Chemical Properties of Ethyleneglycol,monobutylether acetate

InChI

InChI=1S/C8H16O3/c1-3-4-5-10-6-7-11-8(2)9/h3-7H2,1-2H3

InChI Key

NQBXSWAWVZHKBZ-UHFFFAOYSA-N

Formula

C8H16O3

SMILES

CCCCOCCOC(C)=O

Molecular Weight¹

160.21

Other Names

• 1-Acetoxy-2-butoxyethane
• 2-Butoxyethanol acetate
• 2-Butoxyethylester kyseliny octove
• 2-butoxyethyl acetate
• 2-butoxyethyl ethanoate
• Acetic acid, 2-butoxyethyl ester
• Butoxyethanol acetate
• Butoxyethyl acetate
• Butylcelosolvacetat
• Butylglycol acetate
• Ektasolve eb acetate
• Ethanol, 2-butoxy-, 1-acetate
• Ethylene glycol mono-n-butyl ether acetate
• butyl cellosolve acetate
• butyl glycol acetate
• ethanol, 2-butoxy-, acetate
• ethylene glycol butyl ether acetate
• ethylene glycol monobutyl ether acetate
• glycol monobutyl ether acetate
• n-Butyl cellosolve acetate

• ω : Acentric Factor.
• C_p,gas : Ideal gas 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).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-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).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.6015		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ΔfG°	-398.89	kJ/mol	Joback Calculated Property
ΔfH°gas	-653.18	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	22.03	kJ/mol	Joback Calculated Property
ΔvapH°	[59.50; 59.54]	kJ/mol
ΔvapH°	59.54 ± 0.04	kJ/mol	NIST
ΔvapH°	59.50 ± 0.10	kJ/mol	NIST
IE	9.64	eV	Relay (1.0) Calculated Property
log10WS	-0.96		Relay (1.0) Calculated Property
logPoct/wat	1.708		NCMS SOLV-DB
McVol	136.890	ml/mol	McGowan Calculated Property
Pc	[2694.00; 2695.24]	kPa
Pc	2694.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	2695.24	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2694.00 ± 40.00	kPa	NIST
ρc	291.58 ± 6.41	kg/m3	NIST
Inp	[1053.00; 1120.20]
Inp	1096.00		NIST
Inp	1120.20		NIST
Inp	1090.00		NIST
Inp	1090.00		NIST
Inp	1053.00		NIST
Inp	1061.00		NIST
Inp	1089.80		NIST
Inp	1087.00		NIST
Inp	1053.00		NIST
Tboil	[465.15; 466.20]	K
Tboil	465.15	K	NCMS SOLV-DB
Tboil	465.20	K	NIST
Tboil	466.20 ± 1.50	K	NIST
Tc	[640.20; 641.20]	K
Tc	640.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	640.20	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	641.20 ± 1.60	K	NIST
Tc	640.20 ± 0.80	K	NIST
Tfus	[209.15; 210.15]	K
Tfus	210.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	209.15	K	NCMS SOLV-DB
Tfus	209.70 ± 0.60	K	NIST
Vc	[0.549; 0.549]	m3/kmol
Vc	0.549	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.549	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Zc	0.2780000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	0.0017000	Pa×s	298.15	NCMS SOLV-DB
ΔvapH	51.90	kJ/mol	379.00	NIST
Pvap	[2.92; 98.36]	kPa	[363.15; 464.20]
Pvap	2.92	kPa	363.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	4.57	kPa	373.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	6.72	kPa	383.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	9.96	kPa	393.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	14.42	kPa	403.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	20.44	kPa	413.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	28.85	kPa	423.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	33.94	kPa	428.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	39.87	kPa	433.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	46.80	kPa	438.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	54.64	kPa	443.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	63.48	kPa	448.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	85.24	kPa	458.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	93.70	kPa	463.00	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Pvap	98.36	kPa	463.15	Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
Pvap	93.60	kPa	463.30	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Pvap	93.90	kPa	464.20	Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
n0	[1.41183; 1.41300]		[298.15; 298.15]
n0	1.41183		298.15	Excess molar volumes and excess molar enthalpies of binary mixtures for 1,2-dichloropropane + 2-alkoxyethanol acetates at 298.15K
n0	1.41300		298.15	NCMS SOLV-DB
ρl	[901.29; 960.40]	kg/m3	[273.15; 333.15]
ρl	960.40	kg/m3	273.15	Below the room temperature measurements of CO2 solubilities in six physical absorbents
ρl	950.40	kg/m3	283.15	Below the room temperature measurements of CO2 solubilities in six physical absorbents
ρl	940.70	kg/m3	293.15	Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
ρl	930.89	kg/m3	303.15	Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
ρl	921.05	kg/m3	313.15	Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
ρl	911.18	kg/m3	323.15	Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
ρl	901.29	kg/m3	333.15	Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
γ	0.03	N/m	298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[206.93; 458.66]	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			4.65250e+01
Coefficient B			6.45840e-01
Coefficient C			-2.05800e-04
Coefficient D			-2.79000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	206.93	J/mol×K	273.00	Calculated Property
Cp,gas	248.02	J/mol×K	353.78	Calculated Property
Cp,gas	286.03	J/mol×K	434.56	Calculated Property
Cp,gas	320.88	J/mol×K	515.33	Calculated Property
Cp,gas	352.48	J/mol×K	596.11	Calculated Property
Cp,gas	380.74	J/mol×K	676.89	Calculated Property
Cp,gas	405.58	J/mol×K	757.67	Calculated Property
Cp,gas	426.91	J/mol×K	838.44	Calculated Property
Cp,gas	444.63	J/mol×K	919.22	Calculated Property
Cp,gas	458.66	J/mol×K	1000.00	Calculated Property

Similar Compounds

Find more compounds similar to Ethyleneglycol,monobutylether acetate.

Mixtures

• Carbon dioxide + Ethyleneglycol,monobutylether acetate
• Propane, 1,2-dichloro- + Ethyleneglycol,monobutylether acetate
• Ethyleneglycol,monobutylether acetate + Sulfuryl fluoride
• Ethyleneglycol,monobutylether acetate + Ethanol, 2-ethoxy-
• 2-Ethoxyethyl acetate + Ethyleneglycol,monobutylether acetate
• Ethanol, 2-butoxy- + Ethyleneglycol,monobutylether acetate

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.
• 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
• Solubilities of CO2 capture absorbents 2-ethoxyethyl ether, 2-butoxyethyl acetate and 2-(2-ethoxyethoxy)ethyl acetate
• Below the room temperature measurements of CO2 solubilities in six physical absorbents
• Excess molar volumes and excess molar enthalpies of binary mixtures for 1,2-dichloropropane + 2-alkoxyethanol acetates at 298.15K
• Solubilities of Sulfuryl Fluoride in 2-Butoxyethyl Acetate, 3-Methoxybutyl Acetate, 2-Methoxyethyl Acetate, 1-Methoxy-2-propyl Acetate, and 2-(2-Ethoxyethoxy)ethyl Acetate
• Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
• Critical Assessment of CO2 Solubility in Volatile Solvents at 298.15 K
• Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
• Joback Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB

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