Chemical Properties of 2-Ethoxyethyl acetate (CAS 111-15-9)

InChI

InChI=1S/C6H12O3/c1-3-8-4-5-9-6(2)7/h3-5H2,1-2H3

InChI Key

SVONRAPFKPVNKG-UHFFFAOYSA-N

Formula

C6H12O3

SMILES

CCOCCOC(C)=O

Molecular Weight¹

132.16

CAS

111-15-9

Other Names

• ''cellosolve'' Acetate
• 1-Acetoxy-2-ethoxyethane
• 2-Aethoxy-aethylacetat
• 2-Ethoxy etheracetate
• 2-Ethoxy-ethylacetaat
• 2-Ethoxyethanol acetate
• 2-Ethoxyethanol, ester with acetic acid
• 2-Ethoxyethyl ester of acetic acid
• 2-Ethoxyethyle, acetate de
• 2-Ethoxyethylester kyseliny octove
• 2-Etossietil-acetato
• 2-ethoxyethyl ethanoate
• 2EEA
• Acetate d'ethylglycol
• Acetate de cellosolve
• Acetate de l'ether monoethylique de l'ethylene-glycol
• Acetato di cellosolve
• Aethylenglykolaetheracetat
• CSAC
• Cellosove acetate
• Celosolvacetat
• EE acetate
• EEA
• Ektasolve EE acetate solvent
• Ethanol, 2-ethoxy-, acetate
• Ethoxy acetate
• Ethoxyethanol acetate
• Ethoxyethyl acetate
• Ethyl acetyl glycolate
• Ethyl cellosolve acetaat
• Ethyl cellosolve acetate
• Ethyl glycol acetate
• Ethylene glycol monethyl ether acetate
• Ethylene glycol monoethyl ether acetate
• Ethylene glycol monoethyl ether monoacetate
• Ethylglykolacetat
• Glycol ether EE acetate
• Glycol monoethyl ether acetate
• NSC 8658
• Octan etoksyetylu
• Oxitol acetate
• Oxytol acetate
• Poly-Solv EE acetate
• Sensolve EEA
• UN 1172
• acetic acid, 2-ethoxyethyl ester
• cellosolve acetate
• ethylene glycol ethyl ether acetate
• «beta»-Ethoxyethyl acetate

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_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).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4830		Relay (1.0) Calculated Property
ΔfG°	-415.73	kJ/mol	Joback Calculated Property
ΔfH°gas	-615.21	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	16.85	kJ/mol	Joback Calculated Property
ΔvapH°	[52.60; 52.70]	kJ/mol
ΔvapH°	52.69 ± 0.02	kJ/mol	NIST
ΔvapH°	52.70 ± 0.10	kJ/mol	NIST
ΔvapH°	52.60 ± 0.40	kJ/mol	NIST
IE	9.63	eV	Relay (1.0) Calculated Property
log10WS	-0.05		Relay (1.0) Calculated Property
logPoct/wat	0.586		Crippen Calculated Property
McVol	108.710	ml/mol	McGowan Calculated Property
Pc	[3166.00; 3180.00]	kPa
Pc	3180.00 ± 150.00	kPa	NIST
Pc	3166.00 ± 40.00	kPa	NIST
ρc	[297.35; 300.00]	kg/m3
ρc	300.00 ± 12.03	kg/m3	NIST
ρc	297.35 ± 6.61	kg/m3	NIST
Inp	[852.00; 909.40]
Inp	882.00		NIST
Inp	875.00		NIST
Inp	888.00		NIST
Inp	880.80		NIST
Inp	Outlier 909.40		NIST
Inp	859.00		NIST
Inp	852.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	874.00		NIST
Inp	872.00		NIST
Inp	859.00		NIST
Inp	876.00		NIST
Inp	880.80		NIST
I	[1290.00; 1319.00]
I	1319.00		NIST
I	1299.00		NIST
I	1299.00		NIST
I	1299.00		NIST
I	1318.00		NIST
I	1290.00		NIST
I	1305.00		NIST
I	1290.00		NIST
Tboil	[428.80; 429.60]	K
Tboil	428.80	K	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Tboil	429.60	K	NIST
Tboil	429.30 ± 0.30	K	NIST
Tboil	429.45	K	NIST
Tc	[607.30; 610.60]	K
Tc	610.60 ± 1.50	K	NIST
Tc	608.70 ± 0.60	K	NIST
Tc	607.30 ± 0.80	K	NIST
Tfus	211.45	K	NIST
Vc	0.415	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	376.00	J/mol×K	298.15	NIST
ΔvapH	50.90	kJ/mol	376.00	NIST
Pvap	[53.33; 101.33]	kPa	[408.20; 429.70]
Pvap	53.33	kPa	408.20	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	69.33	kPa	416.70	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	80.00	kPa	421.50	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	85.33	kPa	423.70	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	90.66	kPa	425.80	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	93.30	kPa	427.80	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Pvap	93.70	kPa	428.30	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Pvap	93.30	kPa	428.60	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Pvap	101.33	kPa	428.80	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	100.93	kPa	428.80	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
Pvap	100.93	kPa	429.70	Vapor Liquid Equilibrium for the 2-Ethoxyethanol 2-Ethoxyethyl Acetate System
n0	1.40311		298.15	Excess molar volumes and excess molar enthalpies of binary mixtures for 1,2-dichloropropane + 2-alkoxyethanol acetates at 298.15K
γ	0.03	N/m	298.15	Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[164.51; 355.48]	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			4.83430e+01
Coefficient B			4.55840e-01
Coefficient C			-9.70000e-05
Coefficient D			-5.17000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	164.51	J/mol×K	273.00	Calculated Property
Cp,gas	195.18	J/mol×K	353.78	Calculated Property
Cp,gas	223.87	J/mol×K	434.56	Calculated Property
Cp,gas	250.42	J/mol×K	515.33	Calculated Property
Cp,gas	274.65	J/mol×K	596.11	Calculated Property
Cp,gas	296.42	J/mol×K	676.89	Calculated Property
Cp,gas	315.55	J/mol×K	757.67	Calculated Property
Cp,gas	331.88	J/mol×K	838.44	Calculated Property
Cp,gas	345.24	J/mol×K	919.22	Calculated Property
Cp,gas	355.48	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0058312; 0.0002139]	Pa×s	[211.45; 426.21]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.17050e+01
Coefficient B			1.38721e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			211.45
Temperature range, max.			426.21
η	0.0058312	Pa×s	211.45	Calculated Property
η	0.0029980	Pa×s	235.31	Calculated Property
η	0.0017423	Pa×s	259.17	Calculated Property
η	0.0011095	Pa×s	283.04	Calculated Property
η	0.0007580	Pa×s	306.90	Calculated Property
η	0.0005470	Pa×s	330.76	Calculated Property
η	0.0004125	Pa×s	354.62	Calculated Property
η	0.0003224	Pa×s	378.48	Calculated Property
η	0.0002594	Pa×s	402.34	Calculated Property
η	0.0002139	Pa×s	426.21	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[327.31; 454.96]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46408e+01
Coefficient B			-3.40251e+03
Coefficient C			-9.02510e+01
Temperature range, min.			327.31
Temperature range, max.			454.96
Pvap	1.33	kPa	327.31	Calculated Property
Pvap	3.00	kPa	341.49	Calculated Property
Pvap	6.18	kPa	355.68	Calculated Property
Pvap	11.85	kPa	369.86	Calculated Property
Pvap	21.32	kPa	384.04	Calculated Property
Pvap	36.34	kPa	398.23	Calculated Property
Pvap	59.10	kPa	412.41	Calculated Property
Pvap	92.26	kPa	426.59	Calculated Property
Pvap	138.92	kPa	440.78	Calculated Property
Pvap	202.63	kPa	454.96	Calculated Property

Similar Compounds

Find more compounds similar to 2-Ethoxyethyl acetate.

Mixtures

• 2-Ethoxyethyl acetate + Propane, 1,2-dichloro-
• 2-Ethoxyethyl acetate + Ethanol, 2-ethoxy-
• 2-Ethoxyethyl acetate + Water
• 2-Ethoxyethyl acetate + Ethanol, 2-butoxy-
• 2-Ethoxyethyl acetate + Ethyleneglycol,monobutylether acetate

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Excess molar volumes and excess molar enthalpies of binary mixtures for 1,2-dichloropropane + 2-alkoxyethanol acetates at 298.15K
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• 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
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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