Chemical Properties of Isobutyl acetate (CAS 110-19-0)

InChI

InChI=1S/C6H12O2/c1-5(2)4-8-6(3)7/h5H,4H2,1-3H3

InChI Key

GJRQTCIYDGXPES-UHFFFAOYSA-N

Formula

C6H12O2

SMILES

CC(=O)OCC(C)C

Molecular Weight¹

116.16

CAS

110-19-0

Other Names

• 2-METHYL-1-PROPYL ACETATE
• 2-METHYLPROPYL ESTER ACETIC ACID
• 2-Methyl-1-propanol, acetate
• 2-Methylpropyl acetate
• 2-Methylpropyl ethanoate
• Acetate d'isobutyle
• Acetic acid, 2-methylpropyl ester
• Acetic acid, isobutyl ester
• ISOBUTYL ETHANOATE
• Isobutyl acetate fcc
• Isobutylester kyseliny octove
• NSC 8035
• UN 1213
• ethanoic acid, isobutyl ester
• i-Butyl acetate
• «beta»-Methylpropyl ethanoate
• «beta»-Methylpropyl ethanoate

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health 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 : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (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	0.4550		KDB
Tig	695.93	K	KDB
ΔcH°liquid	-3534.00	kJ/mol	NIST
μ	1.90	debye	KDB
LFL	2.40	% in Air	KDB
UFL	10.50	% in Air	KDB
Tflash,cc	302.59	K	KDB
Tflash,oc	289.82	K	KDB
ΔfG°	-236.72	kJ/mol	Joback Calculated Property
ΔfH°gas	-495.50	kJ/mol	KDB
ΔfusH°	10.56	kJ/mol	Joback Calculated Property
ΔvapH°	35.90 ± 0.04	kJ/mol	NIST
IE	9.97	eV	NIST
log10WS	[-1.21; -1.21]
log10WS	-1.21		Aq. Solubility Prediction
log10WS	-1.21		Estimated Solubility
logPoct/wat	1.206		Crippen Calculated Property
McVol	102.840	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3010.00; 3180.00]	kPa
Pc	3160.00	kPa	KDB
Pc	3010.00 ± 20.00	kPa	NIST
Pc	3180.00 ± 60.79	kPa	NIST
ρc	281.10 ± 8.13	kg/m3	NIST
Inp	[730.00; 788.00]
Inp	757.70		NIST
Inp	758.98		NIST
Inp	757.00		NIST
Inp	755.00		NIST
Inp	757.20		NIST
Inp	750.00		NIST
Inp	768.00		NIST
Inp	758.00		NIST
Inp	750.00		NIST
Inp	762.00		NIST
Inp	764.00		NIST
Inp	763.00		NIST
Inp	764.00		NIST
Inp	763.00		NIST
Inp	758.00		NIST
Inp	760.00		NIST
Inp	764.00		NIST
Inp	750.00		NIST
Inp	Outlier 783.00		NIST
Inp	Outlier 788.00		NIST
Inp	753.00		NIST
Inp	767.20		NIST
Inp	741.00		NIST
Inp	741.00		NIST
Inp	781.00		NIST
Inp	779.00		NIST
Inp	756.00		NIST
Inp	755.00		NIST
Inp	755.00		NIST
Inp	755.00		NIST
Inp	770.00		NIST
Inp	745.30		NIST
Inp	748.40		NIST
Inp	749.70		NIST
Inp	752.10		NIST
Inp	749.80		NIST
Inp	748.70		NIST
Inp	754.45		NIST
Inp	754.00		NIST
Inp	754.00		NIST
Inp	747.00		NIST
Inp	746.00		NIST
Inp	750.00		NIST
Inp	750.00		NIST
Inp	748.00		NIST
Inp	749.00		NIST
Inp	749.00		NIST
Inp	782.00		NIST
Inp	780.00		NIST
Inp	Outlier 786.00		NIST
Inp	763.00		NIST
Inp	776.00		NIST
Inp	768.00		NIST
Inp	771.00		NIST
Inp	757.00		NIST
Inp	766.00		NIST
Inp	Outlier 734.00		NIST
Inp	749.00		NIST
Inp	770.00		NIST
Inp	770.00		NIST
Inp	767.00		NIST
Inp	779.50		NIST
Inp	757.00		NIST
Inp	764.00		NIST
Inp	760.00		NIST
Inp	760.00		NIST
Inp	770.00		NIST
Inp	758.00		NIST
Inp	744.00		NIST
Inp	745.00		NIST
Inp	743.00		NIST
Inp	744.00		NIST
Inp	754.00		NIST
Inp	758.00		NIST
Inp	764.00		NIST
Inp	764.00		NIST
Inp	758.00		NIST
Inp	Outlier 730.00		NIST
Inp	780.00		NIST
Inp	782.00		NIST
Inp	771.00		NIST
Inp	772.00		NIST
Inp	781.00		NIST
Inp	768.00		NIST
Inp	750.00		NIST
Inp	772.00		NIST
Inp	750.00		NIST
Inp	768.00		NIST
Inp	758.00		NIST
Inp	753.00		NIST
Inp	767.00		NIST
Inp	772.00		NIST
Inp	753.00		NIST
Inp	758.00		NIST
Inp	775.00		NIST
Inp	749.00		NIST
Inp	758.00		NIST
Inp	759.00		NIST
Inp	762.00		NIST
Inp	762.00		NIST
Inp	759.00		NIST
Inp	754.00		NIST
Inp	750.00		NIST
Inp	755.00		NIST
Inp	748.00		NIST
Inp	758.00		NIST
Inp	749.00		NIST
Inp	746.00		NIST
Inp	748.00		NIST
Inp	750.00		NIST
Inp	753.00		NIST
Inp	780.00		NIST
Inp	771.00		NIST
Inp	Outlier 730.00		NIST
Inp	781.00		NIST
Inp	768.00		NIST
Inp	753.00		NIST
Inp	759.00		NIST
Inp	750.00		NIST
Inp	746.00		NIST
I	[976.00; 1047.00]
I	1025.00		NIST
I	1011.00		NIST
I	1025.00		NIST
I	1013.00		NIST
I	1033.00		NIST
I	1018.00		NIST
I	1020.00		NIST
I	1029.00		NIST
I	1005.00		NIST
I	1017.00		NIST
I	1000.00		NIST
I	1031.00		NIST
I	1029.00		NIST
I	1022.00		NIST
I	1002.00		NIST
I	1007.00		NIST
I	1027.00		NIST
I	989.00		NIST
I	986.00		NIST
I	1014.00		NIST
I	993.00		NIST
I	1012.00		NIST
I	1013.00		NIST
I	1019.00		NIST
I	1011.00		NIST
I	1009.00		NIST
I	1009.00		NIST
I	1012.00		NIST
I	1002.00		NIST
I	1018.00		NIST
I	1016.00		NIST
I	1034.00		NIST
I	1010.00		NIST
I	1012.00		NIST
I	1009.00		NIST
I	1009.00		NIST
I	1035.00		NIST
I	985.00		NIST
I	1015.00		NIST
I	1004.00		NIST
I	1032.00		NIST
I	1008.00		NIST
I	1000.00		NIST
I	1009.00		NIST
I	1000.00		NIST
I	998.00		NIST
I	988.00		NIST
I	988.00		NIST
I	992.00		NIST
I	1005.00		NIST
I	1000.00		NIST
I	1005.00		NIST
I	1014.00		NIST
I	1007.00		NIST
I	1005.00		NIST
I	1005.00		NIST
I	1009.00		NIST
I	1009.00		NIST
I	1017.00		NIST
I	1010.00		NIST
I	1011.00		NIST
I	1014.00		NIST
I	1014.00		NIST
I	Outlier 1047.00		NIST
I	1019.00		NIST
I	1020.00		NIST
I	1012.00		NIST
I	1012.00		NIST
I	Outlier 976.00		NIST
I	1024.00		NIST
I	985.00		NIST
I	1017.00		NIST
I	1020.00		NIST
I	1020.00		NIST
I	987.00		NIST
I	1020.00		NIST
I	1020.00		NIST
I	1000.00		NIST
I	1020.00		NIST
I	1023.00		NIST
I	1023.00		NIST
I	1023.00		NIST
I	Outlier 984.00		NIST
I	1025.00		NIST
Tboil	[389.44; 389.90]	K
Tboil	389.70	K	KDB
Tboil	389.44	K	Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
Tboil	389.55	K	Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
Tboil	389.90	K	Isobaric Vapor Liquid Equilibrium for the Binary and Ternary System with Isobutyl Alcohol, Isobutyl Acetate and Dimethyl Sulfoxide at 101.3 kPa
Tboil	389.75	K	Measurement and Correlation of Isobaric Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol with Isobutyl Acetate, Butyl Acetate, and Butyl Propionate at 101.3 kPa
Tboil	389.55	K	Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
Tc	[560.80; 569.00]	K
Tc	561.00	K	KDB
Tc	560.80 ± 0.60	K	NIST
Tc	561.50 ± 2.00	K	NIST
Tc	569.00 ± 5.00	K	NIST
Tfus	[174.25; 240.15]	K
Tfus	174.30	K	KDB
Tfus	174.25	K	Aq. Solubility Prediction
Tfus	176.05	K	NIST
Tfus	176.10 ± 0.60	K	NIST
Tfus	240.15 ± 0.50	K	NIST
Vc	0.414	m3/kmol	KDB
Zc	0.2804710		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[199.90; 255.87]	J/mol×K	[412.53; 594.22]
Cp,gas	199.90	J/mol×K	412.53	Joback Calculated Property
Cp,gas	210.06	J/mol×K	442.81	Joback Calculated Property
Cp,gas	219.89	J/mol×K	473.09	Joback Calculated Property
Cp,gas	229.39	J/mol×K	503.38	Joback Calculated Property
Cp,gas	238.55	J/mol×K	533.66	Joback Calculated Property
Cp,gas	247.38	J/mol×K	563.94	Joback Calculated Property
Cp,gas	255.87	J/mol×K	594.22	Joback Calculated Property
Cp,liquid	240.20	J/mol×K	290.00	NIST
η	[0.0002624; 0.0046134]	Pa×s	[214.54; 412.53]
η	0.0046134	Pa×s	214.54	Joback Calculated Property
η	0.0020807	Pa×s	247.54	Joback Calculated Property
η	0.0011317	Pa×s	280.54	Joback Calculated Property
η	0.0006998	Pa×s	313.53	Joback Calculated Property
η	0.0004742	Pa×s	346.53	Joback Calculated Property
η	0.0003438	Pa×s	379.53	Joback Calculated Property
η	0.0002624	Pa×s	412.53	Joback Calculated Property
ΔvapH	[39.20; 39.90]	kJ/mol	[321.50; 359.00]
ΔvapH	39.80	kJ/mol	321.50	NIST
ΔvapH	39.90	kJ/mol	349.50	NIST
ΔvapH	39.20	kJ/mol	359.00	NIST
Pvap	101.30	kPa	389.55	Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
n0	[1.38760; 1.39050]		[293.15; 298.20]
n0	1.39050		293.15	Isobaric Vapor Liquid Equilibrium for Binary Systems of Thioglycolic Acid with Water, Butyl Acetate, Butyl Formate, and Isobutyl Acetate at 101.3 kPa
n0	1.39020		293.15	Measurement and Correlation of Phase Equilibria for Isobutyl Acetate + {Ethanol or Methanol} + Water at 303.15 and 323.15 K
n0	1.38760		298.15	Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
n0	1.38760		298.15	Phase equilibria in the systems isobutyl alcohol +N,N-dimethylformamide, isobutyl acetate +N,N-dimethylformamide and isobutyl alcohol + isobutyl acetate +N,N-dimethylformamide at 101.3 kPa
n0	1.38760		298.15	Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
n0	1.38760		298.15	Vapor liquid equilibria in the ternary system isobutyl alcohol + isobutyl acetate + butyl propionate and the binary systems isobutyl alcohol + butyl propionate, isobutyl acetate + butyl propionate at 101.3 kPa
n0	1.38760		298.15	Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
n0	1.38760		298.15	Study of liquid liquid equilibrium of the systems isobutyl acetate + acetic acid +water and isobutyl alcohol + acetic acid +water at different temperatures
n0	1.38780		298.20	Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
ρl	[849.39; 875.00]	kg/m3	[293.00; 313.20]
ρl	875.00	kg/m3	293.00	KDB
ρl	871.30	kg/m3	293.20	Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
ρl	849.39	kg/m3	313.20	Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
γ	[0.02; 0.02]	N/m	[298.15; 313.15]
γ	0.02	N/m	298.15	Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
γ	0.02	N/m	308.15	Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
γ	0.02	N/m	313.15	Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[361.00; 403.64]	K	[39.99; 150.00]
Tboil	361.00	K	39.99	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	367.41	K	49.98	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	372.89	K	59.99	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	377.39	K	70.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	381.58	K	80.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	385.54	K	90.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	389.37	K	100.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	392.35	K	110.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	395.26	K	120.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	398.16	K	130.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	400.84	K	140.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
Tboil	403.64	K	150.00	Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[287.55; 414.85]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.50519e+01
Coefficient B			-3.64415e+03
Coefficient C			-4.07290e+01
Temperature range, min.			287.55
Temperature range, max.			414.85
Pvap	1.33	kPa	287.55	Calculated Property
Pvap	2.97	kPa	301.69	Calculated Property
Pvap	6.08	kPa	315.84	Calculated Property
Pvap	11.63	kPa	329.98	Calculated Property
Pvap	20.92	kPa	344.13	Calculated Property
Pvap	35.72	kPa	358.27	Calculated Property
Pvap	58.28	kPa	372.42	Calculated Property
Pvap	91.34	kPa	386.56	Calculated Property
Pvap	138.19	kPa	400.71	Calculated Property
Pvap	202.63	kPa	414.85	Calculated Property
Pvap	[4.57e-06; 3169.48]	kPa	[174.30; 561.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			9.01223e+01
Coefficient B			-7.87047e+03
Coefficient C			-1.11424e+01
Coefficient D			7.93342e-06
Temperature range, min.			174.30
Temperature range, max.			561.00
Pvap	4.57e-06	kPa	174.30	Calculated Property
Pvap	3.39e-03	kPa	217.27	Calculated Property
Pvap	0.21	kPa	260.23	Calculated Property
Pvap	3.39	kPa	303.20	Calculated Property
Pvap	24.24	kPa	346.17	Calculated Property
Pvap	104.11	kPa	389.13	Calculated Property
Pvap	320.39	kPa	432.10	Calculated Property
Pvap	788.29	kPa	475.07	Calculated Property
Pvap	1665.25	kPa	518.03	Calculated Property
Pvap	3169.48	kPa	561.00	Calculated Property

Similar Compounds

Find more compounds similar to Isobutyl acetate.

Mixtures

• Isobutyl acetate + 1-Propanol, 2-methyl-
• Isobutyl acetate + Formamide, N,N-dimethyl-
• Isobutyl acetate + Formamide, N,N-dimethyl- + 1-Propanol, 2-methyl-
• Isobutyl acetate + 1-Hexanol
• Isobutyl acetate + 1-Propanol, 2-methyl- + 1-Hexanol
• Propanoic acid, butyl ester + Isobutyl acetate
• Propanoic acid, butyl ester + Isobutyl acetate + 1-Propanol, 2-methyl-
• Isobutyl acetate + 1-Propanol, 2-methyl- + Water
• Isobutyl acetate + Glycerin + 1-Propanol, 2-methyl-
• Isobutyl acetate + Acetic acid + Water
• Isobutyl acetate + Simvastatin
• Isobutyl acetate + Ethanol
• 1-Propanol + Isobutyl acetate
• Isobutyl acetate + Isopropyl Alcohol
• Isobutyl acetate + Heptane + Simvastatin
• Isobutyl acetate + Water
• Isobutyl acetate + Phenol + Water
• Isobutyl acetate + Carbonic acid, dimethyl ester
• Isobutyl acetate + Ethyl Acetate
• Isobutyl acetate + 1-Butanol, 3-methyl-, acetate

Find more mixtures with Isobutyl acetate.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
• Phase equilibria in the systems isobutyl alcohol +N,N-dimethylformamide, isobutyl acetate +N,N-dimethylformamide and isobutyl alcohol + isobutyl acetate +N,N-dimethylformamide at 101.3 kPa
• Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
• Vapor liquid equilibria in the ternary system isobutyl alcohol + isobutyl acetate + butyl propionate and the binary systems isobutyl alcohol + butyl propionate, isobutyl acetate + butyl propionate at 101.3 kPa
• Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
• Study of liquid liquid equilibrium of the systems isobutyl acetate + acetic acid +water and isobutyl alcohol + acetic acid +water at different temperatures
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Investigation on isobaric vapor-liquid equilibrium for acetic acid + water + (n-propyl acetate or iso-butyl acetate)
• Solubility of lansoprazole in different solvents
• Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
• Phase behavior of binary mixture for the isoalkyl acetate in supercritical carbon dioxide
• Solution thermodynamics of simvastatin in pure solvents and binary solvent mixtures
• Liquid-liquid equilibrium determination and thermodynamics modeling for extraction of isopropanol from its aqueous solution
• Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
• (Liquid + liquid) equilibria in ternary aqueous mixtures of phosphoric acid with organic solvents at T = 298.2 K
• Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
• Measurement and thermodynamic modelling of ternary liquid-liquid equilibrium for extraction of thioglycolic acid from aqueous solution with different solvents
• Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
• Binodal Curves and Tie Line Data of the Water - Propionic Acid - Isobutyl Acetate at T = (298.2, 308.2, 318.2, and 328.2) K
• Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
• Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Thioglycolic Acid with Water, Butyl Acetate, Butyl Formate, and Isobutyl Acetate at 101.3 kPa
• Measurement and Correlation of Phase Equilibria for Isobutyl Acetate + {Ethanol or Methanol} + Water at 303.15 and 323.15 K
• Isobaric Vapor Liquid Equilibrium for the Binary and Ternary System with Isobutyl Alcohol, Isobutyl Acetate and Dimethyl Sulfoxide at 101.3 kPa
• Separation of Protocatechuic Acid Using Di-(2-ethylhexyl)phosphoric Acid in Isobutyl Acetate, Toluene, and Petroleum Ether
• Measurement and Correlation of Isobaric Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol with Isobutyl Acetate, Butyl Acetate, and Butyl Propionate at 101.3 kPa
• Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
• Liquid-Liquid Equilibrium of Isobutyl Acetate + Isobutyl Alcohol + Imidazolium-Based Ionic Liquids at 298.15 and 308.15 K
• Vapor-Liquid Equilibrium for Carbon Dioxide + Isopropyl, Isobutyl, and Isoamyl Acetates
• Solubilities of Benzene Carboxylic Acids in Isobutyl Acetate from (299.73 to 353.15) K
• Ternary Liquid Liquid Equilibria of Water + Prop-2-enoic Acid + Isobutyl Ethanoate at Different Temperatures
• Fast Determination of Binary Vapor Liquid Equilibrium of CO2-Based Mixtures at Elevated Pressures
• Liquid-Liquid Equilibria for the Ternary Systems Acetic Acid + Water + Butyl Acetate and Acetic Acid + Water + 2-Methyl Propyl Acetate at 304.15 K, 332.15 K, and 366.15 K
• Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
• Solubility of Lovastatin in Ethyl Acetate, Propyl Acetate, Isopropyl Acetate, Butyl Acetate, sec-Butyl Acetate, Isobutyl Acetate, tert-Butyl Acetate, and 2-Butanone, between (285 and 313) K
• Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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