Chemical Properties of Acetic acid, methyl ester (CAS 79-20-9)

InChI

InChI=1S/C3H6O2/c1-3(4)5-2/h1-2H3

InChI Key

KXKVLQRXCPHEJC-UHFFFAOYSA-N

Formula

C3H6O2

SMILES

COC(C)=O

Molecular Weight¹

74.08

CAS

79-20-9

Other Names

• Acetate de methyle
• CH3COOCH3
• Devoton
• Ethyl ester of monoacetic acid
• Methyl acetic ester
• Methyl ester of acetic acid
• Methylacetaat
• Methylacetat
• Methyle (acetate de)
• Methylester kiseliny octove
• Metile (acetato di)
• NSC 405071
• Tereton
• UN 1231
• ethanoic acid, methyl ester
• methyl acetate
• methyl ethanoate

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• 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).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point 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.
• 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 thermal conductivity (W/m×K).
• λ : 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).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3230; 0.3260]
ω	0.3230		ChemSep v8.3 pure component data
ω	0.3260		KDB
PAff	821.60	kJ/mol	NIST
Tig	[727.15; 774.82]	K
Tig	774.82	K	KDB
Tig	727.15	K	NCMS SOLV-DB
BasG	790.70	kJ/mol	NIST
ΔcH°liquid	[-1592.20; -1583.00]	kJ/mol
ΔcH°liquid	-1583.00	kJ/mol	NIST
ΔcH°liquid	-1592.20 ± 0.67	kJ/mol	NIST
μ	[1.68; 1.70]	debye
μ	1.68	debye	ChemSep v8.3 pure component data
μ	1.70	debye	KDB
η	[0.0003711; 0.0004000]	Pa×s
η	0.0003711	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η	0.0004000	Pa×s	Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
η	0.0003800	Pa×s	Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
εr	6.68		NCMS SOLV-DB
LFL	3.10	% in Air	KDB
UFL	16.00	% in Air	KDB
Tflash,cc	[263.15; 267.59]	K
Tflash,cc	267.59	K	KDB
Tflash,cc	263.15	K	NCMS SOLV-DB
Tflash,oc	263.15	K	KDB
ΔfG°	-324.20	kJ/mol	ChemSep v8.3 pure component data
Rg	2.8620		KDB
ΔfH°gas	[-411.90; -409.70]	kJ/mol
ΔfH°gas	-411.90	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-409.70	kJ/mol	KDB
ΔfH°gas	-410.00	kJ/mol	NIST
ΔfH°liquid	-445.89	kJ/mol	NIST
ΔfusH°	7.90	kJ/mol	Joback Calculated Property
ΔvapH°	[30.40; 35.90]	kJ/mol
ΔvapH°	32.30	kJ/mol	NCMS SOLV-DB
ΔvapH°	32.50	kJ/mol	NIST
ΔvapH°	32.30 ± 0.10	kJ/mol	NIST
ΔvapH°	32.60 ± 0.06	kJ/mol	NIST
ΔvapH°	32.60 ± 0.10	kJ/mol	NIST
ΔvapH°	35.90	kJ/mol	NIST
ΔvapH°	35.90	kJ/mol	NIST
ΔvapH°	30.40 ± 0.04	kJ/mol	NIST
IE	[10.20; 11.00]	eV
IE	10.25 ± 0.02	eV	NIST
IE	10.20	eV	NIST
IE	10.25	eV	NIST
IE	10.25 ± 0.05	eV	NIST
IE	10.33	eV	NIST
IE	10.27 ± 0.02	eV	NIST
IE	10.50	eV	NIST
IE	10.25	eV	NIST
IE	Outlier 11.00	eV	NIST
IE	10.59	eV	NIST
log10WS	[0.46; 0.52]
log10WS	0.52		Aq. Solubility Prediction
log10WS	0.46		Estimated Solubility
logPoct/wat	0.180		NCMS SOLV-DB
McVol	60.570	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=3); %!d(float64=3)]
NFPA Fire	3		KDB
NFPA Fire	3		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[4690.00; 5840.00]	kPa
Pc	4690.00	kPa	ChemSep v8.3 pure component data
Pc	4750.00	kPa	KDB
Pc	4750.00 ± 4.74	kPa	NIST
Pc	4694.00 ± 81.06	kPa	NIST
Pc	4694.30 ± 40.00	kPa	NIST
Pc	4817.00 ± 101.32	kPa	NIST
Pc	Outlier 5840.00 ± 607.95	kPa	NIST
Ptriple	1.02e-03	kPa	ChemSep v8.3 pure component data
ρc	[320.02; 325.50]	kg/m3
ρc	325.50 ± 3.70	kg/m3	NIST
ρc	320.02 ± 5.93	kg/m3	NIST
Inp	[501.15; 560.00]
Inp	501.15		NIST
Inp	522.17		NIST
Inp	520.60		NIST
Inp	521.00		NIST
Inp	526.20		NIST
Inp	521.30		NIST
Inp	515.70		NIST
Inp	513.80		NIST
Inp	511.50		NIST
Inp	529.70		NIST
Inp	525.70		NIST
Inp	523.70		NIST
Inp	530.00		NIST
Inp	525.70		NIST
Inp	522.40		NIST
Inp	505.00		NIST
Inp	505.00		NIST
Inp	505.00		NIST
Inp	509.00		NIST
Inp	505.00		NIST
Inp	529.00		NIST
Inp	Outlier 560.00		NIST
Inp	525.90		NIST
Inp	509.00		NIST
Inp	509.00		NIST
Inp	505.00		NIST
Inp	506.00		NIST
Inp	510.00		NIST
Inp	531.00		NIST
Inp	509.00		NIST
Inp	522.00		NIST
Inp	531.00		NIST
Inp	517.20		NIST
Inp	526.30		NIST
Inp	506.00		NIST
Inp	511.00		NIST
Inp	511.00		NIST
Inp	521.30		NIST
Inp	516.70		NIST
Inp	536.00		NIST
Inp	515.00		NIST
Inp	Outlier 559.00		NIST
Inp	512.00		NIST
Inp	513.00		NIST
Inp	513.00		NIST
Inp	510.00		NIST
Inp	511.00		NIST
Inp	507.00		NIST
Inp	512.00		NIST
Inp	515.00		NIST
Inp	524.00		NIST
Inp	515.30		NIST
Inp	525.00		NIST
Inp	511.00		NIST
Inp	515.00		NIST
Inp	513.00		NIST
Inp	519.00		NIST
Inp	509.00		NIST
Inp	531.00		NIST
Inp	528.00		NIST
Inp	509.00		NIST
Inp	509.00		NIST
Inp	525.00		NIST
Inp	509.00		NIST
Inp	Outlier 559.00		NIST
Inp	523.00		NIST
Inp	513.00		NIST
Inp	509.00		NIST
Inp	530.00		NIST
Inp	512.00		NIST
Inp	510.00		NIST
Inp	507.00		NIST
Inp	512.00		NIST
Inp	513.00		NIST
Inp	524.00		NIST
Inp	508.00		NIST
Inp	508.00		NIST
Inp	519.00		NIST
Inp	513.00		NIST
Inp	509.00		NIST
Inp	531.00		NIST
Inp	515.30		NIST
Inp	519.00		NIST
Inp	530.00		NIST
Inp	513.00		NIST
I	[782.00; 877.00]
I	844.00		NIST
I	Outlier 877.00		NIST
I	823.00		NIST
I	839.00		NIST
I	850.00		NIST
I	836.00		NIST
I	832.00		NIST
I	810.00		NIST
I	827.00		NIST
I	828.00		NIST
I	798.00		NIST
I	839.00		NIST
I	826.00		NIST
I	Outlier 864.00		NIST
I	832.80		NIST
I	801.00		NIST
I	834.00		NIST
I	825.00		NIST
I	829.00		NIST
I	827.00		NIST
I	817.00		NIST
I	825.00		NIST
I	828.00		NIST
I	825.00		NIST
I	848.00		NIST
I	818.00		NIST
I	843.00		NIST
I	828.00		NIST
I	813.00		NIST
I	832.00		NIST
I	828.00		NIST
I	826.00		NIST
I	Outlier 782.00		NIST
I	856.00		NIST
I	822.00		NIST
I	Outlier 782.00		NIST
I	Outlier 782.00		NIST
I	825.00		NIST
I	827.00		NIST
I	837.00		NIST
I	845.00		NIST
I	825.00		NIST
I	825.00		NIST
I	828.00		NIST
I	Outlier 784.00		NIST
I	834.00		NIST
I	854.00		NIST
I	826.00		NIST
I	827.00		NIST
I	813.00		NIST
I	834.00		NIST
I	804.00		NIST
I	834.00		NIST
I	834.00		NIST
I	813.00		NIST
I	834.00		NIST
I	841.00		NIST
I	841.00		NIST
I	827.00		NIST
I	796.00		NIST
I	832.00		NIST
I	825.00		NIST
I	848.00		NIST
I	844.00		NIST
I	836.00		NIST
Tboil	[324.35; 332.15]	K
Tboil	330.04	K	Volumetric property for carbon dioxide + methyl acetate system at 313.15K
Tboil	330.05	K	Multiphase equilibria for mixtures containing water, acetic acid, propionic acid, methyl acetate and methyl propionate
Tboil	330.95	K	Isobaric vapor-liquid equilibrium data for the binary system methyl acetate + isopropyl acetate and the quaternary system methyl acetate + methanol + isopropanol + isopropyl acetate at 101.3 kPa
Tboil	330.40	K	Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
Tboil	330.02	K	Experimental isobaric vapor-liquid equilibrium for the binary and ternary systems with methanol, methyl acetate and dimethyl sulfoxide at 101.3 kPa
Tboil	330.05	K	Isobaric vapor-liquid equilibrium for methanol + methyl acetate with ionic liquids [OMMIM][Tf2N] and [OMIM][Tf2N] as entrainers at 101.3 kPa
Tboil	330.20	K	Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
Tboil	329.85	K	Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
Tboil	329.97	K	Vapor-Liquid Equilibrium and Liquid-Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Acetate
Tboil	329.95	K	Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
Tboil	330.09	K	ChemSep v8.3 pure component data
Tboil	330.02	K	KDB
Tboil	330.15	K	NCMS SOLV-DB
Tboil	330.05 ± 0.30	K	NIST
Tboil	330.02 ± 0.20	K	NIST
Tboil	329.82 ± 0.20	K	NIST
Tboil	330.20	K	NIST
Tboil	330.09 ± 0.20	K	NIST
Tboil	330.09 ± 0.30	K	NIST
Tboil	330.10	K	NIST
Tboil	330.30 ± 0.20	K	NIST
Tboil	330.00 ± 0.50	K	NIST
Tboil	330.04 ± 0.08	K	NIST
Tboil	330.00 ± 0.30	K	NIST
Tboil	330.35 ± 0.15	K	NIST
Tboil	330.01 ± 0.50	K	NIST
Tboil	329.95 ± 0.30	K	NIST
Tboil	329.95 ± 0.30	K	NIST
Tboil	328.65 ± 2.00	K	NIST
Tboil	330.15 ± 2.00	K	NIST
Tboil	Outlier 326.65 ± 2.00	K	NIST
Tboil	330.15 ± 0.10	K	NIST
Tboil	329.93 ± 0.15	K	NIST
Tboil	329.55 ± 1.00	K	NIST
Tboil	330.45 ± 2.00	K	NIST
Tboil	330.05 ± 1.00	K	NIST
Tboil	329.90 ± 2.00	K	NIST
Tboil	330.05 ± 1.00	K	NIST
Tboil	330.10 ± 0.30	K	NIST
Tboil	Outlier 324.35 ± 2.00	K	NIST
Tboil	Outlier 332.15 ± 2.00	K	NIST
Tboil	329.25 ± 2.00	K	NIST
Tboil	Outlier 327.65 ± 2.00	K	NIST
Tboil	329.47 ± 0.08	K	NIST
Tboil	330.30 ± 0.15	K	NIST
Tboil	330.70 ± 1.00	K	NIST
Tboil	330.15 ± 2.00	K	NIST
Tboil	330.25 ± 1.00	K	NIST
Tboil	329.40 ± 0.50	K	NIST
Tboil	330.40 ± 0.30	K	NIST
Tboil	330.00 ± 1.50	K	NIST
Tboil	330.25 ± 0.50	K	NIST
Tboil	329.05 ± 1.00	K	NIST
Tboil	328.65 ± 2.00	K	NIST
Tboil	Outlier 327.60 ± 1.00	K	NIST
Tboil	330.10 ± 0.30	K	NIST
Tboil	330.45 ± 0.50	K	NIST
Tboil	330.30 ± 0.50	K	NIST
Tboil	330.20 ± 1.00	K	NIST
Tboil	329.85 ± 2.00	K	NIST
Tboil	330.45 ± 0.50	K	NIST
Tboil	330.30 ± 0.50	K	NIST
Tboil	328.90 ± 1.00	K	NIST
Tboil	330.50 ± 1.50	K	NIST
Tboil	330.65 ± 2.00	K	NIST
Tboil	329.65 ± 2.00	K	NIST
Tboil	329.45 ± 2.00	K	NIST
Tboil	329.45 ± 2.00	K	NIST
Tc	[503.00; 552.00]	K
Tc	506.80	K	ChemSep v8.3 pure component data
Tc	506.55	K	KDB
Tc	506.80	K	NIST
Tc	506.65 ± 0.40	K	NIST
Tc	506.55 ± 0.05	K	NIST
Tc	506.90 ± 1.00	K	NIST
Tc	506.90 ± 1.00	K	NIST
Tc	509.00 ± 3.00	K	NIST
Tc	Outlier 552.00 ± 20.00	K	NIST
Tc	506.10 ± 2.00	K	NIST
Tc	513.00 ± 5.00	K	NIST
Tc	503.00 ± 3.00	K	NIST
Tfus	[175.00; 175.15]	K
Tfus	175.15	K	ChemSep v8.3 pure component data
Tfus	175.00	K	KDB
Tfus	175.05	K	NCMS SOLV-DB
Tfus	175.15 ± 0.30	K	NIST
Tfus	175.10 ± 0.20	K	NIST
Ttriple	[174.90; 175.15]	K
Ttriple	175.15	K	ChemSep v8.3 pure component data
Ttriple	174.90 ± 0.01	K	NIST
Ttriple	174.90 ± 0.01	K	NIST
UQi	2.58		ChemSep v8.3 pure component data
URi	2.80		ChemSep v8.3 pure component data
Vc	[0.228; 0.228]	m3/kmol
Vc	0.228	m3/kmol	ChemSep v8.3 pure component data
Vc	0.228	m3/kmol	KDB
Zc	[0.2540000; 0.2571400]
Zc	0.2540000		ChemSep v8.3 pure component data
Zc	0.2571400		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[92.58; 114.63]	J/mol×K	[335.00; 450.00]
Cp,gas	92.58	J/mol×K	335.00	NIST
Cp,gas	95.46	J/mol×K	350.00	NIST
Cp,gas	100.39	J/mol×K	375.00	NIST
Cp,gas	105.31	J/mol×K	400.00	NIST
Cp,gas	109.98	J/mol×K	425.00	NIST
Cp,gas	114.63	J/mol×K	450.00	NIST
Cp,liquid	[123.70; 141.34]	J/mol×K	[288.58; 298.15]
Cp,liquid	140.20	J/mol×K	288.58	NIST
Cp,liquid	123.70	J/mol×K	297.00	NIST
Cp,liquid	141.34	J/mol×K	298.15	NIST
Cp,liquid	140.60	J/mol×K	298.15	NIST
Cp,liquid	140.56	J/mol×K	298.15	NIST
η	[0.0003480; 0.0003860]	Pa×s	[293.15; 308.15]
η	0.0003860	Pa×s	293.15	Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
η	0.0003860	Pa×s	293.15	Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η	0.0003670	Pa×s	298.15	Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
η	0.0003840	Pa×s	298.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
η	0.0003670	Pa×s	298.15	Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η	0.0003640	Pa×s	298.15	NCMS SOLV-DB
η	0.0003480	Pa×s	303.15	Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
η	0.0003480	Pa×s	303.15	Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η	0.0003510	Pa×s	308.15	Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
ΔfusH	[7.49; 7.49]	kJ/mol	[174.90; 174.90]
ΔfusH	7.49	kJ/mol	174.90	NIST
ΔfusH	7.49	kJ/mol	174.90	NIST
ΔfusH	7.49	kJ/mol	174.90	NIST
ΔfusH	7.49	kJ/mol	174.90	NIST
ΔfusH	7.49	kJ/mol	174.90	NIST
ΔfusH	7.49	kJ/mol	174.90	NIST
ΔvapH	[29.50; 34.50]	kJ/mol	[295.00; 343.00]
ΔvapH	32.50	kJ/mol	295.00	NIST
ΔvapH	34.50	kJ/mol	295.50	NIST
ΔvapH	33.40	kJ/mol	301.50	NIST
ΔvapH	32.20 ± 0.10	kJ/mol	304.00	NIST
ΔvapH	34.10	kJ/mol	305.50	NIST
ΔvapH	31.60 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	31.80	kJ/mol	323.00	NIST
ΔvapH	30.50 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	30.20	kJ/mol	330.00	NIST
ΔvapH	30.32	kJ/mol	330.10	NIST
ΔvapH	30.30 ± 0.10	kJ/mol	331.00	NIST
ΔvapH	29.50 ± 0.10	kJ/mol	343.00	NIST
Pvap	[28.80; 1500.00]	kPa	[298.15; 436.08]
Pvap	28.80	kPa	298.15	NCMS SOLV-DB
Pvap	37.14	kPa	304.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	40.40	kPa	306.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	43.89	kPa	308.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	47.62	kPa	310.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	51.60	kPa	312.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	53.81	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	55.85	kPa	314.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	60.38	kPa	316.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	65.21	kPa	318.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	70.34	kPa	320.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	75.79	kPa	322.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	79.21	kPa	323.15	Isothermal vapour liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate system, and in five binary subsystems
Pvap	81.58	kPa	324.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	87.72	kPa	326.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	94.23	kPa	328.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	101.33	kPa	329.95	Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
Pvap	101.30	kPa	329.97	Vapor-Liquid Equilibrium and Liquid-Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Acetate
Pvap	101.12	kPa	330.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	101.30	kPa	330.05	Multiphase equilibria for mixtures containing water, acetic acid, propionic acid, methyl acetate and methyl propionate
Pvap	108.41	kPa	332.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	116.11	kPa	334.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	124.25	kPa	336.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	132.83	kPa	338.00	Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
Pvap	600.00	kPa	393.01	Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa
Pvap	1500.00	kPa	436.08	Measurement and modeling of high pressure VLE for methyl acetate or ethyl acetate with 2-butanol. Isobaric data at 1.5 MPa
n0	[1.34823; 1.36500]		[288.15; 318.15]
n0	1.36500		288.15	Density, refraction index and vapor-liquid equilibria of N-methyl-2-hydroxyethylammonium butyrate plus (methyl acetate or ethyl acetate or propyl acetate) at several temperatures
n0	1.36414		288.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0	1.35872		298.15	Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
n0	1.35865		298.15	Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + Ethyl Lactate and Methyl Acetate + Ethyl Lactate
n0	1.35850		298.15	Molecular interactions in (2,4,6-trimethyl-1,3,5-trioxane + n-alkyl acetates) at T=(298.15, 303.15, and 308.15) K
n0	1.35850		298.15	Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
n0	1.35893		298.15	Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
n0	1.35900		298.15	NCMS SOLV-DB
n0	1.35881		298.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0	1.35880		298.15	A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
n0	1.35906		298.15	Excess molar volumes and excess molar enthalpies for binary mixtures of 1,2-dichloropropane with methyl ethanoate, methyl propanoate, and methyl butanoate at T = 298.15K
n0	1.36146		298.15	Isobaric Vapor-Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa
n0	1.35870		298.15	Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
n0	1.35875		298.15	Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
n0	1.35890		298.15	Vapor-liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method
n0	1.35881		298.15	Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0	1.35893		298.15	Isobaric Vapor-Liquid Equilibria for the Binary Systems Benzene + Methyl Ethanoate, Benzene + Butyl Ethanoate, and Benzene + Methyl Heptanoate at 101.31kPa
n0	1.35670		303.15	Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
n0	1.35367		308.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0	1.34860		318.15	Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol
n0	1.34823		318.15	Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0	1.34900		318.15	Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
ρl	[907.90; 935.01]	kg/m3	[293.00; 313.15]
ρl	934.00	kg/m3	293.00	KDB
ρl	935.01	kg/m3	293.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	928.46	kg/m3	298.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	927.10	kg/m3	298.15	Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer
ρl	926.90	kg/m3	298.15	Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
ρl	927.30	kg/m3	298.15	Isobaric vapor-liquid equilibrium for methyl acetate + methanol system containing different ionic liquids at 101.3 kPa
ρl	927.30	kg/m3	298.15	Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
ρl	927.70	kg/m3	298.15	Liquid Liquid Equilibrium for Ternary System Methanol + Methyl Acetate + 1,3-Dimethylimidazolium Dimethylphosphate at Several Temperatures and Atmospheric Pressure
ρl	927.10	kg/m3	298.15	Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
ρl	927.50	kg/m3	298.15	Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
ρl	921.85	kg/m3	303.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	920.50	kg/m3	303.15	Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
ρl	915.16	kg/m3	308.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	908.49	kg/m3	313.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	907.90	kg/m3	313.15	Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
csound,fluid	[1110.02; 1200.38]	m/s	[288.15; 308.15]
csound,fluid	1200.38	m/s	288.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1178.95	m/s	293.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1155.93	m/s	298.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1132.98	m/s	303.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1110.02	m/s	308.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
γ	[0.02; 0.02]	N/m	[298.15; 298.15]
γ	0.02	N/m	298.15	Surface Tension Data of Aqueous Binary Mixtures of Methyl, Ethyl, Propyl, and Butyl Acetates at 298.15 K
γ	0.02	N/m	298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[72.71; 207.17]	J/mol×K	[220.00; 1500.00]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			6.22350e+01
Coefficient B			-6.85050e+02
Coefficient C			5.44024e+00
Coefficient D			1.23630e-04
Coefficient E			-8.56410e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			220.00
Temperature range, max.			1500.00
Cp,gas	72.71	J/mol×K	220.00	Calculated Property
Cp,gas	98.20	J/mol×K	362.22	Calculated Property
Cp,gas	123.97	J/mol×K	504.44	Calculated Property
Cp,gas	145.75	J/mol×K	646.67	Calculated Property
Cp,gas	163.33	J/mol×K	788.89	Calculated Property
Cp,gas	177.29	J/mol×K	931.11	Calculated Property
Cp,gas	188.20	J/mol×K	1073.33	Calculated Property
Cp,gas	196.58	J/mol×K	1215.56	Calculated Property
Cp,gas	202.80	J/mol×K	1357.78	Calculated Property
Cp,gas	207.17	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[127.36; 161.16]	J/mol×K	[207.38; 373.40]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			6.31440e+00
Coefficient B			6.80300e+02
Coefficient C			-2.73106e+00
Coefficient D			2.61480e-02
Coefficient E			-2.73410e-05
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			207.38
Temperature range, max.			373.40
Cp,liquid	127.36	J/mol×K	207.38	Calculated Property
Cp,liquid	126.86	J/mol×K	225.83	Calculated Property
Cp,liquid	129.02	J/mol×K	244.27	Calculated Property
Cp,liquid	132.89	J/mol×K	262.72	Calculated Property
Cp,liquid	137.82	J/mol×K	281.17	Calculated Property
Cp,liquid	143.25	J/mol×K	299.61	Calculated Property
Cp,liquid	148.71	J/mol×K	318.06	Calculated Property
Cp,liquid	153.78	J/mol×K	336.51	Calculated Property
Cp,liquid	158.05	J/mol×K	354.95	Calculated Property
Cp,liquid	161.16	J/mol×K	373.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0006151; 0.0000845]	Pa×s	[250.00; 473.00]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			1.11200e+01
Coefficient B			-1.00130e+02
Coefficient C			-3.27450e+00
Coefficient D			-5.30510e-07
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			250.00
Temperature range, max.			473.00
η	0.0006151	Pa×s	250.00	Calculated Property
η	0.0004648	Pa×s	274.78	Calculated Property
η	0.0003583	Pa×s	299.56	Calculated Property
η	0.0002811	Pa×s	324.33	Calculated Property
η	0.0002238	Pa×s	349.11	Calculated Property
η	0.0001805	Pa×s	373.89	Calculated Property
η	0.0001472	Pa×s	398.67	Calculated Property
η	0.0001213	Pa×s	423.44	Calculated Property
η	0.0001009	Pa×s	448.22	Calculated Property
η	0.0000845	Pa×s	473.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[38.99; 0.00]	kJ/mol	[175.15; 506.80]	ChemSep v8.3 pure component data
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			4.99290e+01
Coefficient B			7.91970e-01
Coefficient C			-7.31360e-01
Coefficient D			3.74290e-01
Coefficient E			-1.99740e-02
Critical temperature, Tc (K)			5.06800e+02
Comment			ChemSep eq 106, HeatOfVaporization, ChemSep Tmax 506.85 K
Temperature range, min.			175.15
Temperature range, max.			506.80
ΔvapH	38.99	kJ/mol	175.15	Calculated Property
ΔvapH	37.06	kJ/mol	212.00	Calculated Property
ΔvapH	35.13	kJ/mol	248.85	Calculated Property
ΔvapH	33.11	kJ/mol	285.70	Calculated Property
ΔvapH	30.94	kJ/mol	322.55	Calculated Property
ΔvapH	28.49	kJ/mol	359.40	Calculated Property
ΔvapH	25.57	kJ/mol	396.25	Calculated Property
ΔvapH	21.88	kJ/mol	433.10	Calculated Property
ΔvapH	16.62	kJ/mol	469.95	Calculated Property
ΔvapH	0.00	kJ/mol	506.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4701.97]	kPa	[243.21; 506.55]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47592e+01
Coefficient B			-2.94089e+03
Coefficient C			-3.99950e+01
Temperature range, min.			243.21
Temperature range, max.			506.55
Pvap	1.33	kPa	243.21	Calculated Property
Pvap	8.24	kPa	272.47	Calculated Property
Pvap	33.89	kPa	301.73	Calculated Property
Pvap	104.88	kPa	330.99	Calculated Property
Pvap	264.06	kPa	360.25	Calculated Property
Pvap	569.61	kPa	389.51	Calculated Property
Pvap	1091.09	kPa	418.77	Calculated Property
Pvap	1903.99	kPa	448.03	Calculated Property
Pvap	3083.95	kPa	477.29	Calculated Property
Pvap	4701.97	kPa	506.55	Calculated Property
Pvap	[9.02e-04; 4642.15]	kPa	[175.15; 506.85]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			7.61104e+01
Coefficient B			-6.28858e+03
Coefficient C			-9.18586e+00
Coefficient D			7.59537e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			175.15
Temperature range, max.			506.85
Pvap	9.02e-04	kPa	175.15	Calculated Property
Pvap	0.09	kPa	212.01	Calculated Property
Pvap	1.89	kPa	248.86	Calculated Property
Pvap	16.03	kPa	285.72	Calculated Property
Pvap	77.10	kPa	322.57	Calculated Property
Pvap	254.99	kPa	359.43	Calculated Property
Pvap	654.11	kPa	396.28	Calculated Property
Pvap	1406.48	kPa	433.14	Calculated Property
Pvap	2670.52	kPa	469.99	Calculated Property
Pvap	4642.15	kPa	506.85	Calculated Property
Pvap	[9.06e-04; 4664.54]	kPa	[175.15; 506.80]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			7.85873e+01
Coefficient B			-6.36277e+03
Coefficient C			-9.58632e+00
Coefficient D			8.25370e-06
Coefficient E			0.00000e+00
Temperature range, min.			175.15
Temperature range, max.			506.80
Pvap	9.06e-04	kPa	175.15	Calculated Property
Pvap	0.09	kPa	212.00	Calculated Property
Pvap	1.90	kPa	248.85	Calculated Property
Pvap	16.12	kPa	285.70	Calculated Property
Pvap	77.21	kPa	322.55	Calculated Property
Pvap	254.55	kPa	359.40	Calculated Property
Pvap	651.98	kPa	396.25	Calculated Property
Pvap	1402.54	kPa	433.10	Calculated Property
Pvap	2670.14	kPa	469.95	Calculated Property
Pvap	4664.54	kPa	506.80	Calculated Property
Pvap	[9.20; 97.56]	kPa	[274.91; 328.99]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42844e+01
Coefficient B			-2.68119e+03
Coefficient C			-5.26900e+01
Reference			Polák and Mertl, 1965
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			274.91
Temperature range, max.			328.99
Pvap	9.20	kPa	274.91	Calculated Property
Pvap	12.64	kPa	280.92	Calculated Property
Pvap	17.08	kPa	286.93	Calculated Property
Pvap	22.74	kPa	292.94	Calculated Property
Pvap	29.86	kPa	298.95	Calculated Property
Pvap	38.70	kPa	304.95	Calculated Property
Pvap	49.56	kPa	310.96	Calculated Property
Pvap	62.75	kPa	316.97	Calculated Property
Pvap	78.63	kPa	322.98	Calculated Property
Pvap	97.56	kPa	328.99	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1068.84; 328.09]	kg/m3	[175.15; 506.85]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.28422e+01
Coefficient B			2.42800e-01
Coefficient C			5.06860e+02
Coefficient D			2.54900e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			175.15
Temperature range, max.			506.85
ρl	1068.84	kg/m3	175.15	Calculated Property
ρl	1029.42	kg/m3	212.01	Calculated Property
ρl	987.81	kg/m3	248.86	Calculated Property
ρl	943.48	kg/m3	285.72	Calculated Property
ρl	895.65	kg/m3	322.57	Calculated Property
ρl	843.10	kg/m3	359.43	Calculated Property
ρl	783.70	kg/m3	396.28	Calculated Property
ρl	713.19	kg/m3	433.14	Calculated Property
ρl	619.89	kg/m3	469.99	Calculated Property
ρl	328.09	kg/m3	506.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 2.70e-05]	N/m	[175.15; 505.89]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-5.32490e-02
Coefficient B			2.57220e+00
Coefficient C			-2.20270e+00
Coefficient D			-8.53490e-04
Coefficient E			-1.18350e-06
Comment			ChemSep eq 16, SurfaceTension, ChemSep Tmax 506.55 K
Temperature range, min.			175.15
Temperature range, max.			505.89
γ	0.04	N/m	175.15	Calculated Property
γ	0.04	N/m	211.90	Calculated Property
γ	0.03	N/m	248.65	Calculated Property
γ	0.03	N/m	285.40	Calculated Property
γ	0.02	N/m	322.14	Calculated Property
γ	0.02	N/m	358.89	Calculated Property
γ	0.01	N/m	395.64	Calculated Property
γ	0.01	N/m	432.39	Calculated Property
γ	0.00	N/m	469.14	Calculated Property
γ	2.70e-05	N/m	505.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.00; 0.12]	W/m×K	[175.15; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			-2.32570e+04
Coefficient B			-1.73800e-01
Coefficient C			1.02870e+07
Coefficient D			-6.92430e+10
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			175.15
Temperature range, max.			1000.00
λ	0.00	W/m×K	175.15	Calculated Property
λ	0.01	W/m×K	266.80	Calculated Property
λ	0.02	W/m×K	358.45	Calculated Property
λ	0.03	W/m×K	450.10	Calculated Property
λ	0.04	W/m×K	541.75	Calculated Property
λ	0.05	W/m×K	633.40	Calculated Property
λ	0.06	W/m×K	725.05	Calculated Property
λ	0.08	W/m×K	816.70	Calculated Property
λ	0.10	W/m×K	908.35	Calculated Property
λ	0.12	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.20; 0.12]	W/m×K	[175.15; 386.15]	ChemSep v8.3 pure component data
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-2.84160e-01
Coefficient B			2.71860e+01
Coefficient C			-9.44570e-01
Coefficient D			8.39740e-04
Coefficient E			-2.44120e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			175.15
Temperature range, max.			386.15
λ	0.20	W/m×K	175.15	Calculated Property
λ	0.19	W/m×K	198.59	Calculated Property
λ	0.19	W/m×K	222.04	Calculated Property
λ	0.18	W/m×K	245.48	Calculated Property
λ	0.17	W/m×K	268.93	Calculated Property
λ	0.16	W/m×K	292.37	Calculated Property
λ	0.15	W/m×K	315.82	Calculated Property
λ	0.14	W/m×K	339.26	Calculated Property
λ	0.13	W/m×K	362.71	Calculated Property
λ	0.12	W/m×K	386.15	Calculated Property

Similar Compounds

Find more compounds similar to Acetic acid, methyl ester.

Mixtures

• Acetic acid, methyl ester + Methyl Alcohol
• Ethanol + Acetic acid, methyl ester
• 1,2-Ethanediol + TETRAMETHYLAMMONIUM CHLORIDE + Acetic acid, methyl ester
• 1-Propanol + Acetic acid, methyl ester + Water
• Acetic acid, methyl ester + Water
• Acetic acid + Acetic acid, methyl ester
• Acetic acid, methyl ester + LACTIC ACID, ETHYL ESTER
• Acetic acid, methyl ester + LACTIC ACID, ETHYL ESTER + Methyl Alcohol
• Paraldehyde + Acetic acid, methyl ester
• Acetic acid, methyl ester + Propanoic acid
• Methyl propionate + Acetic acid, methyl ester
• Methyl propionate + Acetic acid, methyl ester + Water
• Dimethyl Sulfoxide + Acetic acid, methyl ester
• Dimethyl Sulfoxide + Acetic acid, methyl ester + Methyl Alcohol
• Magnesium chloride + Acetic acid, methyl ester + Methyl Alcohol
• Heptane + Acetic acid, methyl ester
• Acetic acid, methyl ester + Nonane
• Undecane + Acetic acid, methyl ester
• Tridecane + Acetic acid, methyl ester
• Pentadecane + Acetic acid, methyl ester

Find more mixtures with Acetic acid, methyl ester.

Sources

• KDB Vapor Pressure Data
• 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.
• Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• (Liquid + liquid) equilibria of (water + 1-propanol + solvent) at T = 298.2K
• Isothermal vapour liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate system, and in five binary subsystems
• Volumetric property for carbon dioxide + methyl acetate system at 313.15K
• Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
• Multiphase equilibria for mixtures containing water, acetic acid, propionic acid, methyl acetate and methyl propionate
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Experimental measurements of vapor liquid equilibria at low pressure: Systems containing alcohols, esters and organic acids
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Excess molar volumes and excess molar enthalpies for binary mixtures of 1,2-dichloropropane with methyl ethanoate, methyl propanoate, and methyl butanoate at T = 298.15K
• Vapor-liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography
• Isobaric vapor-liquid equilibrium data for the binary system methyl acetate + isopropyl acetate and the quaternary system methyl acetate + methanol + isopropanol + isopropyl acetate at 101.3 kPa
• Vapor-liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
• Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
• Effect of bivalent cation inorganic salts on isobaric vapor-liquidequilibrium of methyl acetate - methanol system
• Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Measurement and correlation of solubility of D-camphor-10-sulfonic acid in pure solvents
• Separation of methyl acetate + methanol azeotropic mixture using ionic liquids as entrainers
• Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
• Isobaric vapor-liquid equilibrium for methyl acetate + methanol system containing different ionic liquids at 101.3 kPa
• Solution thermodynamics of simvastatin in pure solvents and binary solvent mixtures
• Experimental isobaric vapor-liquid equilibrium for the binary and ternary systems with methanol, methyl acetate and dimethyl sulfoxide at 101.3 kPa
• Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Isobaric vapor-liquid equilibrium for methanol + methyl acetate with ionic liquids [OMMIM][Tf2N] and [OMIM][Tf2N] as entrainers at 101.3 kPa
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
• Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
• Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
• Molecular interactions in (2,4,6-trimethyl-1,3,5-trioxane + n-alkyl acetates) at T=(298.15, 303.15, and 308.15) K
• Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
• Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
• Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
• Physical and excess properties of (methyl acetate + methanol + 1-octyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide) and its binary mixtures at T = 298.15 K and atmospheric pressure
• Ternary excess molar volumes of {methyltrioctylammonium bis(trifluoromethylsulfonyl)imide + ethanol + methyl acetate, or ethyl acetate} systems at T = (298.15, 303.15, and 313.15) K
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Density, refraction index and vapor-liquid equilibria of N-methyl-2-hydroxyethylammonium butyrate plus (methyl acetate or ethyl acetate or propyl acetate) at several temperatures
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Thermodynamics of 4'-bromomethyl-2-cyanobiphenyl in different solvents
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Solid-liquid phase equilibrium and mixing properties of 2-Cyano-4'-methylbiphenyl in pure solvents
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
• Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
• Ternary liquid-liquid equilibria for systems containing (dimethyl carbonate or methyl acetate + methanol + 1-methylmidazole hydrogen sulfate) at 298.15 K and 318.15 K
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
• Effects of temperature and concentration on interactions in (methanol + ethyl acetate) and (ethanol + methyl acetate or ethyl acetate) systems: insights from apparent molar volume and apparent molar isentropic compressibility study
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
• Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
• Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
• Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
• Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
• Solubility of Agomelatine Crystal Form I and Form II in Pure Solvents and (Isopropanol + Water) Mixtures
• Measurement and Correlation of the Solubility of Vanillic Acid in Eight Pure and Water + Ethanol Mixed Solvents at Temperatures from (293.15 to 323.15) K
• Measurement and modeling of high pressure VLE for methyl acetate or ethyl acetate with 2-butanol. Isobaric data at 1.5 MPa
• A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
• Differential Scanning Calorimetry Data and Solubility of Rosmarinic Acid in Different Pure Solvents and in Binary Mixtures (Methyl Acetate + Water) and (Ethyl Acetate + Water) from 293.2 to 313.2 K
• Measurement and Correlation of the Solubility of p-Coumaric Acid in Nine Pure and Water + Ethanol Mixed Solvents at Temperatures from 293.15 to 333.15 K
• Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
• Solubilities of Three Flavonoids in Different Natural Deep Eutectic Solvents at T = (288.15 to 328.15) K
• Determination of Vapor Liquid Equilibrium of Methyl Acetate + Methanol + 1-Alkyl-3-methylimidazolium Dialkylphosphates at 101.3 kPa
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
• Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
• Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Solution Thermodynamics of Benzotriazole in Different Pure Solvents
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• Isobaric Vapor-Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa
• Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
• Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
• Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
• Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
• Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
• Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
• Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
• Measurement and Correlation of the Solubility of Tetramethylpyrazine in Nine Monosolvents and Two Binary Solvent Systems
• Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
• Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Measurement and Correlation of the Solubility of Aminocaproic Acid in Some Pure and Binary Solvents
• Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
• 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
• Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Liquid-Liquid Equilibria of Methyl Acetate + Methanol + Octane or Nonane
• Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
• Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Excess Molar Enthalpies of Methyl Acetate and (1-Propanol, 2-Propanol, 1-Butanol, 2-Butanol, and 1-Pentanol) at T = (298.15 and 308.15) K and P = (5.0 and 10.0) MPa
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + Ethyl Lactate and Methyl Acetate + Ethyl Lactate
• Solubility of 1H-1,2,4-Triazole in Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, Ethyl Formate, Methyl Acetate, Ethyl Acetate, and Butyl Acetate at (283 to 363) K
• Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
• Liquid-Liquid Equilibrium of Ternary and Quaternary Systems Including Methyl Acetate, Benzene, Toluene, and Water at 283.2 K under Atmosphere
• Vapor-Liquid Equilibrium and Liquid-Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Acetate
• Critical Assessment of CO2 Solubility in Volatile Solvents at 298.15 K
• Article Isobaric Vapor Liquid Equilibrium for Methanol + Methyl Acetate + 1-Octyl-3-methylimidazolium Hexafluorophosphate at 101.3 kPa
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
• Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
• Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa
• Measurement and Correlation of Solubility and Dissolution Thermodynamic Properties of Furan-2-carboxylic Acid in Pure and Binary Solvents
• Experimental VLE data of Methyl Acetate or Ethyl Acetate with 2-Butanol at 0.3 and 0.6 MPa. Quality assessment and predictions.
• Experimental Measurement and Correlation of Solubility Data and Thermodynamic Properties of Protocatechuic Acid in Four Organic Solvents
• Liquid Liquid Equilibrium for Ternary System Methanol + Methyl Acetate + 1,3-Dimethylimidazolium Dimethylphosphate at Several Temperatures and Atmospheric Pressure
• Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Liquid Liquid Equilibria of Mixtures Containing Methyl Acetate + Methanol + Hexane or Heptane
• Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
• 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
• Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
• Solubility of Valsartan in Different Organic Solvents and Ethanol + Water Binary Mixtures from (278.15 to 313.15) K
• Isobaric Vapor-Liquid Equilibria for the Binary Systems Benzene + Methyl Ethanoate, Benzene + Butyl Ethanoate, and Benzene + Methyl Heptanoate at 101.31kPa
• Solubility of Captopril in 2-Propanol, Acetone, Acetonitrile, Methyl Acetate, Ethyl Acetate, and Butyl Acetate
• Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
• Surface Tension Data of Aqueous Binary Mixtures of Methyl, Ethyl, Propyl, and Butyl Acetates at 298.15 K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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