	1099.00		NIST
Tboil	[399.00; 400.10]	K
Tboil	399.32	K	VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
Tboil	399.32	K	Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
Tboil	399.60	K	Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
Tboil	399.65	K	KDB
Tboil	399.20	K	NIST
Tboil	399.00	K	NIST
Tboil	399.70 ± 0.50	K	NIST
Tboil	400.10 ± 0.40	K	NIST
Tboil	400.10 ± 0.40	K	NIST
Tboil	399.70 ± 0.50	K	NIST
Tboil	399.65 ± 0.50	K	NIST
Tboil	399.10 ± 0.50	K	NIST
Tc	[578.10; 578.20]	K
Tc	578.10	K	Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
Tc	578.20	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tfus	[195.86; 230.15]	K
Tfus	195.86	K	Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
Tfus	196.40	K	Vapor Pressures and Thermophysical Properties of Dimethyl Carbonate, Diethyl Carbonate, and Dipropyl Carbonate
Tfus	230.15	K	KDB
Vc	0.375	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[182.00; 254.40]	J/mol×K	[288.15; 373.15]
Cp,liquid	210.20	J/mol×K	288.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	211.49	J/mol×K	293.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	219.90	J/mol×K	293.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	210.90	J/mol×K	294.20	NIST
Cp,liquid	210.90	J/mol×K	294.70	NIST
Cp,liquid	182.00	J/mol×K	298.00	NIST
Cp,liquid	221.20	J/mol×K	298.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	212.46	J/mol×K	298.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	222.30	J/mol×K	303.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	213.83	J/mol×K	303.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	214.89	J/mol×K	308.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	223.40	J/mol×K	308.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	225.30	J/mol×K	313.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	215.80	J/mol×K	313.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	218.55	J/mol×K	318.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	226.60	J/mol×K	318.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	220.32	J/mol×K	323.15	Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
Cp,liquid	228.40	J/mol×K	323.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	230.80	J/mol×K	328.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	232.00	J/mol×K	333.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	234.60	J/mol×K	338.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	237.60	J/mol×K	343.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	240.30	J/mol×K	348.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	242.50	J/mol×K	353.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	245.50	J/mol×K	358.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	248.90	J/mol×K	363.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	251.30	J/mol×K	368.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
Cp,liquid	254.40	J/mol×K	373.15	Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
η	[0.0003580; 0.0008640]	Pa×s	[288.15; 363.15]
η	0.0008640	Pa×s	288.15	Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η	0.0008000	Pa×s	293.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0008030	Pa×s	293.15	Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η	0.0008090	Pa×s	293.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0008010	Pa×s	293.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0008000	Pa×s	293.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0007570	Pa×s	298.15	Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η	0.0007460	Pa×s	298.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0007460	Pa×s	298.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0007500	Pa×s	298.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0006950	Pa×s	303.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0007020	Pa×s	303.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0007000	Pa×s	303.15	Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η	0.0006950	Pa×s	303.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0006580	Pa×s	308.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0006160	Pa×s	313.15	Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η	0.0006100	Pa×s	313.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0006100	Pa×s	313.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0006180	Pa×s	313.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0005410	Pa×s	323.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0005410	Pa×s	323.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0004830	Pa×s	333.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0004830	Pa×s	333.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0004350	Pa×s	343.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0004350	Pa×s	343.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0003930	Pa×s	353.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0003930	Pa×s	353.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0003580	Pa×s	363.15	Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η	0.0003580	Pa×s	363.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
εr	[2.83; 2.84]		[288.15; 328.15]
εr	2.84		288.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	2.83		298.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	2.84		308.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	2.84		318.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
εr	2.84		328.15	On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
ΔfusH	9.24	kJ/mol	198.20	NIST
ΔvapH	[39.10; 44.30]	kJ/mol	[331.00; 377.50]
ΔvapH	44.30	kJ/mol	331.00	NIST
ΔvapH	39.10	kJ/mol	338.00	NIST
ΔvapH	40.90	kJ/mol	354.00	NIST
ΔvapH	42.30	kJ/mol	371.00	NIST
ΔvapH	39.70	kJ/mol	377.50	NIST
Pvap	[0.29; 361.00]	kPa	[273.10; 452.20]
Pvap	0.29	kPa	273.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.29	kPa	273.30	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.30	kPa	274.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.31	kPa	274.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.33	kPa	275.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.35	kPa	276.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.36	kPa	276.50	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.38	kPa	277.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.40	kPa	277.96	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.41	kPa	278.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.41	kPa	278.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.52	kPa	282.06	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.56	kPa	282.40	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.58	kPa	283.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.56	kPa	283.30	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.63	kPa	285.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.67	kPa	286.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.78	kPa	286.80	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.80	kPa	288.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.79	kPa	288.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.83	kPa	288.30	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	0.78	kPa	288.40	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.02	kPa	291.80	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.05	kPa	293.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.04	kPa	293.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.03	kPa	293.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.04	kPa	293.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.03	kPa	293.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	1.08	kPa	293.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.06	kPa	293.30	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.45	kPa	296.80	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.49	kPa	298.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.52	kPa	298.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.45	kPa	298.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.41	kPa	298.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	1.54	kPa	298.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.91	kPa	301.80	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.01	kPa	303.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.06	kPa	303.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.02	kPa	303.10	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	1.84	kPa	303.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	1.99	kPa	303.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	1.95	kPa	303.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	1.99	kPa	303.30	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.35	kPa	306.64	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	2.45	kPa	306.80	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.69	kPa	307.80	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.61	kPa	308.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	2.65	kPa	308.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	2.64	kPa	308.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.69	kPa	308.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	2.67	kPa	308.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	3.01	kPa	310.74	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	3.07	kPa	310.90	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	3.43	kPa	313.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	3.45	kPa	313.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	3.65	kPa	313.30	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	3.96	kPa	315.00	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	3.95	kPa	315.20	Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
Pvap	4.58	kPa	318.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	4.46	kPa	318.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	4.51	kPa	318.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	6.17	kPa	323.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	5.75	kPa	323.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	5.83	kPa	323.15	Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap	7.16	kPa	328.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	9.09	kPa	333.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	11.56	kPa	338.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	13.78	kPa	343.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	13.80	kPa	343.77	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	16.09	kPa	348.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	19.30	kPa	351.67	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	20.83	kPa	353.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	20.74	kPa	353.15	Isothermal vapor liquid and vapor liquid liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
Pvap	22.56	kPa	354.68	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	22.70	kPa	355.63	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	25.03	kPa	357.44	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	26.00	kPa	358.29	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	27.54	kPa	359.95	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	29.99	kPa	362.26	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	30.23	kPa	363.15	Isothermal vapor liquid and vapor liquid liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
Pvap	31.30	kPa	363.84	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	32.51	kPa	364.46	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	35.05	kPa	366.57	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	35.20	kPa	366.98	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	37.52	kPa	368.45	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	39.10	kPa	369.75	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	40.03	kPa	370.28	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	42.49	kPa	372.04	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	42.80	kPa	372.28	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	45.10	kPa	373.00	Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
Pvap	45.05	kPa	373.73	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	46.50	kPa	374.61	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	47.47	kPa	375.26	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	50.04	kPa	376.81	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	50.50	kPa	377.05	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	52.46	kPa	378.22	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	55.00	kPa	379.59	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	55.03	kPa	379.67	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	57.56	kPa	381.03	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	58.80	kPa	381.49	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	59.95	kPa	382.32	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	63.10	kPa	383.37	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	63.50	kPa	383.57	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	62.52	kPa	383.60	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	64.97	kPa	384.81	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	67.44	kPa	385.98	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	68.50	kPa	386.18	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	70.02	kPa	387.13	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	72.80	kPa	387.61	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	72.51	kPa	388.28	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	74.96	kPa	389.32	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	78.50	kPa	390.35	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	77.43	kPa	390.35	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	79.97	kPa	391.39	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	84.00	kPa	392.39	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	82.52	kPa	392.45	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	84.84	kPa	393.34	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	88.20	kPa	393.93	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	87.52	kPa	394.36	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	89.81	kPa	395.23	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	93.40	kPa	395.72	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	92.53	kPa	396.21	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	94.89	kPa	397.03	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	97.54	kPa	397.96	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	101.50	kPa	398.28	Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
Pvap	100.03	kPa	398.81	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	101.38	kPa	399.27	Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
Pvap	101.30	kPa	399.60	Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
Pvap	143.00	kPa	412.50	Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
Pvap	361.00	kPa	452.20	Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
n0	[1.38210; 1.38450]		[293.15; 298.15]
n0	1.38300		293.15	Vapor liquid equilibria of carbon dioxide with isopropyl acetate, diethyl carbonate and ethyl butyrate at elevated pressures
n0	1.38450		293.15	Densities and derived thermodynamic properties of binary mixtures of diethylcarbonate, acetophenone, and 1-hexanol at T = (293.15 to 323.15) K for the liquid region and at ambient pressure
n0	1.38450		293.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices for Binary Mixtures of Diethylcarbonate, Acetophenone, and 1-Hexanol at (293.15, 303.15, 313.15, and 323.15) K for the Liquid Region and at Ambient Pressure
n0	1.38280		298.15	Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0	1.38210		298.15	Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
n0	1.38300		298.15	Viscosities, Ultrasonic Velocities at (288.15 and 298.15) K, and Refractive Indices at (298.15) K of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane with Dimethyl Carbonate, Diethyl Carbonate, and Propylene Carbonate
ρl	[935.08; 991.60]	kg/m3	[278.15; 328.15]
ρl	991.60	kg/m3	278.15	Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
ρl	980.29	kg/m3	288.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	980.29	kg/m3	288.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	980.49	kg/m3	288.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	980.09	kg/m3	288.15	Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
ρl	974.57	kg/m3	293.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	974.91	kg/m3	293.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	974.90	kg/m3	293.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	969.18	kg/m3	298.15	Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
ρl	969.07	kg/m3	298.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	969.07	kg/m3	298.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	968.89	kg/m3	298.15	Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
ρl	969.23	kg/m3	298.15	Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
ρl	970.00	kg/m3	298.15	Low pressure carbon dioxide solubility in lithium-ion batteries based electrolytes as a function of temperature. Measurement and prediction
ρl	969.10	kg/m3	298.15	Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
ρl	969.30	kg/m3	298.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	969.08	kg/m3	298.15	Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
ρl	969.12	kg/m3	298.15	Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
ρl	967.83	kg/m3	298.15	Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
ρl	969.10	kg/m3	298.15	Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
ρl	969.00	kg/m3	298.15	Isobaric Vapor Liquid Equilibria for Binary Systems of Diethyl Carbonate + Propylene Carbonate, Diethyl Carbonate + Propylene Glycol, and Ethanol + Propylene Carbonate at 101.3 kPa
ρl	969.30	kg/m3	298.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	969.32	kg/m3	298.15	Influence of alkyl group and temperature on thermophysical properties of carboxylic acid and their binary mixtures
ρl	969.10	kg/m3	298.15	Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
ρl	963.50	kg/m3	303.15	Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
ρl	963.66	kg/m3	303.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	963.70	kg/m3	303.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	963.60	kg/m3	303.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	958.00	kg/m3	308.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	958.00	kg/m3	308.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	957.98	kg/m3	308.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	957.90	kg/m3	308.15	Excess Enthalpies, Densities, Viscosities, and Refractive Indices of Binary Mixtures Involving Some Poly(glycols) + Diethyl Carbonate at 308.15 K
ρl	957.80	kg/m3	308.15	Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
ρl	957.98	kg/m3	308.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	952.40	kg/m3	313.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	952.43	kg/m3	313.15	Densities, Viscosities, and Refractive Indices of New Mixtures of Poly(ethylene glycols) + Dialkyl Carbonates at 313.15 K
ρl	952.15	kg/m3	313.15	Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
ρl	952.32	kg/m3	313.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	952.10	kg/m3	313.15	Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
ρl	947.67	kg/m3	318.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	946.70	kg/m3	318.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	946.40	kg/m3	318.15	Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
ρl	946.60	kg/m3	318.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	947.67	kg/m3	318.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
ρl	940.70	kg/m3	323.15	Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
ρl	940.86	kg/m3	323.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	940.90	kg/m3	323.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	935.08	kg/m3	328.15	Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
ρl	935.12	kg/m3	328.15	On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
ρl	935.20	kg/m3	328.15	Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
ρl	935.12	kg/m3	328.15	Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
csound,fluid	1178.00	m/s	298.15	Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
γ	[0.02; 0.03]	N/m	[273.18; 373.17]
γ	0.03	N/m	273.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	278.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	283.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	288.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	293.16	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	298.10	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	298.15	Surface tension, density, and speed of sound for the ternary mixture {diethyl carbonate + p-xylene + decane}
γ	0.03	N/m	303.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.03	N/m	308.11	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	308.15	Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
γ	0.02	N/m	313.19	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	318.16	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	323.16	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	328.12	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	333.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	338.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	343.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	348.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	353.19	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	358.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	363.16	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	368.18	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
γ	0.02	N/m	373.17	Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	980.3
288.15	5000.00	984.5
288.15	10000.00	988.6
288.15	20000.00	996.3
288.15	30000.00	1003.6
288.15	40000.00	1010.5
298.15	100.00	968.9
298.15	5000.00	973.8
298.15	10000.00	977.8
298.15	20000.00	986.0
298.15	30000.00	993.6
298.15	40000.00	1000.8
308.15	100.00	957.7
308.15	5000.00	962.4
308.15	10000.00	967.1
308.15	20000.00	975.7
308.15	30000.00	983.8
308.15	40000.00	991.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	969.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	969.4
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[143.29; 303.89]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			4.92520e+01
Coefficient B			3.60840e-01
Coefficient C			-4.26000e-05
Coefficient D			-6.36000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	143.29	J/mol×K	273.00	Calculated Property
Cp,gas	168.76	J/mol×K	353.78	Calculated Property
Cp,gas	192.79	J/mol×K	434.56	Calculated Property
Cp,gas	215.19	J/mol×K	515.33	Calculated Property
Cp,gas	235.74	J/mol×K	596.11	Calculated Property
Cp,gas	254.26	J/mol×K	676.89	Calculated Property
Cp,gas	270.53	J/mol×K	757.67	Calculated Property
Cp,gas	284.36	J/mol×K	838.44	Calculated Property
Cp,gas	295.55	J/mol×K	919.22	Calculated Property
Cp,gas	303.89	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[3.67e-03; 3396.12]	kPa	[230.15; 576.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.76598e+02
Coefficient B			-1.16692e+04
Coefficient C			-2.43764e+01
Coefficient D			2.02849e-05
Coefficient E			0.00000e+00
Temperature range, min.			230.15
Temperature range, max.			576.00
Pvap	3.67e-03	kPa	230.15	Calculated Property
Pvap	0.18	kPa	268.58	Calculated Property
Pvap	2.46	kPa	307.01	Calculated Property
Pvap	15.84	kPa	345.43	Calculated Property
Pvap	62.89	kPa	383.86	Calculated Property
Pvap	183.16	kPa	422.29	Calculated Property
Pvap	437.25	kPa	460.72	Calculated Property
Pvap	921.36	kPa	499.14	Calculated Property
Pvap	1803.01	kPa	537.57	Calculated Property
Pvap	3396.12	kPa	576.00	Calculated Property
Pvap	[0.13; 101.60]	kPa	[263.10; 399.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.56027e+01
Coefficient B			-3.96483e+03
Coefficient C			-3.79590e+01
Reference			Stull, 1947
Temperature range, min.			263.10
Temperature range, max.			399.00
Pvap	0.13	kPa	263.10	Calculated Property
Pvap	0.41	kPa	278.20	Calculated Property
Pvap	1.08	kPa	293.30	Calculated Property
Pvap	2.57	kPa	308.40	Calculated Property
Pvap	5.57	kPa	323.50	Calculated Property
Pvap	11.19	kPa	338.60	Calculated Property
Pvap	21.02	kPa	353.70	Calculated Property
Pvap	37.28	kPa	368.80	Calculated Property
Pvap	62.91	kPa	383.90	Calculated Property
Pvap	101.60	kPa	399.00	Calculated Property

Similar Compounds

Find more compounds similar to Diethyl carbonate.

Mixtures

• Diethyl carbonate + Propanoic acid + Water
• Diethyl carbonate + Carbon dioxide
• Diethyl carbonate + Diphenyl carbonate
• Diethyl carbonate + Aniline
• Diethyl carbonate + Benzonitrile
• Diethyl carbonate + Benzaldehyde
• Diethyl carbonate + n-Hexane
• Diethyl carbonate + Heptane
• Diethyl carbonate + Octane
• Diethyl carbonate + Cyclohexane
• Diethyl carbonate + Ethanol
• Diethyl carbonate + Ethanol + Heptane
• Diethyl carbonate + Water
• Diethyl carbonate + Ethanol + Water
• Diethyl carbonate + 2,5,8,11-Tetraoxadodecane
• Diethyl carbonate + Acetone + Water
• Diethyl carbonate + 2-Butanone + Water
• Diethyl carbonate + 2,5,8,11,14-Pentaoxapentadecane
• Diethyl carbonate + p-Xylene
• Diethyl carbonate + Ethyl Acetate

Find more mixtures with Diethyl carbonate.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Vapor liquid equilibria of carbon dioxide with isopropyl acetate, diethyl carbonate and ethyl butyrate at elevated pressures
• Excess molar enthalpies for binary carbon dioxide + diethyl carbonate system at 298.15 - 308.15K and 5.0 - 6.5MPa
• Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
• Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
• Vapor-liquid equilibrium data for the binary systems in the process of synthesizing diethyl carbonate
• Separation of propionic acid by diethyl carbonate or diethyl malonate or diethyl fumarate and the synergistic effect of phosphorus compounds and amines
• Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
• Activity coefficients and partial molar excess enthalpies at infinite dilution for four esters in water
• Liquid phase equilibria of (water + formic acid + diethyl carbonate or diethyl malonate or diethyl fumarate) ternary systems at 298.15K and atmospheric pressure
• Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
• Isothermal vapor liquid and vapor liquid liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
• Ionic interplay of lithium salts in binary mixtures of acetonitrile and diethyl carbonate probed by physicochemical approach
• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
• Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
• VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
• Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
• Densities and derived thermodynamic properties of binary mixtures of diethylcarbonate, acetophenone, and 1-hexanol at T = (293.15 to 323.15) K for the liquid region and at ambient pressure
• On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
• High-pressure phase equilibrium for the binary systems of {carbon dioxide (1) + dimethyl carbonate (2)} and {carbon dioxide (1) + diethyl carbonate (2)} at temperatures of 273 K, 283 K, and 293 K
• Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
• On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
• Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
• Surface tension, density, and speed of sound for the ternary mixture {diethyl carbonate + p-xylene + decane}
• Thermophysical properties for (diethyl carbonate + p-xylene + octane) ternary system
• Low pressure carbon dioxide solubility in pure electrolyte solvents for lithium-ion batteries as a function of temperature. Measurement and prediction
• Volumetric properties of dialkyl carbonate + n-alkane mixtures at high pressures: Experimental measurement and Nitta-Chao model prediction
• Low pressure carbon dioxide solubility in lithium-ion batteries based electrolytes as a function of temperature. Measurement and prediction
• Ternary (liquid + liquid) equilibria for (water + 1-propanol + dimethyl carbonate, or diethyl carbonate) systems at several temperatures
• Experimental and Nitta-Chao model prediction of high pressure density of p-xylene with dialkyl carbonates or n-alkanes
• Effect of temperature on density, sound velocity, refractive index and their derived properties for the binary systems (heptanoic acid + propanoic or butanoic acids)
• Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
• Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
• Phase equilibria of the ternary systems of (water + diethyl carbonate) with acetone, or 2-butanone at four temperatures
• Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
• Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
• Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
• Influence of alkyl group and temperature on thermophysical properties of carboxylic acid and their binary mixtures
• Isobaric Vapor Liquid Equilibria for Binary Systems of Diethyl Carbonate + Propylene Carbonate, Diethyl Carbonate + Propylene Glycol, and Ethanol + Propylene Carbonate at 101.3 kPa
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
• Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
• Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
• Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
• Vapor Pressures and Thermophysical Properties of Dimethyl Carbonate, Diethyl Carbonate, and Dipropyl Carbonate
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
• Atmospheric Ternary Liquid-Liquid Equilibrium for the Diethyl Carbonate + 1-Propanol + Water System at Temperature of 303.15, 313.15, 323.15, and 333.15 K
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Isopropyl Acetate, sec-Butyl Acetate, or Isoamyl Acetate at 101.3 kPa
• Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
• Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
• Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
• Vapor-Liquid Equilibria of Binary Carbon Dioxide + Alkyl Carbonate Mixture Systems
• Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
• Densities, Viscosities, and Refractive Indices of New Mixtures of Poly(ethylene glycols) + Dialkyl Carbonates at 313.15 K
• Excess Enthalpies, Densities, Viscosities, and Refractive Indices of Binary Mixtures Involving Some Poly(glycols) + Diethyl Carbonate at 308.15 K
• Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
• Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
• Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
• Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
• Viscosities, Ultrasonic Velocities at (288.15 and 298.15) K, and Refractive Indices at (298.15) K of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane with Dimethyl Carbonate, Diethyl Carbonate, and Propylene Carbonate
• Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
• Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
• Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
• Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
• Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate + Methanol, + Ethanol, + Dimethyl Carbonate, or + Diethyl Carbonate at 101.3 kPa
• Experimental Measurements and Correlations of Liquid-Liquid Equilibria for the Ternary and Quaternary Mixtures Formed by Dialkyl Carbonates at T = 298.15 K
• Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
• Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
• Liquid Liquid Equilibrium for the Water + Diethyl Carbonate + Ethanol System at Different Temperatures
• Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
• Liquid Liquid Equilibria for Quaternary Systems of Water + Ethanol + Diethyl Carbonate + Methylbenzene or Heptane
• Densities, Viscosities, Speeds of Sound, and Refractive Indices for Binary Mixtures of Diethylcarbonate, Acetophenone, and 1-Hexanol at (293.15, 303.15, 313.15, and 323.15) K for the Liquid Region and at Ambient Pressure
• Determination of Temperature-Dependent Henry s Law Constant of Four Oxygenated Solutes in Water Using Headspace Solid-Phase Microextraction Technique
• Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
• Solubility of HFC134a (1,1,1,2-Tetrafluoroethane) in Two Dialkyl Carbonates
• Mutual Diffusion Coefficients of Diethyl Carbonate and Diethyl Adipate in Heptane at T = (278.15 to 338.15) K under Atmospheric Pressure
• Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
• Measurements and Correlation of Liquid-Liquid Equilibria Containing Dimethyl Carbonate and Diethyl Carbonate at T = 298.15 K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook

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