Chemical Properties of 1,3-Dioxolane (CAS 646-06-0)

InChI

InChI=1S/C3H6O2/c1-2-5-3-4-1/h1-3H2

InChI Key

WNXJIVFYUVYPPR-UHFFFAOYSA-N

Formula

C3H6O2

SMILES

C1COCO1

Molecular Weight¹

74.08

CAS

646-06-0

Other Names

• 1,3-Dioxole, dihydro-
• 1,3-dioxacyclopentane
• 1,3-dioxolan
• Dioxolan
• Dioxolane
• Ethylene glycol formal
• Formal glycol
• Glycolformal
• dihydro-1,3-dioxole
• ethylene glycol methylene ether
• formaldehyde ethylene acetal

• 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).
• 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).
• ν : Kinematic viscosity (m²/s).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• 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_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.2707		Relay (1.0) Calculated Property
ΔcH°liquid	[-1705.00; -1700.00]	kJ/mol
ΔcH°liquid	-1700.80 ± 1.40	kJ/mol	NIST
ΔcH°liquid	-1700.00	kJ/mol	NIST
ΔcH°liquid	-1705.00	kJ/mol	NIST
Cp,liquid	121.66	J/mol×K	Thermodynamics of Mixtures Involving Some Linear or Cyclic Ketones and Cyclic Ethers. 4. Systems Containing 1,3-Dioxolane
η	0.0005310	Pa×s	Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
ΔfG°	-153.60	kJ/mol	Joback Calculated Property
ΔfH°gas	-301.70 ± 2.20	kJ/mol	NIST
ΔfH°liquid	-337.20 ± 1.40	kJ/mol	NIST
ΔfusH°	12.35	kJ/mol	Joback Calculated Property
ΔvapH°	[35.50; 36.00]	kJ/mol
ΔvapH°	35.50	kJ/mol	NIST
ΔvapH°	36.00 ± 0.40	kJ/mol	NIST
IE	[9.90; 10.10]	eV
IE	9.90	eV	NIST
IE	10.02	eV	NIST
IE	10.10	eV	NIST
logPoct/wat	-0.009		Crippen Calculated Property
McVol	54.010	ml/mol	McGowan Calculated Property
Pc	5818.28	kPa	Joback Calculated Property
Inp	[582.00; 638.00]
Inp	638.00		NIST
Inp	594.00		NIST
Inp	597.00		NIST
Inp	582.00		NIST
Inp	593.00		NIST
Inp	590.00		NIST
Inp	608.00		NIST
Inp	592.00		NIST
Inp	592.00		NIST
Inp	635.00		NIST
Inp	597.00		NIST
Inp	635.00		NIST
Ip	935.00		NIST
S°gas	310.50 ± 4.10	J/mol×K	NIST
S°liquid	280.20	J/mol×K	NIST
Tboil	[339.12; 348.75]	K
Tboil	339.12	K	Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
Tboil	348.57	K	Vapor-Liquid Equilibrium Data for Methanol + 1,3-Dioxolane + Water and Constituent Binary Systems at 101.3 kPa.
Tboil	348.00	K	Study of Solution Properties of Some Alkali Bromides in Aqueous Binary Mixtures of 1,3-Dioxolane in View of Different Models
Tboil	347.70	K	NIST
Tboil	348.75	K	NIST
Tc	532.03	K	Relay (1.0) Calculated Property
Tfus	[175.85; 178.15]	K
Tfus	178.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	175.85	K	NIST
Tfus	175.90 ± 0.60	K	NIST
Ttriple	175.93 ± 0.02	K	NIST
Vc	0.197	m3/kmol	Relay (1.0) Calculated Property

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	[118.00; 129.50]	J/mol×K	[288.15; 328.15]
Cp,liquid	118.80	J/mol×K	288.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	120.30	J/mol×K	293.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	118.00	J/mol×K	298.00	NIST
Cp,liquid	121.70	J/mol×K	298.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	120.84	J/mol×K	298.15	NIST
Cp,liquid	123.30	J/mol×K	303.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	124.40	J/mol×K	308.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	125.30	J/mol×K	313.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	126.80	J/mol×K	318.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	128.10	J/mol×K	323.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid	129.50	J/mol×K	328.15	Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
η	[0.0004580; 0.0005878]	Pa×s	[298.15; 318.15]
η	0.0005878	Pa×s	298.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
η	0.0005128	Pa×s	308.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
η	0.0004580	Pa×s	318.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
ΔfusH	[2.68; 6.57]	kJ/mol	[142.40; 175.90]
ΔfusH	2.68	kJ/mol	142.40	NIST
ΔfusH	6.57	kJ/mol	175.90	NIST
ΔfusH	6.57	kJ/mol	175.90	NIST
ΔvapH	[33.70; 35.80]	kJ/mol	[301.50; 339.00]
ΔvapH	35.80	kJ/mol	301.50	NIST
ΔvapH	34.10	kJ/mol	317.50	NIST
ΔvapH	34.60	kJ/mol	326.00	NIST
ΔvapH	33.70	kJ/mol	326.00	NIST
ΔvapH	33.70	kJ/mol	339.00	NIST
ν	[0.0000005; 0.0000007]	m2/s	[283.15; 313.15]
ν	0.0000007	m2/s	283.15	Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
ν	0.0000006	m2/s	298.15	Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
ν	0.0000005	m2/s	313.15	Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
Pvap	[5.42; 49.01]	kPa	[280.46; 328.15]
Pvap	5.42	kPa	280.46	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	6.20	kPa	282.96	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	7.14	kPa	285.51	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	7.91	kPa	287.44	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	10.78	kPa	293.48	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	13.59	kPa	298.12	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	13.54	kPa	298.15	Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
Pvap	13.54	kPa	298.15	Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
Pvap	15.69	kPa	301.25	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	17.05	kPa	303.00	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	19.15	kPa	305.57	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	23.08	kPa	309.76	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	26.83	kPa	313.15	Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
Pvap	26.73	kPa	313.16	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	31.18	kPa	316.81	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	49.01	kPa	328.15	Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
Pvap	49.01	kPa	328.15	Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
n0	[1.39740; 1.39800]		[298.15; 298.15]
n0	1.39800		298.15	Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
n0	1.39740		298.15	Physics and Chemistry of Lithium Halides in 1,3-Dioxolane and Its Binary Mixtures with Acetonitrile probed by Conductometric, Volumetric, Viscometric, Refractometric and Acoustic Study
n0	1.39779		298.15	Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
ρl	[1046.30; 1059.00]	kg/m3	[298.15; 308.15]
ρl	1059.00	kg/m3	298.15	Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
ρl	1058.73	kg/m3	298.15	Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
ρl	1058.62	kg/m3	298.15	(Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
ρl	1058.62	kg/m3	298.15	Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
ρl	1058.70	kg/m3	298.15	Probing subsistence of ion-pair and triple-ion of an ionic salt in liquid environments by means of conductometric contrivance
ρl	1047.20	kg/m3	298.15	Thermodynamic properties of liquid mixtures containing 1,3-dioxolane and anilines: Excess molar volumes, excess molar enthalpies, excess Gibb's free energy and isentropic compressibilities changes of mixing
ρl	1058.76	kg/m3	298.15	Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
ρl	1058.62	kg/m3	298.15	Experimental and predicted viscosities of the ternary mixture (hexane + 1,3-dioxolane + 2-butanol) at 298.15 and 313.15 K
ρl	1058.90	kg/m3	298.15	Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
ρl	1051.80	kg/m3	303.15	Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
ρl	1052.60	kg/m3	303.15	Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
ρl	1046.30	kg/m3	308.15	Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
ΔfusS	[18.80; 37.33]	J/mol×K	[142.40; 175.90]
ΔfusS	18.80	J/mol×K	142.40	NIST
ΔfusS	37.33	J/mol×K	175.90	NIST
csound,fluid	[1270.90; 1406.30]	m/s	[283.15; 313.15]
csound,fluid	1406.30	m/s	283.15	Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid	1339.90	m/s	298.15	Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid	1340.20	m/s	298.15	Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
csound,fluid	1271.60	m/s	313.15	Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid	1270.90	m/s	313.15	Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
γ	[0.03; 0.03]	N/m	[288.15; 308.15]
γ	0.03	N/m	288.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.03	N/m	298.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.03	N/m	308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[68.35; 189.78]	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			-3.16200e+01
Coefficient B			4.41000e-01
Coefficient C			-2.94400e-04
Coefficient D			7.48000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	68.35	J/mol×K	273.00	Calculated Property
Cp,gas	90.86	J/mol×K	353.78	Calculated Property
Cp,gas	110.56	J/mol×K	434.56	Calculated Property
Cp,gas	127.70	J/mol×K	515.33	Calculated Property
Cp,gas	142.50	J/mol×K	596.11	Calculated Property
Cp,gas	155.20	J/mol×K	676.89	Calculated Property
Cp,gas	166.04	J/mol×K	757.67	Calculated Property
Cp,gas	175.26	J/mol×K	838.44	Calculated Property
Cp,gas	183.10	J/mol×K	919.22	Calculated Property
Cp,gas	189.78	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 214.40]	kPa	[256.45; 372.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46333e+01
Coefficient B			-3.02711e+03
Coefficient C			-4.54420e+01
Temperature range, min.			256.45
Temperature range, max.			372.15
Pvap	1.33	kPa	256.45	Calculated Property
Pvap	3.04	kPa	269.31	Calculated Property
Pvap	6.33	kPa	282.16	Calculated Property
Pvap	12.23	kPa	295.02	Calculated Property
Pvap	22.16	kPa	307.87	Calculated Property
Pvap	37.98	kPa	320.73	Calculated Property
Pvap	62.03	kPa	333.58	Calculated Property
Pvap	97.16	kPa	346.44	Calculated Property
Pvap	146.69	kPa	359.29	Calculated Property
Pvap	214.40	kPa	372.15	Calculated Property
Pvap	[6.15; 120.87]	kPa	[280.90; 355.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40886e+01
Coefficient B			-2.84917e+03
Coefficient C			-4.87350e+01
Reference			Cherkaskaya, Petrenkova, et al., 1968
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			280.90
Temperature range, max.			355.30
Pvap	6.15	kPa	280.90	Calculated Property
Pvap	9.38	kPa	289.17	Calculated Property
Pvap	13.91	kPa	297.43	Calculated Property
Pvap	20.10	kPa	305.70	Calculated Property
Pvap	28.40	kPa	313.97	Calculated Property
Pvap	39.29	kPa	322.23	Calculated Property
Pvap	53.34	kPa	330.50	Calculated Property
Pvap	71.16	kPa	338.77	Calculated Property
Pvap	93.43	kPa	347.03	Calculated Property
Pvap	120.87	kPa	355.30	Calculated Property

Similar Compounds

Find more compounds similar to 1,3-Dioxolane.

Mixtures

• 1,3-Dioxolane + TETRABUTYLAMMONIUM HEXAFLUOROPHOSPHATE
• 1,3-Dioxolane + Butane, 1-chloro-
• 1,3-Dioxolane + Butane, 2-chloro-
• 1,3-Dioxolane + Propane, 1-chloro-2-methyl-
• 1,3-Dioxolane + Propane, 2-chloro-2-methyl-
• 1,3-Dioxolane + 1-Propanol, 2-methyl-
• 2-Propanol, 2-methyl- + 1,3-Dioxolane
• 1,3-Dioxolane + Methyl Alcohol + Water
• 1,3-Dioxolane + Ethanol + Water
• 1,3-Dioxolane + 1-Propanol + Water
• 1,3-Dioxolane + 2-Propanol + Water
• 1,3-Dioxolane + 1-Butanol + Water
• 2-Propanol, 2-methyl- + 1,3-Dioxolane + Water
• 1,3-Dioxolane + 1-Butanol, 3-methyl- + Water
• 1,3-Dioxolane + Water
• 1,3-Dioxolane + Tetrabutylammonium tetrafluoroborate
• 1,3-Dioxolane + Pentane, 1-chloro-
• 1,3-Dioxolane + Hexane, 1-chloro-
• 1,3-Dioxolane + Water + 4-morpholinepropanesulfonic acid
• 1,3-Dioxolane + 1,4-Dioxane

Find more mixtures with 1,3-Dioxolane.

Sources

• 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).
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
• Partial Molar Volumes, Viscosity B-Coefficients, and Adiabatic Compressibilities of Sodium Molybdate in Aqueous 1,3-Dioxolane Mixtures from 303.15 to 323.15 K
• Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
• Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
• Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
• Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
• Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
• Ionic solvation of tetrabutylammonium hexafluorophosphate in pure nitromethane, 1, 3-dioxolane and nitrobenzene: A comparative physicochemical study
• Separation of 1,3-dioxolane from its azeotropic aqueous solution by using Good's buffer ionic liquid [TMA][EPPS]
• (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
• Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
• Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
• Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
• Partial molar volumes of organic solutes in water. XXI: Cyclic ethers at temperatures T = (278 to 373) K and at low pressure
• Partial molar volumes of organic solutes in water. XXII. Cyclic ethers at temperatures (298 to 573) K and pressures up to 30 MPa
• Probing subsistence of ion-pair and triple-ion of an ionic salt in liquid environments by means of conductometric contrivance
• (Liquid + liquid), (solid + liquid), and (solid + liquid + liquid) equilibria of systems containing cyclic ether (tetrahydrofuran or 1,3-dioxolane), water, and a biological buffer MOPS
• Excess molar volumes and excess isentropic compressibilities of mixtures containing lactam, cyclic ethers and cyclic alkanones
• Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
• Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
• Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
• Thermodynamic properties of liquid mixtures containing 1,3-dioxolane and anilines: Excess molar volumes, excess molar enthalpies, excess Gibb's free energy and isentropic compressibilities changes of mixing
• Physics and Chemistry of Lithium Halides in 1,3-Dioxolane and Its Binary Mixtures with Acetonitrile probed by Conductometric, Volumetric, Viscometric, Refractometric and Acoustic Study
• Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
• Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
• Vapor-Liquid Equilibrium Data for Methanol + 1,3-Dioxolane + Water and Constituent Binary Systems at 101.3 kPa.
• Thermodynamics of Mixtures Involving Some Linear or Cyclic Ketones and Cyclic Ethers. 4. Systems Containing 1,3-Dioxolane
• Experimental and predicted viscosities of the ternary mixture (hexane + 1,3-dioxolane + 2-butanol) at 298.15 and 313.15 K
• Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
• Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
• Partial Molar Isentropic Compressions of Selected Cyclic Ethers at Infinite Dilution in Water at Temperatures T = (278 to 318) K and Atmospheric Pressure
• Isobaric Vapor Liquid Equilibrium for the Ternary System (Formaldehyde + 1,3-Dioxolane + Water) at 101.3 kPa
• Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
• Studies on Molecular Interactions of Some Thiocyanate Salts in Coaqueous Solutions of 1,3-Dioxolane + Water by Volumetric, Viscometric, and Speed of Sound Measurements
• Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
• Density, Viscosity, Refractive Index, and Ultrasonic Speed of Binary Mixtures of 1,3-Dioxolane with 2-Methoxyethanol, 2-Ethoxyethanol, 2-Butoxyethanol, 2-Propylamine, and Cyclohexylamine
• Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
• Study of Solution Properties of Some Alkali Bromides in Aqueous Binary Mixtures of 1,3-Dioxolane in View of Different Models
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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