Chemical Properties of 1,3-Dioxolan-2-one (CAS 96-49-1)

InChI

InChI=1S/C3H4O3/c4-3-5-1-2-6-3/h1-2H2

InChI Key

KMTRUDSVKNLOMY-UHFFFAOYSA-N

Formula

C3H4O3

SMILES

O=C1OCCO1

Molecular Weight¹

88.06

CAS

96-49-1

Other Names

• 1,3-Dioxacyclopentan-2-one
• 2-Dioxolone
• Carbonic acid, cyclic ethylene ester
• Cyclic ethylene carbonate
• Dioxolone-2
• Ethylene glycol, cyclic carbonate
• Ethylenester kyseliny uhlicite
• Glycol carbonate
• NSC 11801
• Texacar EC
• carbonic acid, ethylene ester
• ethylene carbonate
• ethylene glycol carbonate

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• Δ_cH°_solid : Standard solid 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• 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°_liquid : Liquid phase 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 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).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• ρ_s : Solid Density (kg/m³).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4060; 0.4423]
ω	0.4060		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4423		ChemSep v8.3 pure component data Compiled value
PAff	814.20	kJ/mol	NIST
BasG	784.40	kJ/mol	NIST
ΔcH°liquid	-1069.30 ± 2.10	kJ/mol	NIST
ΔcH°solid	[-1171.32; -1161.40]	kJ/mol
ΔcH°solid	-1161.40	kJ/mol	NIST
ΔcH°solid	-1165.90 ± 3.70	kJ/mol	NIST
ΔcH°solid	-1170.60 ± 0.40	kJ/mol	NIST
ΔcH°solid	-1171.32	kJ/mol	NIST
μ	4.50	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-410.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-506.90; -503.00]	kJ/mol
ΔfH°gas	-506.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-503.00 ± 4.20	kJ/mol	NIST
ΔfH°liquid	-682.80 ± 2.10	kJ/mol	NIST
ΔfH°solid	[-590.90; -581.60]	kJ/mol
ΔfH°solid	-590.90	kJ/mol	NIST
ΔfH°solid	-586.30 ± 3.80	kJ/mol	NIST
ΔfH°solid	-581.60 ± 0.40	kJ/mol	NIST
ΔfusH°	12.94	kJ/mol	Joback Calculated Property
ΔvapH°	[60.80; 179.80]	kJ/mol
ΔvapH°	60.80 ± 0.10	kJ/mol	NIST
ΔvapH°	64.00 ± 0.10	kJ/mol	NIST
ΔvapH°	63.40 ± 0.30	kJ/mol	NIST
ΔvapH°	78.50 ± 4.20	kJ/mol	NIST
ΔvapH°	Outlier 179.80	kJ/mol	NIST
ΔvapH°	62.40	kJ/mol	NIST
IE	[10.40; 11.47]	eV
IE	10.40	eV	NIST
IE	10.40	eV	NIST
IE	10.70	eV	NIST
IE	11.10	eV	NIST
IE	11.47	eV	NIST
logPoct/wat	0.153		Crippen Calculated Property
McVol	55.580	ml/mol	McGowan Calculated Property
Pc	[6141.84; 6770.00]	kPa
Pc	6141.84	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	6770.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	8.01e-03	kPa	ChemSep v8.3 pure component data Compiled value
S°solid,1 bar	[132.54; 132.54]	J/mol×K
S°solid,1 bar	132.54	J/mol×K	NIST
S°solid,1 bar	132.54	J/mol×K	NIST
Tboil	521.15	K	ChemSep v8.3 pure component data Compiled value
Tc	[786.00; 806.00]	K
Tc	786.00	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	794.82	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	806.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[308.53; 312.95]	K
Tfus	308.53	K	Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
Tfus	311.15	K	Characterization on the exothermic behaviors of cathode materials reacted with ethylene carbonate in lithium-ion battery studied by differential scanning calorimeter (DSC)
Tfus	309.13	K	Vapor Pressures and Thermophysical Properties of Ethylene Carbonate, Propylene Carbonate, -Valerolactone, and -Butyrolactone
Tfus	310.90	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	309.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	308.90 ± 0.80	K	NIST
Tfus	Outlier 312.95 ± 0.20	K	NIST
Tfus	309.65 ± 0.15	K	NIST
Tfus	309.45 ± 0.20	K	NIST
Tfus	311.15 ± 1.50	K	NIST
Tfus	308.95 ± 0.50	K	NIST
Tfus	309.50 ± 0.60	K	NIST
Ttriple	[309.47; 309.55]	K
Ttriple	309.55	K	ChemSep v8.3 pure component data Compiled value
Ttriple	309.49	K	KDB
Ttriple	309.47 ± 0.00	K	NIST
Ttriple	309.49 ± 0.02	K	NIST
UQi	2.47		ChemSep v8.3 pure component data Compiled value
URi	2.93		ChemSep v8.3 pure component data Compiled value
Vc	[0.193; 0.195]	m3/kmol
Vc	0.195	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.193	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.1950000		ChemSep v8.3 pure component data Compiled value
Zra	0.24		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[133.90; 158.51]	J/mol×K	[323.15; 398.15]
Cp,liquid	133.90	J/mol×K	323.15	NIST
Cp,liquid	155.87	J/mol×K	383.15	Vapor Pressure and Liquid Heat Capacity of Alkylene Carbonates
Cp,liquid	156.75	J/mol×K	388.15	Vapor Pressure and Liquid Heat Capacity of Alkylene Carbonates
Cp,liquid	157.63	J/mol×K	393.15	Vapor Pressure and Liquid Heat Capacity of Alkylene Carbonates
Cp,liquid	158.51	J/mol×K	398.15	Vapor Pressure and Liquid Heat Capacity of Alkylene Carbonates
Cp,solid	[117.44; 117.44]	J/mol×K	[298.15; 298.15]
Cp,solid	117.44	J/mol×K	298.15	NIST
Cp,solid	117.44	J/mol×K	298.15	NIST
ΔfusH	[13.02; 13.30]	kJ/mol	[309.49; 311.20]
ΔfusH	13.29	kJ/mol	309.49	NIST
ΔfusH	13.29	kJ/mol	309.49	NIST
ΔfusH	13.30	kJ/mol	309.50	NIST
ΔfusH	13.30	kJ/mol	309.50	NIST
ΔfusH	13.02	kJ/mol	311.20	NIST
ΔsubH	68.70	kJ/mol	285.00	NIST
ΔvapH	[55.00; 60.30]	kJ/mol	[400.50; 423.00]
ΔvapH	55.00	kJ/mol	400.50	NIST
ΔvapH	60.30	kJ/mol	408.50	NIST
ΔvapH	56.30	kJ/mol	408.50	NIST
ΔvapH	59.60	kJ/mol	409.00	NIST
ΔvapH	56.48	kJ/mol	423.00	NIST
Pvap	[0.01; 0.47]	kPa	[310.30; 369.50]
Pvap	0.01	kPa	310.30	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.02	kPa	314.40	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.02	kPa	314.50	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.02	kPa	317.30	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.02	kPa	320.30	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.02	kPa	320.40	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.03	kPa	323.50	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.03	kPa	324.40	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.04	kPa	327.40	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.04	kPa	328.60	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.05	kPa	331.30	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.04	kPa	333.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.06	kPa	333.60	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.07	kPa	335.40	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.07	kPa	338.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.08	kPa	338.70	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.10	kPa	341.40	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.10	kPa	342.30	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.09	kPa	343.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.11	kPa	343.80	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.12	kPa	345.20	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.14	kPa	347.60	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.12	kPa	348.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.15	kPa	349.00	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.19	kPa	352.40	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.17	kPa	353.15	Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
Pvap	0.20	kPa	354.00	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.25	kPa	357.50	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.26	kPa	358.90	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.29	kPa	360.60	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.33	kPa	363.20	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.35	kPa	364.10	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.40	kPa	366.70	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
Pvap	0.47	kPa	369.50	Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
ρl	[1315.70; 1350.00]	kg/m3	[298.15; 318.15]
ρl	1350.00	kg/m3	298.15	Low pressure carbon dioxide solubility in lithium-ion batteries based electrolytes as a function of temperature. Measurement and prediction
ρl	1315.70	kg/m3	318.15	Solid-liquid equilibria and thermo-physical properties of liquid electrolyte systems for lithium ion batteries
ρs	1320.00	kg/m3	293.00	Cyclic alkylene carbonates. Experiment and first principle calculations for prediction of thermochemical properties
ΔfusS	[42.96; 42.96]	J/mol×K	[309.49; 309.49]
ΔfusS	42.96	J/mol×K	309.49	NIST
ΔfusS	42.96	J/mol×K	309.49	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	516.70	K	98.70	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[82.85; 197.92]	J/mol×K	[273.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			5.00750e+01
Coefficient B			-5.16610e+02
Coefficient C			5.38024e+00
Coefficient D			1.38930e-05
Coefficient E			-2.68900e-08
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	82.85	J/mol×K	273.00	Calculated Property
Cp,gas	111.59	J/mol×K	409.33	Calculated Property
Cp,gas	134.26	J/mol×K	545.67	Calculated Property
Cp,gas	151.54	J/mol×K	682.00	Calculated Property
Cp,gas	164.77	J/mol×K	818.33	Calculated Property
Cp,gas	175.02	J/mol×K	954.67	Calculated Property
Cp,gas	183.01	J/mol×K	1091.00	Calculated Property
Cp,gas	189.27	J/mol×K	1227.33	Calculated Property
Cp,gas	194.15	J/mol×K	1363.67	Calculated Property
Cp,gas	197.92	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[128.77; 217.00]	J/mol×K	[298.15; 511.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-5.72590e+01
Coefficient B			-1.70210e+01
Coefficient C			4.45824e+00
Coefficient D			3.38170e-03
Coefficient E			-2.06460e-06
Temperature range, min.			298.15
Temperature range, max.			511.15
Cp,liquid	128.77	J/mol×K	298.15	Calculated Property
Cp,liquid	139.08	J/mol×K	321.82	Calculated Property
Cp,liquid	149.36	J/mol×K	345.48	Calculated Property
Cp,liquid	159.58	J/mol×K	369.15	Calculated Property
Cp,liquid	169.69	J/mol×K	392.82	Calculated Property
Cp,liquid	179.65	J/mol×K	416.48	Calculated Property
Cp,liquid	189.41	J/mol×K	440.15	Calculated Property
Cp,liquid	198.92	J/mol×K	463.82	Calculated Property
Cp,liquid	208.14	J/mol×K	487.48	Calculated Property
Cp,liquid	217.00	J/mol×K	511.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0012007; 0.0005343]	Pa×s	[310.93; 372.04]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-8.74020e+00
Coefficient B			1.42450e+03
Coefficient C			-4.57080e-01
Coefficient D			5.93400e-07
Coefficient E			2.00000e+00
Temperature range, min.			310.93
Temperature range, max.			372.04
η	0.0012007	Pa×s	310.93	Calculated Property
η	0.0010807	Pa×s	317.72	Calculated Property
η	0.0009770	Pa×s	324.51	Calculated Property
η	0.0008869	Pa×s	331.30	Calculated Property
η	0.0008082	Pa×s	338.09	Calculated Property
η	0.0007392	Pa×s	344.88	Calculated Property
η	0.0006783	Pa×s	351.67	Calculated Property
η	0.0006246	Pa×s	358.46	Calculated Property
η	0.0005768	Pa×s	365.25	Calculated Property
η	0.0005343	Pa×s	372.04	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[65.25; 22.87]	kJ/mol	[309.55; 779.87]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			8.72970e+01
Coefficient B			-7.50430e-02
Coefficient C			3.70180e+00
Coefficient D			-6.19540e+00
Coefficient E			2.96310e+00
Critical temperature, Tc (K)			8.06000e+02
Temperature range, min.			309.55
Temperature range, max.			779.87
ΔvapH	65.25	kJ/mol	309.55	Calculated Property
ΔvapH	60.83	kJ/mol	361.81	Calculated Property
ΔvapH	56.91	kJ/mol	414.07	Calculated Property
ΔvapH	53.50	kJ/mol	466.32	Calculated Property
ΔvapH	50.48	kJ/mol	518.58	Calculated Property
ΔvapH	47.64	kJ/mol	570.84	Calculated Property
ΔvapH	44.58	kJ/mol	623.10	Calculated Property
ΔvapH	40.64	kJ/mol	675.35	Calculated Property
ΔvapH	34.55	kJ/mol	727.61	Calculated Property
ΔvapH	22.87	kJ/mol	779.87	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 226.20]	kPa	[391.32; 552.31]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.59477e+01
Coefficient B			-5.16933e+03
Coefficient C			-6.12240e+01
Temperature range, min.			391.32
Temperature range, max.			552.31
Pvap	1.33	kPa	391.32	Calculated Property
Pvap	2.98	kPa	409.21	Calculated Property
Pvap	6.17	kPa	427.10	Calculated Property
Pvap	11.91	kPa	444.98	Calculated Property
Pvap	21.70	kPa	462.87	Calculated Property
Pvap	37.57	kPa	480.76	Calculated Property
Pvap	62.18	kPa	498.65	Calculated Property
Pvap	98.92	kPa	516.53	Calculated Property
Pvap	151.94	kPa	534.42	Calculated Property
Pvap	226.20	kPa	552.31	Calculated Property
Pvap	[0.01; 6788.98]	kPa	[309.55; 806.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.25532e+02
Coefficient B			-1.22930e+04
Coefficient C			-1.58750e+01
Coefficient D			7.35720e-06
Coefficient E			2.00000e+00
Temperature range, min.			309.55
Temperature range, max.			806.00
Pvap	0.01	kPa	309.55	Calculated Property
Pvap	0.43	kPa	364.71	Calculated Property
Pvap	5.30	kPa	419.87	Calculated Property
Pvap	32.15	kPa	475.03	Calculated Property
Pvap	124.81	kPa	530.19	Calculated Property
Pvap	362.57	kPa	585.36	Calculated Property
Pvap	871.04	kPa	640.52	Calculated Property
Pvap	1848.78	kPa	695.68	Calculated Property
Pvap	3627.03	kPa	750.84	Calculated Property
Pvap	6788.98	kPa	806.00	Calculated Property
Pvap	[6.83e-03; 6634.23]	kPa	[309.55; 790.00]	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			9.59483e+01
Coefficient B			-1.14946e+04
Coefficient C			-1.11778e+01
Coefficient D			3.17385e-06
Coefficient E			0.00000e+00
Temperature range, min.			309.55
Temperature range, max.			790.00
Pvap	6.83e-03	kPa	309.55	Calculated Property
Pvap	0.30	kPa	362.93	Calculated Property
Pvap	4.35	kPa	416.32	Calculated Property
Pvap	30.24	kPa	469.70	Calculated Property
Pvap	130.53	kPa	523.08	Calculated Property
Pvap	406.10	kPa	576.47	Calculated Property
Pvap	1003.29	kPa	629.85	Calculated Property
Pvap	2100.77	kPa	683.23	Calculated Property
Pvap	3900.82	kPa	736.62	Calculated Property
Pvap	6634.23	kPa	790.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1338.19; 722.69]	kg/m3	[293.15; 779.87]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			1.35985e+02
Coefficient B			2.95900e-01
Coefficient C			8.06000e+02
Coefficient D			2.88570e-01
Temperature range, min.			293.15
Temperature range, max.			779.87
ρl	1338.19	kg/m3	293.15	Calculated Property
ρl	1293.69	kg/m3	347.23	Calculated Property
ρl	1246.96	kg/m3	401.31	Calculated Property
ρl	1197.49	kg/m3	455.39	Calculated Property
ρl	1144.57	kg/m3	509.47	Calculated Property
ρl	1087.11	kg/m3	563.55	Calculated Property
ρl	1023.31	kg/m3	617.63	Calculated Property
ρl	949.87	kg/m3	671.71	Calculated Property
ρl	859.19	kg/m3	725.79	Calculated Property
ρl	722.69	kg/m3	779.87	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[274.00; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			3.08230e-02
Coefficient B			3.49580e-01
Coefficient C			3.00320e+03
Coefficient D			8.30800e+05
Temperature range, min.			274.00
Temperature range, max.			1000.00
λgas	0.01	W/m×K	274.00	Calculated Property
λgas	0.01	W/m×K	354.67	Calculated Property
λgas	0.02	W/m×K	435.33	Calculated Property
λgas	0.03	W/m×K	516.00	Calculated Property
λgas	0.03	W/m×K	596.67	Calculated Property
λgas	0.04	W/m×K	677.33	Calculated Property
λgas	0.05	W/m×K	758.00	Calculated Property
λgas	0.06	W/m×K	838.67	Calculated Property
λgas	0.06	W/m×K	919.33	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.21; 0.16]	W/m×K	[309.55; 521.35]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			9.13420e-04
Coefficient B			-1.10820e+02
Coefficient C			-5.17480e-01
Coefficient D			-2.37930e-03
Coefficient E			3.93760e-07
Temperature range, min.			309.55
Temperature range, max.			521.35
λliquid	0.21	W/m×K	309.55	Calculated Property
λliquid	0.20	W/m×K	333.08	Calculated Property
λliquid	0.20	W/m×K	356.62	Calculated Property
λliquid	0.19	W/m×K	380.15	Calculated Property
λliquid	0.19	W/m×K	403.68	Calculated Property
λliquid	0.18	W/m×K	427.22	Calculated Property
λliquid	0.17	W/m×K	450.75	Calculated Property
λliquid	0.17	W/m×K	474.28	Calculated Property
λliquid	0.16	W/m×K	497.82	Calculated Property
λliquid	0.16	W/m×K	521.35	Calculated Property

Similar Compounds

Find more compounds similar to 1,3-Dioxolan-2-one.

Mixtures

• Tetrahydrofuran + 1,3-Dioxolan-2-one
• Acetonitrile + 1,3-Dioxolan-2-one
• Ethyl Acetate + 1,3-Dioxolan-2-one
• Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one
• lithium perchlorate + Tetrahydrofuran + 1,3-Dioxolan-2-one
• lithium bromide + Tetrahydrofuran + 1,3-Dioxolan-2-one
• Tetraethylammonium bromide + Tetrahydrofuran + 1,3-Dioxolan-2-one
• Tetra-N-butylammonium bromide + Tetrahydrofuran + 1,3-Dioxolan-2-one
• Acetonitrile + lithium perchlorate + 1,3-Dioxolan-2-one
• lithium bromide + Acetonitrile + 1,3-Dioxolan-2-one
• Acetonitrile + Tetraethylammonium bromide + 1,3-Dioxolan-2-one
• Acetonitrile + Tetra-N-butylammonium bromide + 1,3-Dioxolan-2-one
• Ethyl Acetate + lithium perchlorate + 1,3-Dioxolan-2-one
• lithium bromide + Ethyl Acetate + 1,3-Dioxolan-2-one
• Tetraethylammonium bromide + Ethyl Acetate + 1,3-Dioxolan-2-one
• Tetra-N-butylammonium bromide + Ethyl Acetate + 1,3-Dioxolan-2-one
• Ethane, 1,2-dimethoxy- + lithium perchlorate + 1,3-Dioxolan-2-one
• lithium bromide + Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one
• Tetraethylammonium bromide + Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one
• Tetra-N-butylammonium bromide + Ethane, 1,2-dimethoxy- + 1,3-Dioxolan-2-one

Find more mixtures with 1,3-Dioxolan-2-one.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Vapour pressure and enthalpy of vaporization of cyclic alkylene carbonates
• Thermodynamic of LiF dissolution in alkylcarbonates and some of their mixtures with water
• Solid-liquid equilibria and thermo-physical properties of liquid electrolyte systems for lithium ion batteries
• Thermophysical properties of 1-ethyl-3-methylimidazolium bromide ionic liquid in water + ethylene carbonate mixtures at T = (298.2, 308.2 and 318.2) K
• Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
• Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
• Cyclic alkylene carbonates. Experiment and first principle calculations for prediction of thermochemical properties
• Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
• Separation of aromatic hydrocarbons (toluene or benzene) from aliphatic hydrocarbon (n-heptane) by extraction with ethylene carbonate
• Low pressure carbon dioxide solubility in pure electrolyte solvents for lithium-ion batteries as a function of temperature. Measurement and prediction
• Low pressure carbon dioxide solubility in lithium-ion batteries based electrolytes as a function of temperature. Measurement and prediction
• Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
• Phase equilibrium and activity coefficients in ternary systems at 298.15 K: RbCl/CsCl + ethylene carbonate + water
• Liquid liquid equilibria for mixtures of (ethylene carbonate + aromatic hydrocarbon + cyclohexane)
• Characterization on the exothermic behaviors of cathode materials reacted with ethylene carbonate in lithium-ion battery studied by differential scanning calorimeter (DSC)
• Vapor Pressures and Thermophysical Properties of Ethylene Carbonate, Propylene Carbonate, -Valerolactone, and -Butyrolactone
• Measurement and Correlation of the Electrical Conductivity of the Ionic Liquid [BMIM][TFSI] in Binary Organic Solvents
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Infinite Dilution Activity Coefficients in Ethylene Glycol and Ethylene Carbonate
• Vapor Pressure and Liquid Heat Capacity of Alkylene Carbonates
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures Containing the Carbonate Group -OCOO-
• Phase Equilibria in Binary Mixtures of Water with Cyclic Alkylene Carbonates
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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