Chemical Properties of Ethanol, 2-methoxy- (CAS 109-86-4)

InChI

InChI=1S/C3H8O2/c1-5-3-2-4/h4H,2-3H2,1H3

InChI Key

XNWFRZJHXBZDAG-UHFFFAOYSA-N

Formula

C3H8O2

SMILES

COCCO

Molecular Weight¹

76.09

CAS

109-86-4

Other Names

• 1,2-ethanediol, methyl ether
• 1,2-ethanediol, monomethyl ether
• 1-Hydroxy-2-methoxyethane
• 2-Hydroxyethyl methyl ether
• 2-Methoxy-aethanol
• 2-Methoxyethyl alcohol
• 2-Metossietanolo
• 2-methoxy-1-ethanol
• 2-methoxyethan-1-ol
• 2-methoxyethanol
• 2-methoxyethanol (methyl cellosolve)
• 3-oxa-1-butanol
• Aethylenglykol-monomethylaether
• Amsco-Solv EE
• Dowanol EM
• EGM
• EGME
• Ektasolve EM
• Ether monomethylique de l'ethylene-glycol
• Ethylene glycol monomethyl ether
• Glycol ether EM
• Glycol monomethyl ether
• Glycolmethyl ether
• HOCH2CH2OCH3
• Jeffersol EM
• MECS
• Methoxyethanol
• Methoxyethylene glycol
• Methoxyhydroxyethane
• Methyl cellosolve
• Methyl ethoxol
• Methyl glycol
• Methyl icinol
• Methyl oxitol
• Methylcelosolv
• Methylglykol
• Metil cellosolve
• Metoksyetylowy alkohol
• Monoethylene glycol methyl ether
• Monomethyl ether of ethylene glycol
• Monomethyl glycol
• NSC 1258
• Poly-Solv EM
• Prist
• UN 1188
• ethylene glycol methyl ether
• ethylene glycol, monomethyl ether
• «beta»-Methoxyethanol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• 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).
• 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_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.4411		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
PAff	768.80	kJ/mol	NIST
Tig	508.15	K	NCMS SOLV-DB
BasG	729.80	kJ/mol	NIST
ΔcH°liquid	-1880.00	kJ/mol	NIST
η	0.0015119	Pa×s	Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
Tflash,cc	316.15	K	NCMS SOLV-DB
ΔfG°	-267.44	kJ/mol	Joback Calculated Property
ΔfH°gas	[-395.90; -376.90]	kJ/mol
ΔfH°gas	-376.90 ± 8.10	kJ/mol	NIST
ΔfH°gas	-395.90	kJ/mol	NIST
ΔfH°liquid	[-441.00; -422.00]	kJ/mol
ΔfH°liquid	-422.00 ± 7.60	kJ/mol	NIST
ΔfH°liquid	-441.00	kJ/mol	NIST
ΔfusH°	8.80	kJ/mol	Joback Calculated Property
ΔvapH°	[45.10; 45.20]	kJ/mol
ΔvapH°	45.20	kJ/mol	NIST
ΔvapH°	45.10	kJ/mol	NIST
ΔvapH°	45.20 ± 0.20	kJ/mol	NIST
IE	10.13	eV	NIST
log10WS	1.19		Relay (1.0) Calculated Property
logPoct/wat	-0.770		NCMS SOLV-DB
McVol	64.870	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[3600.00; 5285.00]	kPa
Pc	5280.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	5285.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5285.00 ± 20.00	kPa	NIST
Pc	3600.00 ± 5.00	kPa	NIST
ρc	[289.16; 306.66]	kg/m3
ρc	289.16 ± 6.85	kg/m3	NIST
ρc	306.66 ± 3.04	kg/m3	NIST
Inp	[588.00; 646.00]
Inp	630.00		NIST
Inp	Outlier 588.00		NIST
Inp	591.00		NIST
Inp	595.00		NIST
Inp	617.00		NIST
Inp	624.00		NIST
Inp	635.00		NIST
Inp	629.00		NIST
Inp	629.00		NIST
Inp	618.00		NIST
Inp	646.00		NIST
Inp	626.00		NIST
Inp	623.00		NIST
Inp	616.00		NIST
Inp	635.30		NIST
Inp	617.00		NIST
Inp	617.00		NIST
Inp	616.00		NIST
Inp	616.00		NIST
Inp	617.00		NIST
Ip	[1172.00; 1225.00]
Ip	1184.00		NIST
Ip	Outlier 1225.00		NIST
Ip	1180.00		NIST
Ip	1202.00		NIST
Ip	1199.00		NIST
Ip	1199.00		NIST
Ip	1172.00		NIST
Ip	1180.00		NIST
Tboil	[397.30; 397.75]	K
Tboil	397.63	K	Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
Tboil	397.67	K	Isobaric vapor-liquid equilibrium data for methylcyclohexane + 2-methoxyethanol and methylcyclohexane + 2-ethoxyethanol at 50.00 and 101.33 kPa
Tboil	397.67	K	Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
Tboil	397.58	K	Evaluation of the 2-Methoxyethanol as Entrainer in Ethanol Water and 1-Propanol Water Mixtures
Tboil	397.75	K	NCMS SOLV-DB
Tboil	397.60 ± 0.40	K	NIST
Tboil	397.50 ± 0.50	K	NIST
Tboil	397.70	K	NIST
Tboil	Outlier 397.30	K	NIST
Tboil	397.65 ± 0.40	K	NIST
Tboil	397.36 ± 0.20	K	NIST
Tboil	397.65	K	NIST
Tboil	397.70 ± 0.50	K	NIST
Tboil	397.60 ± 1.00	K	NIST
Tc	[571.00; 597.60]	K
Tc	597.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	597.60	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	597.60 ± 0.20	K	NIST
Tc	571.00 ± 2.00	K	NIST
Tfus	[188.05; 188.15]	K
Tfus	188.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	188.05	K	NCMS SOLV-DB
Tfus	188.05	K	NIST
Vc	[0.263; 0.263]	m3/kmol
Vc	0.263	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.263	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vm	7.93e-05	m3/mol	Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
Zc	0.2790000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[174.90; 176.60]	J/mol×K	[298.15; 298.15]
Cp,liquid	175.38	J/mol×K	298.15	NIST
Cp,liquid	176.60	J/mol×K	298.15	NIST
Cp,liquid	174.90	J/mol×K	298.15	NIST
η	[0.0010470; 0.0017080]	Pa×s	[293.15; 318.15]
η	0.0017080	Pa×s	293.15	Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
η	0.0015440	Pa×s	298.15	Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
η	0.0015920	Pa×s	298.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
η	0.0015430	Pa×s	298.15	Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
η	0.0015430	Pa×s	298.15	Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
η	0.0015700	Pa×s	298.15	NCMS SOLV-DB
η	0.0014040	Pa×s	303.15	Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
η	0.0012420	Pa×s	308.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
η	0.0012560	Pa×s	308.15	Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
η	0.0012570	Pa×s	308.15	Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
η	0.0010470	Pa×s	318.15	Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
η	0.0010510	Pa×s	318.15	Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
ΔvapH	[37.54; 43.00]	kJ/mol	[273.00; 397.30]
ΔvapH	41.30	kJ/mol	273.00	NIST
ΔvapH	42.90	kJ/mol	362.50	NIST
ΔvapH	43.00	kJ/mol	371.50	NIST
ΔvapH	42.80	kJ/mol	378.00	NIST
ΔvapH	37.54	kJ/mol	397.30	NIST
Pvap	[1.27; 176.50]	kPa	[298.15; 416.60]
Pvap	1.27	kPa	298.15	NCMS SOLV-DB
Pvap	15.00	kPa	346.40	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	23.50	kPa	356.90	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	28.10	kPa	364.15	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	32.00	kPa	364.70	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	34.20	kPa	368.84	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	41.30	kPa	373.48	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	49.00	kPa	376.00	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	47.90	kPa	377.22	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	53.70	kPa	380.17	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	57.50	kPa	380.60	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	60.50	kPa	383.30	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	66.00	kPa	384.50	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	68.60	kPa	386.66	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	74.50	kPa	388.10	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	76.40	kPa	389.59	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	81.20	kPa	391.28	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	83.00	kPa	391.30	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	88.70	kPa	393.75	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	91.50	kPa	394.40	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	95.30	kPa	395.78	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	100.00	kPa	397.20	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	101.30	kPa	397.58	Evaluation of the 2-Methoxyethanol as Entrainer in Ethanol Water and 1-Propanol Water Mixtures
Pvap	101.30	kPa	397.67	Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
Pvap	108.50	kPa	400.10	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	117.00	kPa	402.60	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	125.50	kPa	404.90	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	134.00	kPa	407.00	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	142.50	kPa	409.10	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	151.00	kPa	411.10	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	159.50	kPa	412.90	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	168.00	kPa	414.70	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	176.50	kPa	416.60	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
n0	[1.39830; 1.40300]		[298.15; 303.15]
n0	1.40020		298.15	Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether isopropyl alcohol azeotropic mixture
n0	1.40040		298.15	Non-ideal behaviour of a room temperature ionic liquid in an alkoxyethanol or poly ethers at T = (298.15 to 318.15) K
n0	1.40040		298.15	Physical and excess properties of a room temperature ionic liquid (1-methyl-3-octylimidazolium tetrafluoroborate) with n-alkoxyethanols (C1Em, m = 1 to 3) at T = (298.15 to 318.15) K
n0	1.40020		298.15	Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
n0	1.40030		298.15	Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
n0	1.40060		298.15	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
n0	1.40300		298.15	NCMS SOLV-DB
n0	1.39830		303.15	Densities, Viscosities, Sound Speeds, Refractive Indices, and Excess Properties of Binary Mixtures of Isoamyl Alcohol with Some Alkoxyethanols
ρl	[898.55; 974.70]	kg/m3	[283.15; 363.15]
ρl	974.70	kg/m3	283.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	969.90	kg/m3	288.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	966.52	kg/m3	291.15	Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
ρl	964.70	kg/m3	293.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	964.70	kg/m3	293.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	964.86	kg/m3	293.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρl	964.88	kg/m3	293.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρl	965.20	kg/m3	293.15	Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
ρl	964.88	kg/m3	293.15	Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
ρl	964.70	kg/m3	293.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	960.20	kg/m3	298.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	960.31	kg/m3	298.15	Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
ρl	959.73	kg/m3	298.15	Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
ρl	960.20	kg/m3	298.15	Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
ρl	960.10	kg/m3	298.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	960.29	kg/m3	298.15	Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
ρl	960.10	kg/m3	298.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	960.29	kg/m3	298.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρl	960.32	kg/m3	298.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	960.90	kg/m3	298.15	Study of molecular interactions in binary liquid mixtures of [Emim][BF4] with 2-methoxyethanol using thermo acoustic, volumetric and optical properties
ρl	960.29	kg/m3	298.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	960.01	kg/m3	298.15	Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
ρl	960.89	kg/m3	298.15	Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
ρl	960.10	kg/m3	298.15	Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
ρl	960.32	kg/m3	298.15	Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
ρl	955.84	kg/m3	303.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	955.72	kg/m3	303.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	956.73	kg/m3	303.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	955.71	kg/m3	303.15	Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
ρl	955.50	kg/m3	303.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	955.50	kg/m3	303.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	955.68	kg/m3	303.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρl	955.50	kg/m3	303.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	955.76	kg/m3	303.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρl	955.71	kg/m3	303.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	955.76	kg/m3	303.15	Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
ρl	951.70	kg/m3	308.15	Study of molecular interactions in binary liquid mixtures of [Emim][BF4] with 2-methoxyethanol using thermo acoustic, volumetric and optical properties
ρl	951.11	kg/m3	308.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	950.90	kg/m3	308.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	952.09	kg/m3	308.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	951.08	kg/m3	308.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	951.10	kg/m3	308.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρl	950.90	kg/m3	308.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	951.16	kg/m3	308.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	951.08	kg/m3	308.15	Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
ρl	951.10	kg/m3	308.15	Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
ρl	950.90	kg/m3	308.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	946.38	kg/m3	313.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρl	946.20	kg/m3	313.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	947.42	kg/m3	313.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	946.41	kg/m3	313.15	Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
ρl	946.20	kg/m3	313.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	946.54	kg/m3	313.15	Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
ρl	946.49	kg/m3	313.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	946.27	kg/m3	313.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	946.42	kg/m3	313.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	946.20	kg/m3	313.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	941.50	kg/m3	318.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	941.89	kg/m3	318.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	941.50	kg/m3	318.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	941.72	kg/m3	318.15	Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
ρl	942.72	kg/m3	318.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	941.50	kg/m3	318.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	941.72	kg/m3	318.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	942.70	kg/m3	318.15	Study of molecular interactions in binary liquid mixtures of [Emim][BF4] with 2-methoxyethanol using thermo acoustic, volumetric and optical properties
ρl	941.64	kg/m3	318.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	936.95	kg/m3	323.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρl	936.88	kg/m3	323.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	936.89	kg/m3	323.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	936.70	kg/m3	323.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	936.99	kg/m3	323.15	Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
ρl	936.70	kg/m3	323.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	936.80	kg/m3	323.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	937.98	kg/m3	323.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	932.00	kg/m3	328.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	933.21	kg/m3	328.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	932.00	kg/m3	328.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	932.00	kg/m3	328.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	933.40	kg/m3	328.15	Study of molecular interactions in binary liquid mixtures of [Emim][BF4] with 2-methoxyethanol using thermo acoustic, volumetric and optical properties
ρl	927.38	kg/m3	333.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρl	927.20	kg/m3	333.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	927.20	kg/m3	333.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	928.39	kg/m3	333.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	927.20	kg/m3	333.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	923.54	kg/m3	338.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	922.30	kg/m3	338.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	922.40	kg/m3	338.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	917.50	kg/m3	343.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	917.64	kg/m3	343.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρl	917.40	kg/m3	343.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	918.64	kg/m3	343.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	913.69	kg/m3	348.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	912.50	kg/m3	348.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	912.40	kg/m3	348.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	907.50	kg/m3	353.15	Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
ρl	908.70	kg/m3	353.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	907.40	kg/m3	353.15	Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
ρl	903.65	kg/m3	358.15	Surface tension of four oxygenated fuels: experiment and correlation
ρl	898.55	kg/m3	363.15	Surface tension of four oxygenated fuels: experiment and correlation
csound,fluid	[1260.70; 1380.00]	m/s	[288.15; 323.15]
csound,fluid	1376.47	m/s	288.15	Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
csound,fluid	1380.00	m/s	288.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
csound,fluid	1359.23	m/s	293.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
csound,fluid	1359.04	m/s	293.15	Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
csound,fluid	1367.00	m/s	293.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
csound,fluid	1341.72	m/s	298.15	Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
csound,fluid	1341.58	m/s	298.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
csound,fluid	1351.00	m/s	298.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
csound,fluid	1324.20	m/s	303.15	Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
csound,fluid	1324.50	m/s	303.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1324.47	m/s	303.15	Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
csound,fluid	1337.00	m/s	303.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
csound,fluid	1324.29	m/s	303.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
csound,fluid	1321.00	m/s	308.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
csound,fluid	1312.60	m/s	308.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1307.14	m/s	308.15	Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
csound,fluid	1299.60	m/s	313.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1304.00	m/s	313.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
csound,fluid	1293.90	m/s	313.15	Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
csound,fluid	1289.95	m/s	313.15	Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
csound,fluid	1287.20	m/s	318.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1287.00	m/s	318.15	Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
csound,fluid	1272.81	m/s	318.15	Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
csound,fluid	1260.70	m/s	323.15	Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
γ	[0.03; 0.03]	N/m	[298.15; 318.15]
γ	0.03	N/m	298.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
γ	0.03	N/m	298.15	Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	308.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
γ	0.03	N/m	313.15	Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
γ	0.03	N/m	318.15	Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K

Datasets

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

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	20000.00	0.0019
293.15	40000.00	0.0022
293.15	60000.00	0.0024
293.15	80000.00	0.0027
293.15	100000.00	0.0029
303.15	20000.00	0.0016
303.15	40000.00	0.0018
303.15	60000.00	0.0020
303.15	80000.00	0.0022
303.15	100000.00	0.0024
313.15	20000.00	0.0013
313.15	40000.00	0.0015
313.15	60000.00	0.0016
313.15	80000.00	0.0018
313.15	100000.00	0.0020
323.15	20000.00	0.0011
323.15	40000.00	0.0013
323.15	60000.00	0.0014
323.15	80000.00	0.0015
323.15	100000.00	0.0017
333.15	20000.00	0.0010
333.15	40000.00	0.0011
333.15	60000.00	0.0012
333.15	80000.00	0.0013
333.15	100000.00	0.0015
343.15	20000.00	0.0009
343.15	40000.00	0.0010
343.15	60000.00	0.0011
343.15	80000.00	0.0011
343.15	100000.00	0.0012
353.15	20000.00	0.0007
353.15	40000.00	0.0008
353.15	60000.00	0.0009
353.15	80000.00	0.0010
353.15	100000.00	0.0011
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	303.15	0.0014
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	964.5
293.15	5000.00	967.5
293.15	10000.00	970.7
293.15	15000.00	973.8
293.15	20000.00	976.6
293.15	25000.00	979.5
293.15	30000.00	982.3
293.15	35000.00	985.1
293.15	40000.00	987.7
293.15	45000.00	990.3
293.15	50000.00	992.9
293.15	55000.00	995.3
293.15	60000.00	997.7
303.15	100.00	955.4
303.15	5000.00	958.4
303.15	10000.00	961.8
303.15	15000.00	965.1
303.15	20000.00	968.0
303.15	25000.00	971.1
303.15	30000.00	974.0
303.15	35000.00	976.9
303.15	40000.00	979.6
303.15	45000.00	982.3
303.15	50000.00	984.8
303.15	55000.00	987.5
303.15	60000.00	989.9
313.15	100.00	945.9
313.15	5000.00	949.3
313.15	10000.00	952.7
313.15	15000.00	956.3
313.15	20000.00	959.5
313.15	25000.00	962.5
313.15	30000.00	965.6
313.15	35000.00	968.5
313.15	40000.00	971.5
313.15	45000.00	974.4
313.15	50000.00	977.0
313.15	55000.00	979.5
313.15	60000.00	982.2
323.15	100.00	936.3
323.15	5000.00	940.2
323.15	10000.00	943.9
323.15	15000.00	947.4
323.15	20000.00	950.8
323.15	25000.00	954.0
323.15	30000.00	957.2
323.15	35000.00	960.5
323.15	40000.00	963.3
323.15	45000.00	966.3
323.15	50000.00	969.1
323.15	55000.00	971.9
323.15	60000.00	974.6
333.15	100.00	926.7
333.15	5000.00	930.9
333.15	10000.00	934.6
333.15	15000.00	938.4
333.15	20000.00	941.9
333.15	25000.00	945.3
333.15	30000.00	948.8
333.15	35000.00	952.0
333.15	40000.00	955.0
333.15	45000.00	958.0
333.15	50000.00	961.0
333.15	55000.00	963.9
333.15	60000.00	966.8
343.15	100.00	917.1
343.15	5000.00	921.2
343.15	10000.00	925.3
343.15	15000.00	929.3
343.15	20000.00	932.9
343.15	25000.00	936.9
343.15	30000.00	940.2
343.15	35000.00	943.6
343.15	40000.00	946.8
343.15	45000.00	950.0
343.15	50000.00	953.1
343.15	55000.00	956.2
343.15	60000.00	959.0
353.15	100.00	907.1
353.15	5000.00	911.7
353.15	10000.00	916.1
353.15	15000.00	920.1
353.15	20000.00	924.0
353.15	25000.00	927.9
353.15	30000.00	931.5
353.15	35000.00	934.9
353.15	40000.00	938.7
353.15	45000.00	941.8
353.15	50000.00	945.1
353.15	55000.00	948.2
353.15	60000.00	951.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[97.03; 211.27]	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			3.09520e+01
Coefficient B			2.59620e-01
Coefficient C			-5.88000e-05
Coefficient D			-2.05000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	97.03	J/mol×K	273.00	Calculated Property
Cp,gas	114.53	J/mol×K	353.78	Calculated Property
Cp,gas	130.99	J/mol×K	434.56	Calculated Property
Cp,gas	146.32	J/mol×K	515.33	Calculated Property
Cp,gas	160.48	J/mol×K	596.11	Calculated Property
Cp,gas	173.39	J/mol×K	676.89	Calculated Property
Cp,gas	184.99	J/mol×K	757.67	Calculated Property
Cp,gas	195.21	J/mol×K	838.44	Calculated Property
Cp,gas	203.99	J/mol×K	919.22	Calculated Property
Cp,gas	211.27	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[300.92; 419.45]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.75122e+01
Coefficient B			-4.95806e+03
Coefficient C			-1.30710e+01
Temperature range, min.			300.92
Temperature range, max.			419.45
Pvap	1.33	kPa	300.92	Calculated Property
Pvap	2.83	kPa	314.09	Calculated Property
Pvap	5.65	kPa	327.26	Calculated Property
Pvap	10.66	kPa	340.43	Calculated Property
Pvap	19.15	kPa	353.60	Calculated Property
Pvap	32.93	kPa	366.77	Calculated Property
Pvap	54.47	kPa	379.94	Calculated Property
Pvap	87.01	kPa	393.11	Calculated Property
Pvap	134.69	kPa	406.28	Calculated Property
Pvap	202.67	kPa	419.45	Calculated Property
Pvap	[7.14; 99.45]	kPa	[329.30; 396.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.62651e+01
Coefficient B			-4.26797e+03
Coefficient C			-3.08380e+01
Reference			Pick, Fried, et al., 1956, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			329.30
Temperature range, max.			396.70
Pvap	7.14	kPa	329.30	Calculated Property
Pvap	10.13	kPa	336.79	Calculated Property
Pvap	14.13	kPa	344.28	Calculated Property
Pvap	19.42	kPa	351.77	Calculated Property
Pvap	26.30	kPa	359.26	Calculated Property
Pvap	35.14	kPa	366.74	Calculated Property
Pvap	46.36	kPa	374.23	Calculated Property
Pvap	60.44	kPa	381.72	Calculated Property
Pvap	77.93	kPa	389.21	Calculated Property
Pvap	99.45	kPa	396.70	Calculated Property
Pvap	[7.14; 99.45]	kPa	[329.30; 396.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.62651e+01
Coefficient B			-4.26797e+03
Coefficient C			-3.08380e+01
Reference			Pick, Fried, et al., 1956
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			329.30
Temperature range, max.			396.70
Pvap	7.14	kPa	329.30	Calculated Property
Pvap	10.13	kPa	336.79	Calculated Property
Pvap	14.13	kPa	344.28	Calculated Property
Pvap	19.42	kPa	351.77	Calculated Property
Pvap	26.30	kPa	359.26	Calculated Property
Pvap	35.14	kPa	366.74	Calculated Property
Pvap	46.36	kPa	374.23	Calculated Property
Pvap	60.44	kPa	381.72	Calculated Property
Pvap	77.93	kPa	389.21	Calculated Property
Pvap	99.45	kPa	396.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[188.05; 397.15]	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			6.01780e-02
Coefficient B			-9.84000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			188.05
Temperature range, max.			397.15
γ	0.04	N/m	188.05	Calculated Property
γ	0.04	N/m	211.28	Calculated Property
γ	0.04	N/m	234.52	Calculated Property
γ	0.03	N/m	257.75	Calculated Property
γ	0.03	N/m	280.98	Calculated Property
γ	0.03	N/m	304.22	Calculated Property
γ	0.03	N/m	327.45	Calculated Property
γ	0.03	N/m	350.68	Calculated Property
γ	0.02	N/m	373.92	Calculated Property
γ	0.02	N/m	397.15	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol, 2-methoxy-.

Mixtures

• Ethanol, 2-methoxy- + Water
• Ethanol, 2-methoxy- + Propane, 2-ethoxy-2-methyl-
• Acetonitrile + Ethanol, 2-methoxy-
• Ethanol, 2-methoxy- + Methane, nitro-
• Benzene + Hexadecane + Ethanol, 2-methoxy-
• Toluene + Hexadecane + Ethanol, 2-methoxy-
• p-Xylene + Hexadecane + Ethanol, 2-methoxy-
• Benzene + Ethanol, 2-methoxy-
• Toluene + Ethanol, 2-methoxy-
• p-Xylene + Ethanol, 2-methoxy-
• Benzyl alcohol + Ethanol, 2-methoxy-
• Ethanol, 2-methoxy- + Cyclohexane, methyl-
• Ethanol, 2-methoxy- + Dimethyl Sulfoxide
• Toluene + Ethanol, 2-methoxy- + Dimethyl Sulfoxide
• Nitrous oxide + Ethanol, 2-methoxy-
• Nitrous oxide + Monoethanolamine + Ethanol, 2-methoxy-
• Monoethanolamine + Ethanol, 2-methoxy-
• Carbon dioxide + Ethanol, 2-methoxy-
• 1-Propanol + Ethanol, 2-methoxy-
• 2-Propanol + Ethanol, 2-methoxy-

Find more mixtures with Ethanol, 2-methoxy-.

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).
• 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)
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
• Densities, Viscosities, Sound Speeds, Refractive Indices, and Excess Properties of Binary Mixtures of Isoamyl Alcohol with Some Alkoxyethanols
• Influence of the molecular structure on the viscosity of some alkoxyethanols
• Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether isopropyl alcohol azeotropic mixture
• Densities, speeds of sound and 1H NMR spectroscopic studies for binary mixtures of 1-hexyl-3-methylimidazolium based ionic liquids with ethylene glycol monomethyl ether at temperature from T = (288.15 318.15) K
• Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
• Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
• Isobaric vapor-liquid equilibrium data for methylcyclohexane + 2-methoxyethanol and methylcyclohexane + 2-ethoxyethanol at 50.00 and 101.33 kPa
• tert-Butyl chloride as a probe of the solvophobic effects
• Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
• Surface tension of four oxygenated fuels: experiment and correlation
• Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
• Volumetric properties of binary mixtures of alkoxyethanols with ethyl tert-butyl ether at various temperatures
• Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
• Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
• Relative permittivity of the binary mixtures of 2-methoxyethanol with diethylene glycol, triethylene glycol, tetraethylene glycol, and polyethylene glycol 200 at various temperatures
• Non-ideal behaviour of a room temperature ionic liquid in an alkoxyethanol or poly ethers at T = (298.15 to 318.15) K
• Physical and excess properties of a room temperature ionic liquid (1-methyl-3-octylimidazolium tetrafluoroborate) with n-alkoxyethanols (C1Em, m = 1 to 3) at T = (298.15 to 318.15) K
• Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
• Thermodynamic and physicochemical properties of binary mixtures of nitromethane with {2-methoxyethanol + 2-butoxyethanol} systems at T = (293.15, 298.15, 303.15, 308.15, and 313.15) K
• Investigation of sodium 4-nitrotoluene-2-sulfonate solubility in aqueous organic solutions
• Volumes, heat capacities, and compressibilities of the mixtures of acetonitrile and 2-methoxyethanol
• Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
• Studies on intermolecular interactions in nitrobenzene + alkoxyethanol binary mixtures by relative permittivity measurements at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
• Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
• Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
• Thermophysical properties of ionic liquid {1-butyl-3-methylimidazolium bromide [bmim][Br] in alkoxyalkanols + water} mixtures at different temperatures
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Isobaric (vapor + liquid) equilibria for the binary systems (1-methoxy-2- propanol + 2-methoxyethanol), (2-butanone + 2-methoxyethanol) and (water + 2-methoxyethanol) at pressures of (74.5, 101.3, and 134.0) kPa
• FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
• Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
• Partial molar volumes of organic solutes in water. XXIX. Four 2-alkoxyethanols at temperatures T = (298 K to 573) K and pressures up to 30 MPa
• Monoethanolamine+2-methoxyethanol mixtures for CO2 capture: Density, viscosity and CO2 solubility
• Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
• Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
• Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
• Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
• Study of molecular interactions in binary liquid mixtures of [Emim][BF4] with 2-methoxyethanol using thermo acoustic, volumetric and optical properties
• Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
• Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
• Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Four 2-Alkoxyethanols at Infinite Dilution in Water at Temperatures T = 278 343 K and Atmospheric Pressure
• Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
• Density and Speed of Sound of the Binary Mixture of 1-Butyl-3-Methylimidazolium Bis(trifluoromethylsulfonyl)imide + 2-Methoxyethanol from T = (298.15 to 323.15) K at Atmospheric Pressure
• Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
• Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) 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
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
• Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
• Experimental Surface Tensions and Derived Surface Properties of Binary Mixtures of Water + Alkoxyethanols (C1Em, m = 1, 2, 3) and Water + Ethylene Glycol Dimethyl Ether (C1E1C1) at (298.15, 308.15, and 318.15) K
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
• Density and Relative Permittivity of 2-Methoxyethanol + Dipropylamine Mixtures at Various Temperatures
• High-Pressure Volumetric Properties of Three Monoethylene Glycol Alkyl Ethers
• Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
• Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
• Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Volumetric and Acoustic Properties of Binary Mixtures of the Ionic Liquid 1-Butyl-3-methylimidazolium Tetrafluoroborate [bmim][BF4] with Alkoxyalkanols at Different Temperatures
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Evaluation of the 2-Methoxyethanol as Entrainer in Ethanol Water and 1-Propanol Water Mixtures
• Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
• Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
• 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
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
• Enthalpies of Solution of 1-Butyl-3-methylimidazolium Tetrafluoroborate in 15 Solvents at 298.15 K
• Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
• Ion-Solvent Interactions of Some Halides of Common Cations with Organic Solvent Mixtures by Conductometric, Volumetric, Viscometric, and Refractometric Techniques
• Joback Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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