Chemical Properties of Ethanol, 2-ethoxy- (CAS 110-80-5)

InChI

InChI=1S/C4H10O2/c1-2-6-4-3-5/h5H,2-4H2,1H3

InChI Key

ZNQVEEAIQZEUHB-UHFFFAOYSA-N

Formula

C4H10O2

SMILES

CCOCCO

Molecular Weight¹

90.12

CAS

110-80-5

Other Names

• 1,2-ethanediol, monoethyl ether
• 2-Ethoxyethyl alcohol
• 2-ethoxyethan-1-ol
• 2-ethoxyethanol
• 2-ethoxyethanol (cellosolve)
• 2EE
• 3-oxa-1-pentanol
• Bikanol E 1
• Cellosolve
• Cellosolve solvent
• Dowanol EE
• EE solvent
• EGEE
• Ektasolve EE
• Emkanol
• Ether monoethylique de l'ethylene-glycol
• Ethoxyethanol
• Ethyl icinol
• Ethyl-2-hydroxyethyl ether
• Ethylene glycol ethyl ether
• Ethylethylene glycol
• Etoksyetylowy alkohol
• Glycol ether EE
• Glycol ethyl ether
• Glycol monoethyl ether
• HOCH2CH2OC2H5
• Hydroxy ether
• Jeffersol EE
• NCI-C54853
• NSC 8837
• Oxitol
• Plastiazan 60
• Poly-Solv EE
• Solvid
• ethyl cellosolve
• ethyl glycol
• ethylene glycol monoethyl ether
• ethylene glycol, monoethyl ether
• «beta»-Ethoxyethanol

• ω : Acentric Factor.
• 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_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).
• P_c : Critical Pressure (kPa).
• pKa : Log10 of Acid Dissociation Constant.
• 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.
• 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).
• 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_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	[0.6745; 0.7582]
ω	0.6745		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.7582		ChemSep v8.3 pure component data Compiled value
μ	2.08	debye	ChemSep v8.3 pure component data Compiled value
η	0.0018450	Pa×s	Conductance Studies of NaCl, KCl, NaBr, NaI, NaBPh4, and Bu4NI in Water + 2-Ethoxyethanol Mixtures at 298.15 K
εr	29.60		NCMS SOLV-DB
Tflash,cc	317.15	K	NCMS SOLV-DB
ΔfG°	-256.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-400.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	11.39	kJ/mol	Joback Calculated Property
ΔvapH°	[48.20; 50.00]	kJ/mol
ΔvapH°	48.20	kJ/mol	NCMS SOLV-DB
ΔvapH°	48.23	kJ/mol	NIST
ΔvapH°	49.40	kJ/mol	NIST
ΔvapH°	50.00	kJ/mol	NIST
ΔvapH°	48.20 ± 0.10	kJ/mol	NIST
ΔvapH°	49.20	kJ/mol	NIST
IE	[9.60; 9.97]	eV
IE	9.60	eV	NIST
IE	9.97	eV	NIST
log10WS	0.78		Relay (1.0) Calculated Property
logPoct/wat	-0.100		NCMS SOLV-DB
McVol	78.960	ml/mol	McGowan Calculated Property
Pc	[4199.92; 4240.00]	kPa
Pc	4199.92	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4240.00	kPa	ChemSep v8.3 pure component data Compiled value
pKa	14.80		NCMS SOLV-DB
Ptriple	8.58e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[666.00; 743.50]
Inp	695.00		NIST
Inp	687.00		NIST
Inp	671.00		NIST
Inp	694.00		NIST
Inp	666.00		NIST
Inp	670.00		NIST
Inp	718.00		NIST
Inp	708.00		NIST
Inp	716.00		NIST
Inp	Outlier 743.50		NIST
Inp	702.00		NIST
Inp	695.00		NIST
Inp	702.00		NIST
Inp	695.00		NIST
Inp	716.50		NIST
Inp	694.00		NIST
Inp	694.00		NIST
Inp	701.00		NIST
Inp	701.00		NIST
Ip	[1218.00; 1266.00]
Ip	1231.00		NIST
Ip	1266.00		NIST
Ip	1246.00		NIST
Ip	1239.00		NIST
Ip	1239.00		NIST
Ip	1218.00		NIST
Tboil	[407.80; 408.75]	K
Tboil	408.62	K	Isobaric vapor-liquid equilibrium data for methylcyclohexane + 2-methoxyethanol and methylcyclohexane + 2-ethoxyethanol at 50.00 and 101.33 kPa
Tboil	408.19	K	Vapour-liquid equilibrium and extractive distillation for separation of azeotrope isopropyl alcohol and diisopropyl ether
Tboil	407.80	K	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Tboil	408.35	K	Isobaric Vapor Liquid Equilibrium of Binary and Ternary Systems with 2-Ethoxyethanol + Ethylbenzene + Dimethyl Sulfoxide
Tboil	408.75	K	ChemSep v8.3 pure component data Compiled value
Tboil	408.65	K	NCMS SOLV-DB
Tboil	408.20	K	NIST
Tboil	408.10	K	NIST
Tboil	408.25 ± 0.30	K	NIST
Tboil	408.75	K	NIST
Tboil	408.15 ± 0.50	K	NIST
Tboil	408.50 ± 0.60	K	NIST
Tboil	408.45 ± 0.30	K	NIST
Tboil	408.00 ± 1.50	K	NIST
Tc	[569.00; 598.90]	K
Tc	598.90	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	569.65	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	569.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[173.15; 203.15]	K
Tfus	183.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	203.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	173.15	K	NCMS SOLV-DB
Ttriple	214.15	K	ChemSep v8.3 pure component data Compiled value
UQi	3.29		ChemSep v8.3 pure component data Compiled value
URi	3.70		ChemSep v8.3 pure component data Compiled value
Vc	[0.294; 0.295]	m3/kmol
Vc	0.295	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.294	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vm	9.74e-05	m3/mol	Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
Zc	0.2640000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[203.30; 226.50]	J/mol×K	[275.15; 339.15]
Cp,liquid	203.30	J/mol×K	275.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	204.00	J/mol×K	277.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	204.60	J/mol×K	279.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	205.30	J/mol×K	281.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	205.90	J/mol×K	283.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	206.60	J/mol×K	285.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	207.30	J/mol×K	287.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	208.00	J/mol×K	289.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	208.60	J/mol×K	291.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	209.30	J/mol×K	293.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	210.00	J/mol×K	295.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	210.70	J/mol×K	297.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	211.10	J/mol×K	298.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	209.82	J/mol×K	298.15	NIST
Cp,liquid	210.80	J/mol×K	298.15	NIST
Cp,liquid	210.50	J/mol×K	298.15	NIST
Cp,liquid	211.40	J/mol×K	299.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	212.10	J/mol×K	301.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	212.80	J/mol×K	303.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	213.60	J/mol×K	305.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	214.30	J/mol×K	307.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	215.00	J/mol×K	309.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	215.70	J/mol×K	311.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	216.50	J/mol×K	313.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	217.20	J/mol×K	315.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	218.00	J/mol×K	317.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	218.70	J/mol×K	319.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	219.50	J/mol×K	321.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	220.20	J/mol×K	323.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	221.00	J/mol×K	325.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	221.80	J/mol×K	327.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	222.60	J/mol×K	329.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	223.30	J/mol×K	331.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	224.10	J/mol×K	333.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	224.90	J/mol×K	335.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	225.70	J/mol×K	337.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	226.50	J/mol×K	339.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
η	[0.0014070; 0.0021420]	Pa×s	[293.15; 308.15]
η	0.0021420	Pa×s	293.15	Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
η	0.0018480	Pa×s	298.15	Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
η	0.0018500	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	0.0018500	Pa×s	298.15	NCMS SOLV-DB
η	0.0016460	Pa×s	303.15	Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
η	0.0014070	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
ΔvapH	[39.22; 47.40]	kJ/mol	[338.00; 408.10]
ΔvapH	45.90	kJ/mol	338.00	NIST
ΔvapH	47.40	kJ/mol	347.50	NIST
ΔvapH	44.70	kJ/mol	372.00	NIST
ΔvapH	39.22	kJ/mol	408.10	NIST
Pvap	[0.71; 101.33]	kPa	[298.15; 407.80]
Pvap	0.71	kPa	298.15	NCMS SOLV-DB
Pvap	1.30	kPa	308.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
Pvap	1.86	kPa	313.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
Pvap	1.83	kPa	313.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
Pvap	1.80	kPa	313.15	Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
Pvap	5.30	kPa	333.15	Vapor-Liquid Equilibrium for Phenol + r-Methyl Benzyl Alcohol and 2-Ethoxyethanol + n-Butyl Formate
Pvap	8.65	kPa	343.15	Vapor-Liquid Equilibrium for Phenol + r-Methyl Benzyl Alcohol and 2-Ethoxyethanol + n-Butyl Formate
Pvap	13.62	kPa	353.15	Vapor-Liquid Equilibrium for Phenol + r-Methyl Benzyl Alcohol and 2-Ethoxyethanol + n-Butyl Formate
Pvap	28.10	kPa	373.48	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	34.20	kPa	378.36	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	41.30	kPa	383.18	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	47.90	kPa	387.06	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	53.33	kPa	388.60	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	53.70	kPa	390.12	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	60.50	kPa	393.37	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	69.33	kPa	396.10	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	68.60	kPa	396.86	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	76.40	kPa	399.90	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	80.00	kPa	400.40	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	81.20	kPa	401.65	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	85.33	kPa	402.30	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	90.66	kPa	404.20	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	88.70	kPa	404.22	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	93.30	kPa	406.20	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Pvap	95.30	kPa	406.33	Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Pvap	93.30	kPa	406.90	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Pvap	100.93	kPa	407.50	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	101.33	kPa	407.80	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	100.93	kPa	407.80	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	93.60	kPa	407.80	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
n0	[1.40570; 1.40650]		[293.15; 303.15]
n0	1.40650		293.15	Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0	1.40650		293.15	Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-1,4-dihydroxy Phenylene in the Selected Solvents
n0	1.40650		293.15	Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
n0	1.40620		298.15	Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using 2-ethoxyethanol as entrainer
n0	1.40580		298.15	Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
n0	1.40570		298.15	Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
n0	1.40600		298.15	NCMS SOLV-DB
n0	1.40650		303.15	Densities, Viscosities, Sound Speeds, Refractive Indices, and Excess Properties of Binary Mixtures of Isoamyl Alcohol with Some Alkoxyethanols
ρl	[856.30; 941.20]	kg/m3	[283.15; 373.15]
ρl	941.20	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	936.70	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	936.80	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	932.30	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	929.70	kg/m3	293.15	Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
ρl	929.70	kg/m3	293.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	932.20	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	929.50	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	925.10	kg/m3	298.10	Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
ρl	925.36	kg/m3	298.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	925.54	kg/m3	298.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	925.00	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	927.70	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	927.60	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	926.00	kg/m3	298.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	924.92	kg/m3	298.15	Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
ρl	925.20	kg/m3	298.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	925.64	kg/m3	298.15	Thermodynamic properties and sPC-SAFT modeling of 2-ethoxyethanol, 2-propoxyethanol and 2-butoxyethanol from T = (293.15-413.15) K and pressure up to 30 MPa
ρl	920.50	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	920.70	kg/m3	303.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	923.10	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	923.10	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	920.99	kg/m3	303.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	921.19	kg/m3	303.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	920.72	kg/m3	303.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	921.00	kg/m3	303.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	918.50	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	918.50	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	924.97	kg/m3	308.15	Electrical Conductances of Sodium Polystyrenesulfonate in 2-Ethoxyethanol (1) + Water (2) Mixed Solvent Media in the Presence of Sodium Chloride at (308.15, 313.15, 318.15, and 323.15) K
ρl	917.00	kg/m3	308.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	916.43	kg/m3	308.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	915.90	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	916.11	kg/m3	308.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	916.41	kg/m3	308.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	916.10	kg/m3	308.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	916.00	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	911.47	kg/m3	313.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	911.58	kg/m3	313.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	913.80	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	913.90	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	911.80	kg/m3	313.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	911.50	kg/m3	313.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	912.00	kg/m3	313.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	911.30	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	906.60	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	907.15	kg/m3	318.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	906.80	kg/m3	318.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	906.90	kg/m3	318.15	FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
ρl	907.00	kg/m3	318.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	907.76	kg/m3	318.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	909.30	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	902.46	kg/m3	323.15	Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
ρl	904.60	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	903.45	kg/m3	323.15	Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
ρl	901.90	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	902.10	kg/m3	323.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	904.50	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	897.40	kg/m3	328.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	897.20	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	899.90	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	892.60	kg/m3	333.15	Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
ρl	895.00	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	895.10	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	892.40	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	890.40	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	887.60	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	885.50	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	885.20	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	882.70	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	877.80	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	880.70	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	875.80	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	872.80	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	871.00	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	866.10	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	861.20	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	856.30	kg/m3	373.15	Thermophysical properties of glycols and glymes
csound,fluid	[1224.90; 1319.91]	m/s	[293.15; 323.15]
csound,fluid	1319.91	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	1301.73	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	1290.40	m/s	303.15	Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
csound,fluid	1287.10	m/s	303.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1284.15	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	1268.00	m/s	308.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1257.30	m/s	313.15	Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
csound,fluid	1252.00	m/s	313.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1235.10	m/s	318.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1224.90	m/s	323.15	Acoustic, volumetric, and spectroscopic studies of formamide with 2-alkoxyethanols at different temperatures
γ	0.03	N/m	298.15	NCMS SOLV-DB

Datasets

1. Viscosity, Pa*s (1)
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	0.0024
293.15	40000.00	0.0028
293.15	60000.00	0.0031
293.15	80000.00	0.0035
293.15	100000.00	0.0039
303.15	20000.00	0.0019
303.15	40000.00	0.0022
303.15	60000.00	0.0025
303.15	80000.00	0.0028
303.15	100000.00	0.0031
313.15	20000.00	0.0016
313.15	40000.00	0.0018
313.15	60000.00	0.0021
313.15	80000.00	0.0023
313.15	100000.00	0.0025
323.15	20000.00	0.0013
323.15	40000.00	0.0015
323.15	60000.00	0.0017
323.15	80000.00	0.0019
323.15	100000.00	0.0021
333.15	20000.00	0.0011
333.15	40000.00	0.0012
333.15	60000.00	0.0014
333.15	80000.00	0.0016
333.15	100000.00	0.0018
343.15	20000.00	0.0009
343.15	40000.00	0.0011
343.15	60000.00	0.0012
343.15	80000.00	0.0014
343.15	100000.00	0.0015
353.15	20000.00	0.0008
353.15	40000.00	0.0010
353.15	60000.00	0.0011
353.15	80000.00	0.0012
353.15	100000.00	0.0013
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	929.6
293.15	5000.00	932.9
293.15	10000.00	936.2
293.15	15000.00	939.3
293.15	20000.00	942.4
293.15	25000.00	945.2
293.15	30000.00	948.2
293.15	35000.00	951.1
293.15	40000.00	953.7
293.15	45000.00	956.5
293.15	50000.00	959.0
293.15	55000.00	961.6
293.15	60000.00	964.0
303.15	100.00	920.7
303.15	5000.00	924.0
303.15	10000.00	927.4
303.15	15000.00	930.7
303.15	20000.00	933.9
303.15	25000.00	937.0
303.15	30000.00	939.9
303.15	35000.00	942.9
303.15	40000.00	945.8
303.15	45000.00	948.6
303.15	50000.00	951.3
303.15	55000.00	953.8
303.15	60000.00	956.3
313.15	100.00	911.3
313.15	5000.00	914.9
313.15	10000.00	918.5
313.15	15000.00	922.1
313.15	20000.00	925.5
313.15	25000.00	928.7
313.15	30000.00	931.8
313.15	35000.00	934.9
313.15	40000.00	937.8
313.15	45000.00	940.7
313.15	50000.00	943.4
313.15	55000.00	946.1
313.15	60000.00	948.9
323.15	100.00	901.8
323.15	5000.00	905.8
323.15	10000.00	909.7
323.15	15000.00	913.4
323.15	20000.00	916.9
323.15	25000.00	920.3
323.15	30000.00	923.6
323.15	35000.00	926.9
323.15	40000.00	930.0
323.15	45000.00	933.0
323.15	50000.00	935.7
323.15	55000.00	938.7
323.15	60000.00	941.4
333.15	100.00	892.3
333.15	5000.00	896.5
333.15	10000.00	900.5
333.15	15000.00	904.5
333.15	20000.00	908.2
333.15	25000.00	911.8
333.15	30000.00	915.4
333.15	35000.00	918.7
333.15	40000.00	921.8
333.15	45000.00	925.0
333.15	50000.00	927.9
333.15	55000.00	931.1
333.15	60000.00	933.9
343.15	100.00	882.6
343.15	5000.00	887.2
343.15	10000.00	891.4
343.15	15000.00	895.6
343.15	20000.00	899.4
343.15	25000.00	903.4
343.15	30000.00	906.9
343.15	35000.00	910.5
343.15	40000.00	913.8
343.15	45000.00	917.2
343.15	50000.00	920.4
343.15	55000.00	923.4
343.15	60000.00	926.5
353.15	100.00	872.6
353.15	5000.00	877.6
353.15	10000.00	882.0
353.15	15000.00	886.5
353.15	20000.00	890.6
353.15	25000.00	894.8
353.15	30000.00	898.5
353.15	35000.00	902.0
353.15	40000.00	905.9
353.15	45000.00	908.8
353.15	50000.00	912.5
353.15	55000.00	915.7
353.15	60000.00	918.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[120.99; 296.65]	J/mol×K	[300.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.24500e+01
Coefficient B			2.99800e+02
Coefficient C			1.17310e+03
Coefficient D			2.07750e+02
Coefficient E			4.72800e+02
Temperature range, min.			300.00
Temperature range, max.			1500.00
Cp,gas	120.99	J/mol×K	300.00	Calculated Property
Cp,gas	162.04	J/mol×K	433.33	Calculated Property
Cp,gas	194.12	J/mol×K	566.67	Calculated Property
Cp,gas	221.08	J/mol×K	700.00	Calculated Property
Cp,gas	242.70	J/mol×K	833.33	Calculated Property
Cp,gas	259.52	J/mol×K	966.67	Calculated Property
Cp,gas	272.51	J/mol×K	1100.00	Calculated Property
Cp,gas	282.56	J/mol×K	1233.33	Calculated Property
Cp,gas	290.43	J/mol×K	1366.67	Calculated Property
Cp,gas	296.65	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[205.04; 233.43]	J/mol×K	[283.15; 350.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.35170e+02
Coefficient B			-5.36050e-01
Coefficient C			1.51740e-03
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			283.15
Temperature range, max.			350.00
Cp,liquid	205.04	J/mol×K	283.15	Calculated Property
Cp,liquid	207.53	J/mol×K	290.58	Calculated Property
Cp,liquid	210.18	J/mol×K	298.01	Calculated Property
Cp,liquid	213.00	J/mol×K	305.43	Calculated Property
Cp,liquid	215.99	J/mol×K	312.86	Calculated Property
Cp,liquid	219.14	J/mol×K	320.29	Calculated Property
Cp,liquid	222.46	J/mol×K	327.72	Calculated Property
Cp,liquid	225.95	J/mol×K	335.14	Calculated Property
Cp,liquid	229.61	J/mol×K	342.57	Calculated Property
Cp,liquid	233.43	J/mol×K	350.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0418126; 0.0001150]	Pa×s	[214.15; 453.00]	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			-7.56350e+00
Coefficient B			2.09020e+03
Coefficient C			-1.00090e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			214.15
Temperature range, max.			453.00
η	0.0418126	Pa×s	214.15	Calculated Property
η	0.0126804	Pa×s	240.69	Calculated Property
η	0.0048207	Pa×s	267.23	Calculated Property
η	0.0021631	Pa×s	293.77	Calculated Property
η	0.0011001	Pa×s	320.31	Calculated Property
η	0.0006166	Pa×s	346.84	Calculated Property
η	0.0003732	Pa×s	373.38	Calculated Property
η	0.0002403	Pa×s	399.92	Calculated Property
η	0.0001628	Pa×s	426.46	Calculated Property
η	0.0001150	Pa×s	453.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[53.42; 0.00]	kJ/mol	[214.15; 569.00]	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			6.39040e+01
Coefficient B			3.79370e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			5.69000e+02
Temperature range, min.			214.15
Temperature range, max.			569.00
ΔvapH	53.42	kJ/mol	214.15	Calculated Property
ΔvapH	51.09	kJ/mol	253.58	Calculated Property
ΔvapH	48.57	kJ/mol	293.01	Calculated Property
ΔvapH	45.81	kJ/mol	332.43	Calculated Property
ΔvapH	42.75	kJ/mol	371.86	Calculated Property
ΔvapH	39.28	kJ/mol	411.29	Calculated Property
ΔvapH	35.21	kJ/mol	450.72	Calculated Property
ΔvapH	30.19	kJ/mol	490.14	Calculated Property
ΔvapH	23.21	kJ/mol	529.57	Calculated Property
ΔvapH	0.00	kJ/mol	569.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[309.84; 430.65]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.73172e+01
Coefficient B			-4.91675e+03
Coefficient C			-2.11200e+01
Temperature range, min.			309.84
Temperature range, max.			430.65
Pvap	1.33	kPa	309.84	Calculated Property
Pvap	2.84	kPa	323.26	Calculated Property
Pvap	5.68	kPa	336.69	Calculated Property
Pvap	10.72	kPa	350.11	Calculated Property
Pvap	19.26	kPa	363.53	Calculated Property
Pvap	33.11	kPa	376.96	Calculated Property
Pvap	54.71	kPa	390.38	Calculated Property
Pvap	87.28	kPa	403.80	Calculated Property
Pvap	134.90	kPa	417.23	Calculated Property
Pvap	202.63	kPa	430.65	Calculated Property
Pvap	[8.58e-05; 4267.09]	kPa	[214.15; 569.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			2.13812e+02
Coefficient B			-1.35170e+04
Coefficient C			-3.00620e+01
Coefficient D			2.78350e-05
Coefficient E			2.00000e+00
Temperature range, min.			214.15
Temperature range, max.			569.00
Pvap	8.58e-05	kPa	214.15	Calculated Property
Pvap	0.02	kPa	253.58	Calculated Property
Pvap	0.50	kPa	293.01	Calculated Property
Pvap	5.34	kPa	332.43	Calculated Property
Pvap	29.64	kPa	371.86	Calculated Property
Pvap	110.36	kPa	411.29	Calculated Property
Pvap	321.42	kPa	450.72	Calculated Property
Pvap	809.74	kPa	490.14	Calculated Property
Pvap	1887.77	kPa	529.57	Calculated Property
Pvap	4267.09	kPa	569.00	Calculated Property
Pvap	[6.19; 97.66]	kPa	[336.00; 407.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.58159e+01
Coefficient B			-4.04531e+03
Coefficient C			-4.69200e+01
Reference			Pick, Fried, et al., 1956, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			336.00
Temperature range, max.			407.00
Pvap	6.19	kPa	336.00	Calculated Property
Pvap	8.97	kPa	343.89	Calculated Property
Pvap	12.76	kPa	351.78	Calculated Property
Pvap	17.83	kPa	359.67	Calculated Property
Pvap	24.52	kPa	367.56	Calculated Property
Pvap	33.19	kPa	375.44	Calculated Property
Pvap	44.31	kPa	383.33	Calculated Property
Pvap	58.36	kPa	391.22	Calculated Property
Pvap	75.93	kPa	399.11	Calculated Property
Pvap	97.66	kPa	407.00	Calculated Property
Pvap	[6.19; 97.66]	kPa	[336.00; 407.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.58159e+01
Coefficient B			-4.04531e+03
Coefficient C			-4.69200e+01
Reference			Pick, Fried, et al., 1956
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			336.00
Temperature range, max.			407.00
Pvap	6.19	kPa	336.00	Calculated Property
Pvap	8.97	kPa	343.89	Calculated Property
Pvap	12.76	kPa	351.78	Calculated Property
Pvap	17.83	kPa	359.67	Calculated Property
Pvap	24.52	kPa	367.56	Calculated Property
Pvap	33.19	kPa	375.44	Calculated Property
Pvap	44.31	kPa	383.33	Calculated Property
Pvap	58.36	kPa	391.22	Calculated Property
Pvap	75.93	kPa	399.11	Calculated Property
Pvap	97.66	kPa	407.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[992.80; 306.54]	kg/m3	[214.15; 569.00]	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			8.29320e+01
Coefficient B			2.70540e-01
Coefficient C			5.69000e+02
Coefficient D			2.25710e-01
Temperature range, min.			214.15
Temperature range, max.			569.00
ρl	992.80	kg/m3	214.15	Calculated Property
ρl	962.66	kg/m3	253.58	Calculated Property
ρl	930.50	kg/m3	293.01	Calculated Property
ρl	895.83	kg/m3	332.43	Calculated Property
ρl	857.93	kg/m3	371.86	Calculated Property
ρl	815.64	kg/m3	411.29	Calculated Property
ρl	766.97	kg/m3	450.72	Calculated Property
ρl	707.86	kg/m3	490.14	Calculated Property
ρl	627.06	kg/m3	529.57	Calculated Property
ρl	306.54	kg/m3	569.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[203.15; 408.15]	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			5.50916e-02
Coefficient B			-8.97000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			203.15
Temperature range, max.			408.15
γ	0.04	N/m	203.15	Calculated Property
γ	0.03	N/m	225.93	Calculated Property
γ	0.03	N/m	248.71	Calculated Property
γ	0.03	N/m	271.48	Calculated Property
γ	0.03	N/m	294.26	Calculated Property
γ	0.03	N/m	317.04	Calculated Property
γ	0.02	N/m	339.82	Calculated Property
γ	0.02	N/m	362.59	Calculated Property
γ	0.02	N/m	385.37	Calculated Property
γ	0.02	N/m	408.15	Calculated Property
γ	[0.03; 0.02]	N/m	[293.00; 408.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.47430e-02
Coefficient B			-8.88650e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			293.00
Temperature range, max.			408.15
γ	0.03	N/m	293.00	Calculated Property
γ	0.03	N/m	305.79	Calculated Property
γ	0.03	N/m	318.59	Calculated Property
γ	0.03	N/m	331.38	Calculated Property
γ	0.02	N/m	344.18	Calculated Property
γ	0.02	N/m	356.97	Calculated Property
γ	0.02	N/m	369.77	Calculated Property
γ	0.02	N/m	382.56	Calculated Property
γ	0.02	N/m	395.36	Calculated Property
γ	0.02	N/m	408.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.08]	W/m×K	[408.15; 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			8.90400e-01
Coefficient B			-1.55700e-01
Coefficient C			4.70330e+02
Coefficient D			2.37700e+06
Temperature range, min.			408.15
Temperature range, max.			1000.00
λgas	0.02	W/m×K	408.15	Calculated Property
λgas	0.03	W/m×K	473.91	Calculated Property
λgas	0.03	W/m×K	539.67	Calculated Property
λgas	0.04	W/m×K	605.43	Calculated Property
λgas	0.05	W/m×K	671.19	Calculated Property
λgas	0.05	W/m×K	736.96	Calculated Property
λgas	0.06	W/m×K	802.72	Calculated Property
λgas	0.07	W/m×K	868.48	Calculated Property
λgas	0.07	W/m×K	934.24	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.20; 0.14]	W/m×K	[214.15; 408.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.76700e-01
Coefficient B			-3.38870e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			214.15
Temperature range, max.			408.15
λliquid	0.20	W/m×K	214.15	Calculated Property
λliquid	0.20	W/m×K	235.71	Calculated Property
λliquid	0.19	W/m×K	257.26	Calculated Property
λliquid	0.18	W/m×K	278.82	Calculated Property
λliquid	0.17	W/m×K	300.37	Calculated Property
λliquid	0.17	W/m×K	321.93	Calculated Property
λliquid	0.16	W/m×K	343.48	Calculated Property
λliquid	0.15	W/m×K	365.04	Calculated Property
λliquid	0.15	W/m×K	386.59	Calculated Property
λliquid	0.14	W/m×K	408.15	Calculated Property

Similar Compounds

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

Mixtures

• Di-n-propyl ether + Ethanol, 2-ethoxy-
• 1-Propanol + Ethanol, 2-ethoxy-
• 1-Propanol + Di-n-propyl ether + Ethanol, 2-ethoxy-
• Ethanol, 2-ethoxy- + Water
• Ethanol, 2-ethoxy- + Cyclohexane
• Octane + Ethanol, 2-ethoxy-
• n-Hexane + Ethanol, 2-ethoxy-
• Benzene + Ethanol, 2-ethoxy-
• Benzyl alcohol + Ethanol, 2-ethoxy-
• 2-Propanol + Ethanol, 2-ethoxy-
• Diisopropyl ether + Ethanol, 2-ethoxy-
• Ethanol, 2-ethoxy- + Cyclohexane, methyl-
• Benzenamine, 4,4'-oxybis- + Ethanol, 2-ethoxy-
• Monoethanolamine + Ethanol, 2-ethoxy-
• Nitrous oxide + Ethanol, 2-ethoxy-
• Nitrous oxide + Monoethanolamine + Ethanol, 2-ethoxy-
• Carbon dioxide + Ethanol, 2-ethoxy-
• Monoethanolamine + Carbon dioxide + Ethanol, 2-ethoxy-
• Ethanol, 2-ethoxy- + Methyl Alcohol
• Carbonic acid, dimethyl ester + Ethanol, 2-ethoxy-

Find more mixtures with Ethanol, 2-ethoxy-.

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).
• 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
• 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
• Phase Compositions and Saturated Densities for the Binary System of Carbon Dioxide with 2-ethoxyethanol
• Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
• Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using 2-ethoxyethanol as entrainer
• Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
• Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
• Measurement and correlation of the solubility of 4,4'-oxydianiline in different organic solvents
• Isobaric vapor-liquid equilibrium data for methylcyclohexane + 2-methoxyethanol and methylcyclohexane + 2-ethoxyethanol at 50.00 and 101.33 kPa
• Solubility of disodium 4,4'-dinitrobibenzyl-2,2'-disulfonate in aqueous organic solutions and its effects on the oxidation reaction of DSD acid synthesis
• Thermodynamic properties and sPC-SAFT modeling of 2-ethoxyethanol, 2-propoxyethanol and 2-butoxyethanol from T = (293.15-413.15) K and pressure up to 30 MPa
• Viscosity of aqueous solutions of 2-methoxyethanol, 2-ethoxyethanol, and ethanolamine
• Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
• Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
• Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
• 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
• Solubility of disodium 4,4'-dinitrostilbene-2,2'-disulfonate and sodium 4-nitrotoluene-2-sulfonate in aqueous organic solutions and its application feasibility in oxidation stage of DSD acid synthesis
• 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
• Vapour-liquid equilibrium and extractive distillation for separation of azeotrope isopropyl alcohol and diisopropyl ether
• Solubility of N2O and CO2 in non-aqueous systems of monoethanolamine and glycol ethers: Measurements and model representation
• An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
• Adducts of antimony tri-iodide and aromatic amines: A calorimetric study
• Intermolecular interactions in Formamide +2-Alkoxyethanols: Viscometric study
• Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
• Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
• Thermophysical properties of glycols and glymes
• 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
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• 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
• Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
• Vapor-Liquid Equilibrium for Phenol + r-Methyl Benzyl Alcohol and 2-Ethoxyethanol + n-Butyl Formate
• 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
• Total Vapor Pressure Measurements for 2-Ethoxyethanol with Carbon Tetrachloride, Chloroform, and Dichloromethane at 303.15 K
• High-Pressure Volumetric Properties of Three Monoethylene Glycol Alkyl Ethers
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
• Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
• Isobaric Vapor Liquid Equilibrium of Binary and Ternary Systems with 2-Ethoxyethanol + Ethylbenzene + Dimethyl Sulfoxide
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
• Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-1,4-dihydroxy Phenylene in the Selected Solvents
• Solubilities of Diphenylphosphinic Acid in Selected Solvents
• 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
• Conductance Studies of NaCl, KCl, NaBr, NaI, NaBPh4, and Bu4NI in Water + 2-Ethoxyethanol Mixtures at 298.15 K
• Electrical Conductances of Sodium Polystyrenesulfonate in 2-Ethoxyethanol (1) + Water (2) Mixed Solvent Media in the Presence of Sodium Chloride at (308.15, 313.15, 318.15, and 323.15) K
• Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
• Joback Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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