Chemical Properties of Ethanol, 2,2'-oxybis- (CAS 111-46-6)

InChI

InChI=1S/C4H10O3/c5-1-3-7-4-2-6/h5-6H,1-4H2

InChI Key

MTHSVFCYNBDYFN-UHFFFAOYSA-N

Formula

C4H10O3

SMILES

OCCOCCO

Molecular Weight¹

106.12

CAS

111-46-6

Other Names

• 1,1'-oxybis[1-methoxy]methane
• 1,5-Dihydroxy-3-oxapentane
• 2,2'-Dihydroxyethyl ether
• 2,2'-OXYBIS ETHANOL
• 2,2'-Oxybis[Ethanol]
• 2,2'-Oxyethanol
• 2,2'-oxybis(ethan-1-ol)
• 2,2'-oxybis-ethanol
• 2,2'-oxydiethanol
• 2,2-Di(hydroxyethyl) ether
• 2,4,6-trioxaheptane
• 2-(2-hydroxyethoxy)ethanol
• 2-hydroxyethyl ether
• 3-Oxapentamethylene-1,5-diol
• 3-oxa-1,5-pentanediol
• 3-oxapentan-1,5-diol
• 3-oxapentane-1,5-diol
• BETA,BETA'-DIHYDROXYDIETHYL ETHER
• Bis(«beta»-hydroxyethyl) ether
• Brecolane NDG
• Carbitol
• D.E.H. 20
• D.E.H. 52
• DEG
• Deactivator E
• Deactivator H
• Dicol
• Diethylenglykol
• Digenos
• Diglycol
• Digol
• Dihydroxydiethyl ether
• Dissolvant APV
• Ethanol, 2,2'-oxydi-
• Ethylene diglycol
• Glycol ether
• Glycol hydroxyethyl ether
• Her
• NSC 36391
• TL4N
• bis(2-hydroxyethyl) ether
• diethylene glycol
• «beta»,«beta»'-Dihydroxydiethyl ether
• «beta»,«beta»'-Dihydroxyethyl ether

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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_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 Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point 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.
• γ : Surface Tension (N/m).
• 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).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	[0.5799; 0.6221]
ω	0.5799		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.6221		ChemSep v8.3 pure component data Compiled value
Tig	497.15	K	NCMS SOLV-DB
ΔcH°liquid	[-2374.70; -2372.90]	kJ/mol
ΔcH°liquid	-2374.70 ± 2.40	kJ/mol	NIST
ΔcH°liquid	-2372.90	kJ/mol	NIST
μ	2.52	debye	ChemSep v8.3 pure component data Compiled value
Tflash,cc	389.15	K	NCMS SOLV-DB
ΔfG°	-384.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-571.50; -546.40]	kJ/mol
ΔfH°gas	-546.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-571.50	kJ/mol	KDB
ΔfH°liquid	-628.50 ± 2.40	kJ/mol	NIST
ΔfusH°	15.48	kJ/mol	Joback Calculated Property
ΔvapH°	61.55	kJ/mol	NCMS SOLV-DB
IE	9.88	eV	Relay (1.0) Calculated Property
log10WS	0.73		Relay (1.0) Calculated Property
logPoct/wat	-1.470		NCMS SOLV-DB
McVol	84.830	ml/mol	McGowan Calculated Property
NFPA Fire	1		NCMS SOLV-DB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[4600.00; 4770.38]	kPa
Pc	4700.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	4770.38	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4600.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4700.00	kPa	KDB
Pc	4770.00 ± 50.00	kPa	NIST
Ptriple	3.20e-06	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[925.00; 967.00]
Inp	967.00		NIST
Inp	927.00		NIST
Inp	925.00		NIST
Inp	967.00		NIST
Inp	941.00		NIST
Ip	[1953.00; 1989.00]
Ip	1989.00		NIST
Ip	1975.00		NIST
Ip	1968.00		NIST
Ip	1953.00		NIST
Ip	1989.00		NIST
Ip	1975.00		NIST
Tboil	[517.95; 522.70]	K
Tboil	517.95	K	ChemSep v8.3 pure component data Compiled value
Tboil	519.00	K	KDB
Tboil	518.15	K	NCMS SOLV-DB
Tboil	518.20	K	NIST
Tboil	518.76 ± 0.05	K	NIST
Tboil	518.20 ± 0.80	K	NIST
Tboil	518.95	K	NIST
Tboil	518.65 ± 0.60	K	NIST
Tboil	Outlier 522.70 ± 0.60	K	NIST
Tboil	518.00 ± 2.00	K	NIST
Tc	[680.00; 753.00]	K
Tc	753.00	K	Critical temperatures and pressures of ethylene glycols
Tc	750.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	753.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	744.60	K	ChemSep v8.3 pure component data Compiled value
Tc	681.00	K	KDB
Tc	753.00 ± 4.00	K	NIST
Tc	723.50 ± 50.00	K	NIST
Tc	680.00 ± 20.00	K	NIST
Tc	680.00 ± 20.00	K	NIST
Tfus	[262.70; 265.40]	K
Tfus	262.95	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	262.70	K	ChemSep v8.3 pure component data Compiled value
Tfus	265.00	K	KDB
Tfus	263.15	K	NCMS SOLV-DB
Tfus	265.35	K	NIST
Tfus	265.40 ± 0.60	K	NIST
Tfus	263.05 ± 0.50	K	NIST
Tfus	262.80 ± 0.10	K	NIST
Tfus	262.80 ± 0.10	K	NIST
Ttriple	[262.70; 265.10]	K
Ttriple	265.10	K	Heat Capacity and Phase Behavior of Selected Oligo(ethylene glycol)s
Ttriple	262.70	K	ChemSep v8.3 pure component data Compiled value
UQi	4.80		ChemSep v8.3 pure component data Compiled value
URi	4.94		ChemSep v8.3 pure component data Compiled value
Vc	[0.312; 0.316]	m3/kmol
Vc	0.316	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.312	m3/kmol	ChemSep v8.3 pure component data Compiled value
VCOSTALD	0.35	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	1.07		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	0.2320000		ChemSep v8.3 pure component data Compiled value
Zra	[0.25; 0.25]
Zra	0.25		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[243.90; 287.00]	J/mol×K	[298.00; 353.15]
Cp,liquid	243.90	J/mol×K	298.00	NIST
Cp,liquid	287.00	J/mol×K	298.00	NIST
Cp,liquid	248.20	J/mol×K	303.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	251.30	J/mol×K	313.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	255.00	J/mol×K	323.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	259.20	J/mol×K	333.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	263.80	J/mol×K	343.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
Cp,liquid	266.80	J/mol×K	353.15	Heat capacities of the mixed-solvents desiccants (glycols +water + salts)
η	[0.0007890; 0.0385000]	Pa×s	[293.15; 464.05]
η	0.0364330	Pa×s	293.15	Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
η	0.0365200	Pa×s	293.15	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0381100	Pa×s	293.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0351000	Pa×s	294.20	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0283600	Pa×s	298.15	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0385000	Pa×s	298.15	NCMS SOLV-DB
η	0.0300120	Pa×s	298.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
η	0.0300120	Pa×s	298.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0298200	Pa×s	298.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0220910	Pa×s	303.15	Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
η	0.0221560	Pa×s	303.15	Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
η	0.0236400	Pa×s	303.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0179340	Pa×s	308.15	Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
η	0.0169720	Pa×s	308.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
η	0.0169720	Pa×s	308.15	Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
η	0.0190200	Pa×s	308.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0152500	Pa×s	312.60	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0151000	Pa×s	313.05	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0147060	Pa×s	313.15	Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
η	0.0145630	Pa×s	313.15	Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
η	0.0156000	Pa×s	313.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0121910	Pa×s	318.15	Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
η	0.0126900	Pa×s	318.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0100290	Pa×s	323.15	Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
η	0.0101950	Pa×s	323.15	Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
η	0.0106200	Pa×s	323.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0088530	Pa×s	328.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0084580	Pa×s	329.28	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0076400	Pa×s	333.05	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0072200	Pa×s	333.15	Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
η	0.0073620	Pa×s	333.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0062080	Pa×s	338.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0053690	Pa×s	343.15	Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
η	0.0053240	Pa×s	343.20	Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
η	0.0053400	Pa×s	344.99	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0048090	Pa×s	349.77	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0044100	Pa×s	353.05	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0041390	Pa×s	353.15	Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
η	0.0032310	Pa×s	366.77	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0027600	Pa×s	373.60	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0019200	Pa×s	393.40	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0014100	Pa×s	413.25	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0014090	Pa×s	413.65	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
η	0.0011500	Pa×s	428.15	Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
η	0.0007890	Pa×s	464.05	Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure
εr	[30.03; 31.81]		[293.15; 303.15]
εr	31.81		293.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
εr	30.95		298.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
εr	30.03		303.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
ΔvapH	[55.10; 69.20]	kJ/mol	[273.00; 523.00]
ΔvapH	57.30 ± 5.90	kJ/mol	273.00	NIST
ΔvapH	66.50	kJ/mol	413.00	NIST
ΔvapH	59.80	kJ/mol	441.00	NIST
ΔvapH	69.20	kJ/mol	458.00	NIST
ΔvapH	66.80	kJ/mol	462.50	NIST
ΔvapH	66.90 ± 0.30	kJ/mol	474.50	NIST
ΔvapH	63.10 ± 0.30	kJ/mol	474.50	NIST
ΔvapH	59.20 ± 0.30	kJ/mol	474.50	NIST
ΔvapH	55.10 ± 0.50	kJ/mol	474.50	NIST
ΔvapH	66.57	kJ/mol	523.00	NIST
ΔvapH	66.57	kJ/mol	523.00	NIST
Pvap	1.04e-03	kPa	298.15	NCMS SOLV-DB
n0	[1.44600; 1.44724]		[293.15; 298.15]
n0	1.44724		293.15	Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
n0	1.44600		298.15	NCMS SOLV-DB
ρl	[1059.00; 1123.30]	kg/m3	[283.15; 373.15]
ρl	1123.30	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	1120.05	kg/m3	288.15	Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
ρl	1119.80	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1121.40	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	1120.30	kg/m3	288.15	Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
ρl	1116.00	kg/m3	293.00	KDB
ρl	1116.20	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1117.80	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	1116.73	kg/m3	293.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1116.50	kg/m3	293.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1109.16	kg/m3	298.00	Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
ρl	1112.70	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1113.00	kg/m3	298.15	Solubility for dilute sulfur dioxide, viscosities, excess properties, and viscous flow thermodynamics of binary system N, N-dimethylformamide + diethylene glycol
ρl	1113.17	kg/m3	298.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1112.80	kg/m3	298.15	Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
ρl	1112.56	kg/m3	298.15	Isobaric Vapor-Liquid Equilibrium for Four Binary Systems of Ethane-1,2-diol, Butane-1,4-diol, 2-(2- Hydroxyethoxy)ethan-1-ol and 2-[2-(2- Hydroxyethoxy)ethoxy]ethanol at 10.0 kPa, 20.0 kPa and 40.0 kPa
ρl	1112.70	kg/m3	298.15	Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl	1112.38	kg/m3	298.15	Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
ρl	1114.20	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	1113.00	kg/m3	298.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1112.38	kg/m3	298.15	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	1109.00	kg/m3	303.15	Vapour pressures and densities of the mixed-solvent desiccants (glycols + water + salts)
ρl	1109.40	kg/m3	303.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1109.20	kg/m3	303.15	Solubility for dilute sulfur dioxide, viscosities, excess properties, and viscous flow thermodynamics of binary system N, N-dimethylformamide + diethylene glycol
ρl	1110.60	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	1109.47	kg/m3	303.15	Thermodynamic and physicochemical properties of binary mixtures of sulfolane with ethylene glycol, diethylene glycol, triethylene glycol, and tetraethylene glycol systems at 303.15K
ρl	1109.20	kg/m3	303.15	Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
ρl	1109.10	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	1109.60	kg/m3	303.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1110.00	kg/m3	303.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1109.30	kg/m3	303.15	Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl	1105.50	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	1106.01	kg/m3	308.15	Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
ρl	1105.65	kg/m3	308.15	Excess molar enthalpies of binary mixtures containing ethylene glycols or poly(ethylene glycols) + ethyl alcohol at 308.15K and atmospheric pressure
ρl	1106.10	kg/m3	308.15	Solubility for dilute sulfur dioxide, viscosities, excess properties, and viscous flow thermodynamics of binary system N, N-dimethylformamide + diethylene glycol
ρl	1107.00	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	1105.60	kg/m3	308.15	Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
ρl	1105.90	kg/m3	308.15	Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl	1105.65	kg/m3	308.15	Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
ρl	1105.88	kg/m3	308.15	Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
ρl	1105.80	kg/m3	308.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1105.88	kg/m3	308.15	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	1105.86	kg/m3	308.50	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	1101.90	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	1103.00	kg/m3	313.15	Vapour pressures and densities of the mixed-solvent desiccants (glycols + water + salts)
ρl	1102.30	kg/m3	313.15	Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
ρl	1103.40	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	1102.50	kg/m3	313.15	Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl	1103.00	kg/m3	313.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1103.00	kg/m3	313.15	Solubility for dilute sulfur dioxide, viscosities, excess properties, and viscous flow thermodynamics of binary system N, N-dimethylformamide + diethylene glycol
ρl	1102.20	kg/m3	313.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1099.20	kg/m3	318.15	Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
ρl	1099.70	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	1099.30	kg/m3	318.15	Solubility for dilute sulfur dioxide, viscosities, excess properties, and viscous flow thermodynamics of binary system N, N-dimethylformamide + diethylene glycol
ρl	1098.60	kg/m3	318.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1095.00	kg/m3	323.15	Vapour pressures and densities of the mixed-solvent desiccants (glycols + water + salts)
ρl	1095.00	kg/m3	323.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1095.90	kg/m3	323.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1094.70	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	1096.10	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	1091.40	kg/m3	328.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1092.50	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	1087.70	kg/m3	333.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1087.40	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	1088.80	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	1088.50	kg/m3	333.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1088.00	kg/m3	333.15	Vapour pressures and densities of the mixed-solvent desiccants (glycols + water + salts)
ρl	1085.20	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	1084.00	kg/m3	338.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1081.50	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	1080.30	kg/m3	343.15	Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
ρl	1080.00	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	1081.10	kg/m3	343.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl	1081.00	kg/m3	343.15	Vapour pressures and densities of the mixed-solvent desiccants (glycols + water + salts)
ρl	1077.80	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	1074.10	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	1070.30	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	1066.60	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	1062.80	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	1059.00	kg/m3	373.15	Thermophysical properties of glycols and glymes
γ	0.05	N/m	298.15	NCMS SOLV-DB
λliquid	[0.20; 0.21]	W/m×K	[298.10; 338.20]
λliquid	0.20	W/m×K	298.10	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λliquid	0.20	W/m×K	308.00	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λliquid	0.20	W/m×K	318.20	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λliquid	0.20	W/m×K	328.40	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
λliquid	0.21	W/m×K	338.20	Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	406.20	K	1.90	NIST

Datasets

1. Viscosity, Pa*s (2)
2. Mass density, kg/m3 (3)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	98.00	0.0365
293.15	49030.00	0.0527
293.15	98060.00	0.0742
293.15	147100.00	0.1026
293.15	196130.00	0.1399
293.15	245160.00	0.1873
298.15	98.00	0.0284
298.15	49030.00	0.0404
298.15	98060.00	0.0565
298.15	147100.00	0.0772
298.15	196130.00	0.1038
298.15	245160.00	0.1383
312.60	98.00	0.0152
312.62	49030.00	0.0210
312.63	98060.00	0.0282
312.67	147100.00	0.0371
312.71	196130.00	0.0483
312.75	245160.00	0.0621
329.28	98.00	0.0085
329.33	98060.00	0.0147
329.33	196130.00	0.0238
329.33	245160.00	0.0296
329.38	49030.00	0.0113
329.38	147100.00	0.0188
344.99	98.00	0.0053
345.20	49030.00	0.0071
345.38	98060.00	0.0090
345.47	147100.00	0.0112
345.61	196130.00	0.0138
345.78	245160.00	0.0168
349.77	98.00	0.0048
350.06	49030.00	0.0063
350.13	147100.00	0.0099
350.16	98060.00	0.0079
350.40	196130.00	0.0120
366.77	98.00	0.0032
367.13	49030.00	0.0041
367.26	147100.00	0.0063
367.30	98060.00	0.0051
367.37	196130.00	0.0076
367.61	245160.00	0.0091
413.65	98.00	0.0014
413.80	49030.00	0.0018
413.93	98060.00	0.0022
414.01	147100.00	0.0026
414.09	196130.00	0.0030
414.29	245160.00	0.0035
463.94	98060.00	0.0012
463.99	49030.00	0.0010
464.05	98.00	0.0008
464.09	147100.00	0.0014
464.20	196130.00	0.0017
464.37	245160.00	0.0019
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.30	308.15	0.0176
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1124.3
283.15	1000.00	1124.7
283.15	2000.00	1125.3
283.15	5000.00	1126.5
283.15	7000.00	1127.4
283.15	10000.00	1128.8
283.15	12000.00	1129.6
283.15	16000.00	1131.3
283.15	20000.00	1133.0
283.15	25000.00	1135.1
283.15	30000.00	1137.2
283.15	35000.00	1139.2
283.15	40000.00	1141.2
283.15	45000.00	1143.0
283.15	50000.00	1145.1
283.15	55000.00	1146.9
283.15	60000.00	1148.8
283.15	65000.00	1150.7
283.15	70000.00	1152.4
283.15	75000.00	1154.2
283.15	80000.00	1155.8
283.15	85000.00	1157.5
283.15	90000.00	1159.2
283.15	95000.00	1160.9
293.15	100.00	1117.1
293.15	1000.00	1117.5
293.15	2000.00	1118.0
293.15	5000.00	1119.3
293.15	7000.00	1120.2
293.15	10000.00	1121.6
293.15	12000.00	1122.5
293.15	16000.00	1124.3
293.15	20000.00	1126.0
293.15	25000.00	1128.2
293.15	30000.00	1130.3
293.15	35000.00	1132.4
293.15	40000.00	1134.3
293.15	45000.00	1136.4
293.15	50000.00	1138.4
293.15	55000.00	1140.4
293.15	60000.00	1142.2
293.15	65000.00	1144.1
293.15	70000.00	1145.8
293.15	75000.00	1147.7
293.15	80000.00	1149.4
293.15	85000.00	1151.2
293.15	90000.00	1152.9
293.15	95000.00	1154.6
303.14	100.00	1109.9
303.14	1000.00	1110.3
303.14	2000.00	1110.7
303.14	5000.00	1112.2
303.14	7000.00	1113.1
303.14	10000.00	1114.5
303.14	12000.00	1115.4
303.14	16000.00	1117.3
303.14	20000.00	1119.0
303.14	25000.00	1121.2
303.14	30000.00	1123.4
303.14	35000.00	1125.5
303.14	40000.00	1127.5
303.14	45000.00	1129.6
303.14	50000.00	1131.6
303.14	55000.00	1133.6
303.14	60000.00	1135.5
303.14	65000.00	1137.4
303.14	70000.00	1139.3
303.14	75000.00	1141.1
303.14	80000.00	1142.9
303.14	85000.00	1144.6
303.14	90000.00	1146.4
303.14	95000.00	1148.2
313.15	100.00	1102.7
313.15	1000.00	1103.2
313.15	2000.00	1103.6
313.15	5000.00	1105.2
313.15	7000.00	1106.2
313.15	10000.00	1107.7
313.15	12000.00	1108.6
313.15	16000.00	1110.4
313.15	20000.00	1112.3
313.15	25000.00	1114.5
313.15	30000.00	1116.7
313.15	35000.00	1118.9
313.15	40000.00	1121.0
313.15	45000.00	1123.1
313.15	50000.00	1125.1
313.15	55000.00	1127.1
313.15	60000.00	1129.1
313.15	65000.00	1131.1
313.15	70000.00	1132.9
313.15	75000.00	1134.8
313.15	80000.00	1136.6
313.15	85000.00	1138.4
313.15	90000.00	1140.2
313.15	95000.00	1141.9
323.20	100.00	1095.4
323.20	1000.00	1095.8
323.20	2000.00	1096.3
323.20	5000.00	1097.8
323.20	7000.00	1098.8
323.20	10000.00	1100.3
323.20	12000.00	1101.3
323.20	16000.00	1103.3
323.20	20000.00	1105.2
323.20	25000.00	1107.5
323.20	30000.00	1109.9
323.20	35000.00	1112.0
323.20	40000.00	1114.2
323.20	45000.00	1116.3
323.20	50000.00	1118.4
323.20	55000.00	1120.5
323.20	60000.00	1122.5
323.20	65000.00	1124.5
323.20	70000.00	1126.5
323.20	75000.00	1128.3
323.20	80000.00	1130.3
323.20	85000.00	1132.2
323.20	90000.00	1133.9
323.20	95000.00	1135.7
333.20	100.00	1088.1
333.20	1000.00	1088.7
333.20	2000.00	1089.2
333.20	5000.00	1090.8
333.20	7000.00	1091.8
333.20	10000.00	1093.3
333.20	12000.00	1094.4
333.20	16000.00	1096.4
333.20	20000.00	1098.3
333.20	25000.00	1100.7
333.20	30000.00	1103.0
333.20	35000.00	1105.3
333.20	40000.00	1107.6
333.20	45000.00	1109.7
333.20	50000.00	1111.9
333.20	55000.00	1113.9
333.20	60000.00	1116.0
333.20	65000.00	1118.0
333.20	70000.00	1120.1
333.20	75000.00	1121.9
333.20	80000.00	1123.8
333.20	85000.00	1125.9
333.20	90000.00	1127.7
333.20	95000.00	1129.5
343.20	100.00	1080.7
343.20	1000.00	1081.2
343.20	2000.00	1081.7
343.20	5000.00	1083.4
343.20	7000.00	1084.5
343.20	10000.00	1086.1
343.20	12000.00	1087.1
343.20	16000.00	1089.1
343.20	20000.00	1091.2
343.20	25000.00	1093.7
343.20	30000.00	1096.1
343.20	35000.00	1098.5
343.20	40000.00	1100.8
343.20	45000.00	1103.1
343.20	50000.00	1105.2
343.20	55000.00	1107.4
343.20	60000.00	1109.5
343.20	65000.00	1111.6
343.20	70000.00	1113.7
343.20	75000.00	1115.7
343.20	80000.00	1117.6
343.20	85000.00	1119.5
343.20	90000.00	1121.4
343.20	95000.00	1123.3
353.19	100.00	1073.2
353.19	1000.00	1073.8
353.19	2000.00	1074.3
353.19	5000.00	1076.0
353.19	7000.00	1077.1
353.19	10000.00	1078.7
353.19	12000.00	1079.8
353.19	16000.00	1081.9
353.19	20000.00	1084.0
353.19	25000.00	1086.6
353.19	30000.00	1089.1
353.19	35000.00	1091.6
353.19	40000.00	1093.9
353.19	45000.00	1096.3
353.19	50000.00	1098.5
353.19	55000.00	1100.8
353.19	60000.00	1102.9
353.19	65000.00	1105.0
353.19	70000.00	1107.2
353.19	75000.00	1109.2
353.19	80000.00	1111.2
353.19	85000.00	1113.2
353.19	90000.00	1115.1
353.19	95000.00	1117.0
363.17	100.00	1065.6
363.17	1000.00	1066.2
363.17	2000.00	1066.8
363.17	5000.00	1068.5
363.17	7000.00	1069.6
363.17	10000.00	1071.4
363.17	12000.00	1072.5
363.17	16000.00	1074.6
363.17	20000.00	1076.9
363.17	25000.00	1079.4
363.17	30000.00	1082.0
363.17	35000.00	1084.6
363.17	40000.00	1087.0
363.17	45000.00	1089.4
363.17	50000.00	1091.8
363.17	55000.00	1094.1
363.17	60000.00	1096.3
363.17	65000.00	1098.5
363.17	70000.00	1100.5
363.17	75000.00	1102.6
363.17	80000.00	1104.8
363.17	85000.00	1106.8
363.17	90000.00	1108.8
363.17	95000.00	1110.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1123.1
283.15	100.00	1123.1
283.15	640.00	1123.3
283.15	1080.00	1123.5
283.15	1590.00	1123.7
283.15	2140.00	1124.0
283.15	3050.00	1124.3
283.15	5050.00	1125.2
283.15	6930.00	1126.0
283.15	9930.00	1127.2
283.15	14810.00	1129.3
283.15	19760.00	1131.3
283.15	24610.00	1133.3
283.15	29600.00	1135.2
283.15	34500.00	1137.1
283.15	39420.00	1139.0
283.15	44300.00	1140.8
283.15	49180.00	1142.6
283.15	54060.00	1144.4
283.15	59030.00	1146.1
283.15	63810.00	1147.8
283.15	68760.00	1149.5
293.15	100.00	1115.9
293.15	100.00	1115.9
293.15	570.00	1116.1
293.15	1080.00	1116.3
293.15	1530.00	1116.6
293.15	2110.00	1116.8
293.15	3080.00	1117.2
293.15	5040.00	1118.1
293.15	6990.00	1118.9
293.15	9940.00	1120.2
293.15	14840.00	1122.3
293.15	19740.00	1124.3
293.15	24680.00	1126.4
293.15	29600.00	1128.4
293.15	34530.00	1130.3
293.15	39360.00	1132.2
293.15	44320.00	1134.1
293.15	49120.00	1136.0
293.15	54090.00	1137.8
293.15	58990.00	1139.6
293.15	63820.00	1141.3
293.15	68750.00	1143.0
303.15	100.00	1108.8
303.15	100.00	1108.8
303.15	680.00	1109.0
303.15	1130.00	1109.2
303.15	1580.00	1109.4
303.15	2120.00	1109.7
303.15	3030.00	1110.1
303.15	5040.00	1111.0
303.15	6950.00	1111.9
303.15	9960.00	1113.2
303.15	14840.00	1115.4
303.15	19740.00	1117.5
303.15	24680.00	1119.6
303.15	29610.00	1121.6
303.15	34520.00	1123.6
303.15	39380.00	1125.6
303.15	44350.00	1127.5
303.15	49140.00	1129.4
303.15	54090.00	1131.3
303.15	58990.00	1133.1
303.15	63850.00	1134.9
303.15	68760.00	1136.6
313.15	100.00	1101.7
313.15	100.00	1101.6
313.15	640.00	1101.8
313.15	1140.00	1102.1
313.15	1640.00	1102.3
313.15	2100.00	1102.5
313.15	3090.00	1103.0
313.15	5130.00	1103.9
313.15	6960.00	1104.8
313.15	9960.00	1106.1
313.15	14940.00	1108.4
313.15	19750.00	1110.6
313.15	24640.00	1112.7
313.15	29640.00	1114.8
313.15	34510.00	1116.9
313.15	39340.00	1118.9
313.15	44340.00	1120.9
313.15	49190.00	1123.2
313.15	54020.00	1124.7
313.15	59030.00	1126.7
313.15	63880.00	1128.5
313.15	68820.00	1130.3
323.15	100.00	1094.3
323.15	100.00	1094.3
323.15	680.00	1094.6
323.15	1130.00	1094.8
323.15	1570.00	1095.0
323.15	2100.00	1095.2
323.15	3080.00	1095.7
323.15	5080.00	1096.7
323.15	7000.00	1097.6
323.15	9950.00	1099.0
323.15	14890.00	1101.4
323.15	19770.00	1103.6
323.15	24680.00	1105.8
323.15	29600.00	1108.0
323.15	34530.00	1110.1
323.15	39360.00	1112.2
323.15	44290.00	1114.3
323.15	49260.00	1116.3
323.15	54100.00	1118.2
323.15	59060.00	1120.2
323.15	63880.00	1122.0
323.15	68770.00	1123.8
333.15	100.00	1087.0
333.15	100.00	1087.0
333.15	660.00	1087.3
333.15	1120.00	1087.5
333.15	1630.00	1087.8
333.15	2100.00	1088.0
333.15	3070.00	1088.5
333.15	5060.00	1089.5
333.15	7050.00	1090.5
333.15	9930.00	1091.9
333.15	14780.00	1094.3
333.15	19770.00	1096.7
333.15	24660.00	1099.0
333.15	29540.00	1101.2
333.15	34500.00	1103.4
333.15	39330.00	1105.5
333.15	44230.00	1107.6
333.15	49130.00	1109.7
333.15	54060.00	1111.7
333.15	59020.00	1113.7
333.15	63840.00	1115.7
333.15	68830.00	1117.5
343.15	100.00	1079.7
343.15	100.00	1079.7
343.15	670.00	1080.0
343.15	1100.00	1080.2
343.15	1520.00	1080.4
343.15	2120.00	1080.7
343.15	3060.00	1081.2
343.15	5040.00	1082.3
343.15	6970.00	1083.3
343.15	9950.00	1084.8
343.15	14870.00	1087.3
343.15	19740.00	1089.6
343.15	24710.00	1092.1
343.15	29560.00	1094.4
343.15	34490.00	1096.6
343.15	39350.00	1098.8
343.15	44290.00	1101.0
343.15	49180.00	1103.1
343.15	54070.00	1105.2
343.15	58980.00	1107.3
343.15	63910.00	1109.3
343.15	68720.00	1111.2
353.15	100.00	1072.2
353.15	100.00	1072.2
353.15	560.00	1072.5
353.15	1090.00	1072.8
353.15	1550.00	1073.0
353.15	2080.00	1073.3
353.15	3040.00	1073.8
353.15	5060.00	1074.9
353.15	7020.00	1076.0
353.15	9970.00	1077.5
353.15	14830.00	1080.1
353.15	19740.00	1082.6
353.15	24680.00	1085.1
353.15	29560.00	1087.5
353.15	34550.00	1089.8
353.15	39420.00	1092.1
353.15	44280.00	1094.3
353.15	49230.00	1096.5
353.15	54110.00	1098.7
353.15	59020.00	1100.8
353.15	64010.00	1102.9
353.15	68770.00	1104.8
363.08	100.00	1064.5
363.08	100.00	1064.4
363.08	620.00	1064.7
363.08	1110.00	1065.0
363.08	1570.00	1065.2
363.08	2100.00	1065.5
363.08	3020.00	1066.0
363.08	5070.00	1067.2
363.08	7000.00	1068.3
363.08	9970.00	1069.9
363.08	14840.00	1072.6
363.08	19750.00	1075.1
363.08	24660.00	1077.7
363.08	29610.00	1080.2
363.08	34480.00	1082.6
363.08	39400.00	1084.9
363.08	44290.00	1087.2
363.08	49160.00	1089.5
363.08	54110.00	1091.7
363.08	58990.00	1093.9
363.08	63880.00	1096.0
363.08	68760.00	1098.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	989.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[99.88; 319.79]	J/mol×K	[200.00; 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			8.21070e+01
Coefficient B			-6.87160e+02
Coefficient C			6.44524e+00
Coefficient D			-7.06470e-04
Coefficient E			2.41550e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	99.88	J/mol×K	200.00	Calculated Property
Cp,gas	151.21	J/mol×K	344.44	Calculated Property
Cp,gas	197.93	J/mol×K	488.89	Calculated Property
Cp,gas	231.97	J/mol×K	633.33	Calculated Property
Cp,gas	255.99	J/mol×K	777.78	Calculated Property
Cp,gas	273.45	J/mol×K	922.22	Calculated Property
Cp,gas	286.96	J/mol×K	1066.67	Calculated Property
Cp,gas	298.38	J/mol×K	1211.11	Calculated Property
Cp,gas	309.01	J/mol×K	1355.56	Calculated Property
Cp,gas	319.79	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[231.86; 315.30]	J/mol×K	[262.70; 513.15]	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			1.88290e+02
Coefficient B			2.27630e+02
Coefficient C			-1.19206e+00
Coefficient D			2.05450e-02
Coefficient E			-1.87980e-05
Temperature range, min.			262.70
Temperature range, max.			513.15
Cp,liquid	231.86	J/mol×K	262.70	Calculated Property
Cp,liquid	241.47	J/mol×K	290.53	Calculated Property
Cp,liquid	252.26	J/mol×K	318.36	Calculated Property
Cp,liquid	263.86	J/mol×K	346.18	Calculated Property
Cp,liquid	275.74	J/mol×K	374.01	Calculated Property
Cp,liquid	287.26	J/mol×K	401.84	Calculated Property
Cp,liquid	297.67	J/mol×K	429.67	Calculated Property
Cp,liquid	306.24	J/mol×K	457.49	Calculated Property
Cp,liquid	312.29	J/mol×K	485.32	Calculated Property
Cp,liquid	315.30	J/mol×K	513.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.2747642; 0.0001339]	Pa×s	[262.70; 595.68]	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			-3.74290e+02
Coefficient B			1.81920e+04
Coefficient C			5.51320e+01
Coefficient D			-4.91660e-05
Coefficient E			2.00000e+00
Temperature range, min.			262.70
Temperature range, max.			595.68
η	0.2747642	Pa×s	262.70	Calculated Property
η	0.0273371	Pa×s	299.70	Calculated Property
η	0.0066732	Pa×s	336.70	Calculated Property
η	0.0027302	Pa×s	373.69	Calculated Property
η	0.0014870	Pa×s	410.69	Calculated Property
η	0.0009325	Pa×s	447.69	Calculated Property
η	0.0006126	Pa×s	484.69	Calculated Property
η	0.0003958	Pa×s	521.68	Calculated Property
η	0.0002408	Pa×s	558.68	Calculated Property
η	0.0001339	Pa×s	595.68	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[89.39; 0.00]	kJ/mol	[262.70; 744.60]	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			1.08530e+02
Coefficient B			-8.76655e-03
Coefficient C			1.77095e+00
Coefficient D			-1.35989e+00
Coefficient E			-2.10292e-02
Critical temperature, Tc (K)			7.44600e+02
Temperature range, min.			262.70
Temperature range, max.			744.60
ΔvapH	89.39	kJ/mol	262.70	Calculated Property
ΔvapH	82.48	kJ/mol	316.24	Calculated Property
ΔvapH	75.29	kJ/mol	369.79	Calculated Property
ΔvapH	68.09	kJ/mol	423.33	Calculated Property
ΔvapH	61.07	kJ/mol	476.88	Calculated Property
ΔvapH	54.34	kJ/mol	530.42	Calculated Property
ΔvapH	47.88	kJ/mol	583.97	Calculated Property
ΔvapH	41.36	kJ/mol	637.51	Calculated Property
ΔvapH	33.49	kJ/mol	691.06	Calculated Property
ΔvapH	0.00	kJ/mol	744.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[396.81; 548.09]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.56166e+01
Coefficient B			-4.75686e+03
Coefficient C			-8.64930e+01
Temperature range, min.			396.81
Temperature range, max.			548.09
Pvap	1.33	kPa	396.81	Calculated Property
Pvap	2.93	kPa	413.62	Calculated Property
Pvap	5.97	kPa	430.43	Calculated Property
Pvap	11.36	kPa	447.24	Calculated Property
Pvap	20.44	kPa	464.05	Calculated Property
Pvap	34.97	kPa	480.85	Calculated Property
Pvap	57.26	kPa	497.66	Calculated Property
Pvap	90.19	kPa	514.47	Calculated Property
Pvap	137.28	kPa	531.28	Calculated Property
Pvap	202.64	kPa	548.09	Calculated Property
Pvap	[8.39e-06; 2556.62]	kPa	[262.70; 744.60]	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			3.93582e+01
Coefficient B			-1.02051e+04
Coefficient C			-2.10272e+00
Coefficient D			-7.03647e-06
Coefficient E			2.00000e+00
Temperature range, min.			262.70
Temperature range, max.			744.60
Pvap	8.39e-06	kPa	262.70	Calculated Property
Pvap	3.28e-03	kPa	316.24	Calculated Property
Pvap	0.20	kPa	369.79	Calculated Property
Pvap	3.57	kPa	423.33	Calculated Property
Pvap	29.67	kPa	476.88	Calculated Property
Pvap	140.76	kPa	530.42	Calculated Property
Pvap	441.00	kPa	583.97	Calculated Property
Pvap	1004.40	kPa	637.51	Calculated Property
Pvap	1776.37	kPa	691.06	Calculated Property
Pvap	2556.62	kPa	744.60	Calculated Property
Pvap	[1.07e-05; 4415.80]	kPa	[262.70; 744.60]	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			1.08791e+02
Coefficient B			-1.28556e+04
Coefficient C			-1.28373e+01
Coefficient D			3.16995e-06
Coefficient E			0.00000e+00
Temperature range, min.			262.70
Temperature range, max.			744.60
Pvap	1.07e-05	kPa	262.70	Calculated Property
Pvap	4.34e-03	kPa	316.24	Calculated Property
Pvap	0.24	kPa	369.79	Calculated Property
Pvap	3.86	kPa	423.33	Calculated Property
Pvap	29.48	kPa	476.88	Calculated Property
Pvap	135.63	kPa	530.42	Calculated Property
Pvap	439.99	kPa	583.97	Calculated Property
Pvap	1115.30	kPa	637.51	Calculated Property
Pvap	2367.36	kPa	691.06	Calculated Property
Pvap	4415.80	kPa	744.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1139.68; 614.48]	kg/m3	[262.70; 719.24]	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			8.69062e+01
Coefficient B			2.58230e-01
Coefficient C			7.44600e+02
Coefficient D			2.39790e-01
Temperature range, min.			262.70
Temperature range, max.			719.24
ρl	1139.68	kg/m3	262.70	Calculated Property
ρl	1103.67	kg/m3	313.43	Calculated Property
ρl	1065.59	kg/m3	364.15	Calculated Property
ρl	1024.95	kg/m3	414.88	Calculated Property
ρl	981.10	kg/m3	465.61	Calculated Property
ρl	933.00	kg/m3	516.33	Calculated Property
ρl	878.99	kg/m3	567.06	Calculated Property
ρl	815.95	kg/m3	617.79	Calculated Property
ρl	736.75	kg/m3	668.51	Calculated Property
ρl	614.48	kg/m3	719.24	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.03]	N/m	[262.75; 519.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			7.10072e-02
Coefficient B			-8.80000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			262.75
Temperature range, max.			519.15
γ	0.05	N/m	262.75	Calculated Property
γ	0.05	N/m	291.24	Calculated Property
γ	0.04	N/m	319.73	Calculated Property
γ	0.04	N/m	348.22	Calculated Property
γ	0.04	N/m	376.71	Calculated Property
γ	0.04	N/m	405.19	Calculated Property
γ	0.03	N/m	433.68	Calculated Property
γ	0.03	N/m	462.17	Calculated Property
γ	0.03	N/m	490.66	Calculated Property
γ	0.03	N/m	519.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.08]	W/m×K	[262.70; 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			5.00160e+02
Coefficient B			1.02760e+00
Coefficient C			7.96170e+09
Coefficient D			-7.52580e+11
Temperature range, min.			262.70
Temperature range, max.			1000.00
λgas	0.01	W/m×K	262.70	Calculated Property
λgas	0.01	W/m×K	344.62	Calculated Property
λgas	0.02	W/m×K	426.54	Calculated Property
λgas	0.02	W/m×K	508.47	Calculated Property
λgas	0.03	W/m×K	590.39	Calculated Property
λgas	0.04	W/m×K	672.31	Calculated Property
λgas	0.05	W/m×K	754.23	Calculated Property
λgas	0.06	W/m×K	836.16	Calculated Property
λgas	0.07	W/m×K	918.08	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.20; 0.19]	W/m×K	[262.70; 517.95]	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			-1.15790e-01
Coefficient B			8.22460e+00
Coefficient C			-1.64660e+00
Coefficient D			2.67300e-03
Coefficient E			-3.54120e-06
Temperature range, min.			262.70
Temperature range, max.			517.95
λliquid	0.20	W/m×K	262.70	Calculated Property
λliquid	0.20	W/m×K	291.06	Calculated Property
λliquid	0.21	W/m×K	319.42	Calculated Property
λliquid	0.21	W/m×K	347.78	Calculated Property
λliquid	0.21	W/m×K	376.14	Calculated Property
λliquid	0.21	W/m×K	404.51	Calculated Property
λliquid	0.21	W/m×K	432.87	Calculated Property
λliquid	0.20	W/m×K	461.23	Calculated Property
λliquid	0.19	W/m×K	489.59	Calculated Property
λliquid	0.19	W/m×K	517.95	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol, 2,2'-oxybis-.

Mixtures

• Thiophene + Heptane + Ethanol, 2,2'-oxybis-
• Benzo[b]thiophene + Heptane + Ethanol, 2,2'-oxybis-
• Heptane + Ethanol, 2,2'-oxybis-
• Ethanol, 2,2'-oxybis- + Water
• Ethanol, 2,2'-oxybis- + Methyl Alcohol + Water
• Formaldehyde + Ethanol, 2,2'-oxybis- + Water
• Methane, dimethoxy- + Ethanol, 2,2'-oxybis- + Water
• Ethanol, 2,2'-oxybis- + Dibenzothiophene
• Magnesium chloride + Ethanol, 2,2'-oxybis- + Water
• Ethanol, 2-propoxy- + Ethanol, 2,2'-oxybis-
• 1,2-Ethanediol + Ethanol, 2,2'-oxybis-
• Triethylene glycol + Ethanol, 2,2'-oxybis-
• 1,2-Ethanediol + Triethylene glycol + Ethanol, 2,2'-oxybis-
• Ethanol, 2,2'-oxybis- + Lithium chloride + Water
• lithium bromide + Ethanol, 2,2'-oxybis- + Water
• Carbon dioxide + Ethanol, 2,2'-oxybis-
• Glycerin + Ethanol, 2,2'-oxybis- + Water
• Choline chloride + Ethanol, 2,2'-oxybis-
• Choline chloride + Carbon dioxide + Ethanol, 2,2'-oxybis-
• Ethanol, 2,2'-oxybis- + Tromethamine + Water

Find more mixtures with Ethanol, 2,2'-oxybis-.

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).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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.
• Cheméo Relay (1.0)
• 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
• Application of the Multi-Current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols
• Thermophysical Properties For Diethylene Glycol + Nitrobenzene and Triethylene Glycol + (Chloro-, Bromo-, Nitro-) Benzene Systems at Different Temperatures
• Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
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• Mutual diffusion coefficients of aqueous solutions of some glycols
• Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 465 K and at high pressures up to 245 MPa
• The effect of the end group, molecular weight and size on the solubility of compounds in supercritical carbon dioxide
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• Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study
• Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
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• Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
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• Densities and vapor pressures of mixed-solvent desiccant systems containing {glycol (diethylene, or triethylene, or tetraethylene glycol) + salt (magnesium chloride) + water}
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• Solubilities and thermodynamic properties of CO2 in choline-chloride based deep eutectic solvents
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• Partial molar volumes of organic solutes in water. XXVIII. Three aliphatic poly(ethylene glycols) at temperatures T = 298 K 573 K and pressures up to 30 MPa
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• Binary and ternary solid-liquid phase equilibrium for the systems formed by succinic acid, urea and diethylene glycol: Determination and modelling
• Measurement and correlation of physicochemical properties of phosphonium-based deep eutectic solvents at several temperatures (293.15 K - 343.15 K) for CO2 capture
• Densities and viscosities for binary mixtures of polyoxymethylene dimethyl ethers with different CH2O chain length n = 2, 3, 4 at different temperatures
• Thermal stability analysis, experimental conductivity and pH of phosphonium-based deep eutectic solvents and their prediction by a new empirical equation
• Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
• Phase equilibria study on bromide-based ionic liquids with glycols and sulfolane. Experimental data and correlation
• Volumetric and ultrasonic studies on interactions of ethylene glycol, diethylene glycol and triethylene glycol in aqueous solutions of glycerol at temperatures T = (293.15 K - 308.15) K
• Acoustic and thermodynamic study of D-Panthenol in aqueous solutions of glycol at different temperatures
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• Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
• Heat Capacity of Several Mixed-Solvent Desiccants Containing Glycol + Water + MgCl2
• Molar heat capacity of several aqueous solutions of n-[tris(hydroxymethyl)methyl-3-amino]- propanesulfonic acid (TAPS) + glycol
• Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Four Poly(Ethylene Glycols) at Infinite Dilution in Water at Temperatures T = (278 to 343) K and Atmospheric Pressure
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• Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
• Investigation on Temperature-Dependent Volumetric and Acoustical Properties of Homologous Series of Glycols in Aqueous Sorbitol Solutions
• Solubility of Carbon Dioxide in Poly(oxymethylene) Dimethyl Ethers
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• Thermodynamic and Kinetic Studies of CO2 Capture by Glycol and Amine-Based Deep Eutectic Solvents
• Thermodynamic Interactions Study of Some Ethylene Glycols in Aqueous Aniline Solutions at Different Temperatures: An Acoustical and Volumetric Approach
• Solubility of Acetylene in Alcohols and Ketones
• Effect of Ethylene, Diethylene, and Triethylene Glycols and Glycerol on the Physicochemical Properties and Phase Behavior of Benzyltrimethyl and Benzyltributylammonium Chloride Based Deep Eutectic Solvents at 283.15-343.15 K
• Measurement and Thermodynamic Models for Ternary Liquid-Liquid Equilibrium Systems {Water + Polyoxymethylene Dimethyl Ethers +4-Methyl-2-pentanol} at Different Temperatures
• Experimental Isobaric Vapor Liquid Equilibrium for Binary Systems Diethylene Glycol Dibenzoate + Diethylene Glycol, Diethylene Glycol Dibenzoate + Octyl Benzoate, and Ternary System Diethylene Glycol Dibenzoate + Diethylene Glycol + Octyl Benzoate at 1.0152 kPa
• Liquid-Liquid Equilibrium for Ternary Systems of Polyoxymethylene Dimethyl Ethers + o-Xylene + Water at 293.15 K
• Solubility of 4-Chloro-2,5-dimethoxynitrobenzene, 4-Chloro-2,5-dimethoxyaniline, and 2,5-Dimethoxyaniline in Binary and Pure Solvents: Determination and Modeling
• Salting Effect of Sodium Hydroxide and Sodium Formate on the Liquid-Liquid Equilibrium of Polyoxymethylene Dimethyl Ethers in Aqueous Solution
• Heat Capacity and Phase Behavior of Selected Oligo(ethylene glycol)s
• Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
• Experimental and Correlated Liquid-Liquid Equilibrium Data for Ternary Systems (Water + Poly(oxymethylene) Dimethyl Ethers + Toluene) at T = 293.15 and 303.15 K and p = 101.3 kPa
• Densities, Viscosities, and Excess Properties for Binary Mixtures of Some Glycols and Polyglycols in N-Methylacetamide at 308.15 K
• Density, Viscosity and Thermal Conductivity of Aqueous Ethylene, Diethylene and Triethylene Glycol Mixtures between 290 K and 450 K
• Excess Molar Enthalpies of Binary Mixtures Containing Glycols or Polyglycols + Dimethyl Sulfoxide at 308.15 K
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
• Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
• Liquid-Liquid Equilibrium for the System Heptane + o-Xylene + Diethylene Glycol over the Temperature Range of 288.15 K to 318.15 K
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
• Solubility of Ethane in Diethylene Glycol
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
• Densities, Viscosities, and Surface Tensions of the System Water + Diethylene Glycol
• Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
• Measurement and Correlation of the Solubility of Disodium 4,4?-Dinitrostilbene-2,2?-disulfonate in Aqueous Organic Solutions
• Measurement and Prediction of Excess Enthalpies for Ternary Solutions 1-Ethyl-3-methylimidazolium Dimethylphosphate + Methanol or Ethanol + Water at 298.15 K and at Normal Atmospheric Pressure
• Isobaric Vapor-Liquid Equilibrium for Four Binary Systems of Ethane-1,2-diol, Butane-1,4-diol, 2-(2- Hydroxyethoxy)ethan-1-ol and 2-[2-(2- Hydroxyethoxy)ethoxy]ethanol at 10.0 kPa, 20.0 kPa and 40.0 kPa
• Solubility of CO2 in Nonaqueous Absorption System of 2-(2-Aminoethylamine)ethanol + Benzyl Alcohol
• Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
• Liquid-Liquid Equilibria of (Limonene + Linalool + Ethylene Glycol or Diethylene Glycol or Triethylene Glycol or 1,2-Propylene Glycol) Ternary Systems
• Supplementary Densities and Viscosities of Aqueous Solutions of Diethylene Glycol from (283.15 to 353.15) K
• Solubility Comparison of Bis(2-hydroxyethyl) Ether and Tetraethylene Glycol before and after End-Group Modification by Ethyl Oxalyl Chloride in Supercritical Carbon Dioxide
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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