Chemical Properties of Methyl methacrylate (CAS 80-62-6)

InChI

InChI=1S/C5H8O2/c1-4(2)5(6)7-3/h1H2,2-3H3

InChI Key

VVQNEPGJFQJSBK-UHFFFAOYSA-N

Formula

C5H8O2

SMILES

C=C(C)C(=O)OC

Molecular Weight¹

100.12

CAS

80-62-6

Other Names

• 2-(methoxycarbonyl)-1-propene
• 2-Methyl-2-propenoic acid methyl ester
• 2-Methylacrylic acid, methyl ester
• 2-Methylacrylic, methyl ester
• 2-Propenoic acid, 2-methyl-, methyl ester
• 2-methylpropenoic acid, methyl ester
• Acryester M
• Acrylic acid, 2-methyl-, methyl ester
• CH2=C(CH3)COOCH3
• Diakon
• MMA
• Metakrylan metylu
• Methacrylate de methyle
• Methacrylic acid methyl ester
• Methacrylsaeuremethyl ester
• Methyl 2-methyl-2-propenoate
• Methyl ester of 2-methyl-2-propenoic acid
• Methyl methacrylate monomer
• Methyl methylacrylate
• Methyl «alpha»-methylacrylate
• Methyl-methacrylat
• Methyl-«alpha»-methacrylate
• Methylester kyseliny methakrylove
• Methylmethacrylaat
• Metil metacrilato
• Monocite methacrylate monomer
• NCI-C50680
• NSC 4769
• Paladon
• Pegalan
• Rcra waste number U162
• TEB 3K
• methacrylic acid, methyl ester
• methyl 2-methylpropenoate

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• 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_subH : Enthalpy of sublimation 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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3785		Relay (1.0) Calculated Property
PAff	831.40	kJ/mol	NIST
BasG	800.50	kJ/mol	NIST
ΔcH°liquid	-2724.60 ± 4.00	kJ/mol	NIST
ΔfH°gas	[-348.70; -331.00]	kJ/mol
ΔfH°gas	-348.70	kJ/mol	NIST
ΔfH°gas	-342.30	kJ/mol	NIST
ΔfH°gas	-331.00	kJ/mol	NIST
ΔfH°liquid	[-388.80; -382.40]	kJ/mol
ΔfH°liquid	-382.40	kJ/mol	NIST
ΔfH°liquid	-388.80 ± 4.00	kJ/mol	NIST
ΔfusH°	10.48	kJ/mol	Joback Calculated Property
ΔvapH°	40.10	kJ/mol	NIST
IE	[9.70; 10.28]	eV
IE	9.70	eV	NIST
IE	10.06	eV	NIST
IE	10.28	eV	NIST
log10WS	-0.80		Aq. Solubility Prediction
logPoct/wat	0.735		Crippen Calculated Property
McVol	84.450	ml/mol	McGowan Calculated Property
Pc	3690.97	kPa	Joback Calculated Property
Inp	[666.00; 732.00]
Inp	714.30		NIST
Inp	717.33		NIST
Inp	716.28		NIST
Inp	713.44		NIST
Inp	696.00		NIST
Inp	700.00		NIST
Inp	694.00		NIST
Inp	666.00		NIST
Inp	670.00		NIST
Inp	699.00		NIST
Inp	677.00		NIST
Inp	677.00		NIST
Inp	677.00		NIST
Inp	677.00		NIST
Inp	732.00		NIST
Inp	710.40		NIST
Inp	723.00		NIST
Inp	672.00		NIST
Inp	710.00		NIST
Inp	696.00		NIST
Inp	714.00		NIST
Inp	699.00		NIST
Inp	696.00		NIST
Inp	696.00		NIST
Inp	699.00		NIST
Inp	677.00		NIST
Inp	699.00		NIST
Inp	710.00		NIST
Inp	732.00		NIST
Inp	714.30		NIST
Inp	700.00		NIST
Inp	677.00		NIST
I	[1002.00; 1010.00]
I	1010.00		NIST
I	1002.00		NIST
I	1008.00		NIST
I	1002.00		NIST
I	1008.00		NIST
S°liquid	266.20	J/mol×K	NIST
Tboil	[372.70; 374.15]	K
Tboil	373.55 ± 0.40	K	NIST
Tboil	373.55 ± 0.30	K	NIST
Tboil	373.55 ± 0.30	K	NIST
Tboil	373.70	K	NIST
Tboil	373.55 ± 0.40	K	NIST
Tboil	373.55 ± 0.30	K	NIST
Tboil	373.55 ± 0.30	K	NIST
Tboil	374.15	K	NIST
Tboil	373.25 ± 0.50	K	NIST
Tboil	Outlier 372.70 ± 3.00	K	NIST
Tboil	373.15 ± 1.20	K	NIST
Tc	557.90	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tfus	[225.00; 225.60]	K
Tfus	225.26	K	Aq. Solubility Prediction
Tfus	225.60	K	NIST
Tfus	225.60	K	NIST
Tfus	225.00	K	NIST
Tfus	225.60 ± 0.20	K	NIST
Tfus	225.50 ± 0.20	K	NIST
Tfus	225.15 ± 0.40	K	NIST
Ttriple	225.59 ± 0.02	K	NIST
Vc	0.320	m3/kmol	Relay (1.0) Calculated Property

Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[146.24; 190.98]	J/mol×K	[368.78; 550.45]
Cp,gas	146.24	J/mol×K	368.78	Joback Calculated Property
Cp,gas	154.45	J/mol×K	399.06	Joback Calculated Property
Cp,gas	162.36	J/mol×K	429.34	Joback Calculated Property
Cp,gas	169.97	J/mol×K	459.61	Joback Calculated Property
Cp,gas	177.27	J/mol×K	489.89	Joback Calculated Property
Cp,gas	184.27	J/mol×K	520.17	Joback Calculated Property
Cp,gas	190.98	J/mol×K	550.45	Joback Calculated Property
Cp,liquid	[188.49; 215.30]	J/mol×K	[293.00; 300.00]
Cp,liquid	188.49	J/mol×K	293.00	NIST
Cp,liquid	191.09	J/mol×K	298.15	NIST
Cp,liquid	215.30	J/mol×K	298.15	NIST
Cp,liquid	215.30	J/mol×K	298.15	NIST
Cp,liquid	210.55	J/mol×K	298.15	NIST
Cp,liquid	192.40	J/mol×K	300.00	NIST
Cp,solid	150.20	J/mol×K	210.00	NIST
η	[0.0003398; 0.0006808]	Pa×s	[283.15; 353.15]
η	0.0006808	Pa×s	283.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0006808	Pa×s	283.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0006337	Pa×s	288.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0006337	Pa×s	288.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0005899	Pa×s	293.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0005899	Pa×s	293.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0005540	Pa×s	298.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0005540	Pa×s	298.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0005248	Pa×s	303.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0005248	Pa×s	303.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0004956	Pa×s	308.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0004956	Pa×s	308.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0004719	Pa×s	313.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0004719	Pa×s	313.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0004497	Pa×s	318.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0004497	Pa×s	318.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0004294	Pa×s	323.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0004294	Pa×s	323.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0004100	Pa×s	328.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0004100	Pa×s	328.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0003938	Pa×s	333.15	Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
η	0.0003938	Pa×s	333.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0003636	Pa×s	343.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
η	0.0003398	Pa×s	353.15	Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
ΔfusH	[12.24; 14.44]	kJ/mol	[225.00; 225.59]
ΔfusH	12.24	kJ/mol	225.00	NIST
ΔfusH	12.24	kJ/mol	225.00	NIST
ΔfusH	13.45	kJ/mol	225.50	NIST
ΔfusH	13.45	kJ/mol	225.50	NIST
ΔfusH	14.44	kJ/mol	225.59	NIST
ΔsubH	60.70	kJ/mol	208.50	NIST
ΔvapH	[33.30; 39.00]	kJ/mol	[333.00; 340.50]
ΔvapH	37.90	kJ/mol	333.00	NIST
ΔvapH	37.70	kJ/mol	333.00	NIST
ΔvapH	39.00	kJ/mol	337.00	NIST
ΔvapH	38.00	kJ/mol	339.00	NIST
ΔvapH	38.80 ± 0.10	kJ/mol	340.50	NIST
ΔvapH	36.30 ± 0.20	kJ/mol	340.50	NIST
ΔvapH	33.30 ± 0.40	kJ/mol	340.50	NIST
ρl	[914.66; 949.10]	kg/m3	[288.15; 318.15]
ρl	949.10	kg/m3	288.15	Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
ρl	943.38	kg/m3	293.15	Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl	943.37	kg/m3	293.15	Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
ρl	937.63	kg/m3	298.15	Volumetric Properties of 3-Methylbutyl Ethanoate with Ethyl Acrylate, Butyl Acrylate, Methyl Methacrylate, and Styrene at 25 C
ρl	937.63	kg/m3	298.15	Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
ρl	937.65	kg/m3	298.15	Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
ρl	937.64	kg/m3	298.15	Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl	931.90	kg/m3	303.15	Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl	931.89	kg/m3	303.15	Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
ρl	926.15	kg/m3	308.15	Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
ρl	926.16	kg/m3	308.15	Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl	920.41	kg/m3	313.15	Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
ρl	920.42	kg/m3	313.15	Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ρl	914.66	kg/m3	318.15	Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
ρl	914.67	kg/m3	318.15	Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
ΔfusS	[59.65; 64.00]	J/mol×K	[225.50; 225.59]
ΔfusS	59.65	J/mol×K	225.50	NIST
ΔfusS	59.65	J/mol×K	225.50	NIST
ΔfusS	64.00	J/mol×K	225.59	NIST
csound,fluid	[1152.00; 1182.00]	m/s	[298.15; 308.15]
csound,fluid	1181.00	m/s	298.15	Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
csound,fluid	1182.00	m/s	298.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid	1153.00	m/s	308.15	Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
csound,fluid	1152.00	m/s	308.15	Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.02; 3783.32]	kPa	[224.95; 564.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.28053e+02
Coefficient B			-8.95480e+03
Coefficient C			-1.71457e+01
Coefficient D			1.47176e-05
Temperature range, min.			224.95
Temperature range, max.			564.00
Pvap	0.02	kPa	224.95	Calculated Property
Pvap	0.58	kPa	262.62	Calculated Property
Pvap	5.74	kPa	300.29	Calculated Property
Pvap	29.95	kPa	337.97	Calculated Property
Pvap	103.59	kPa	375.64	Calculated Property
Pvap	273.70	kPa	413.31	Calculated Property
Pvap	605.13	kPa	450.98	Calculated Property
Pvap	1189.92	kPa	488.66	Calculated Property
Pvap	2170.45	kPa	526.33	Calculated Property
Pvap	3783.32	kPa	564.00	Calculated Property

Similar Compounds

Find more compounds similar to Methyl methacrylate.

Mixtures

• Benzonitrile + Methyl methacrylate
• sodium chloride + Methyl methacrylate + Water
• Methyl methacrylate + Water
• 1-Butanol + Methyl methacrylate + Water
• 1-Propanol + Methyl methacrylate + Water
• Formamide, N,N-dimethyl- + Methyl methacrylate
• N,N-Dimethylacetamide + Methyl methacrylate
• Toluene + Methyl methacrylate
• Methyl methacrylate + 2-Propenoic acid, butyl ester
• Toluene + Methyl methacrylate + 2-Propenoic acid, butyl ester
• Acetonitrile + Methyl methacrylate
• 1-Butanol, 3-methyl-, acetate + Methyl methacrylate
• Carbon dioxide + Methyl methacrylate
• 1-Butanol + Methyl methacrylate + Cyclohexane
• Benzene + 1-Butanol + Methyl methacrylate
• Toluene + 1-Butanol + Methyl methacrylate
• p-Xylene + 1-Butanol + Methyl methacrylate
• 1-Butanol + Benzene, ethyl- + Methyl methacrylate
• 1-Pentanol + Methyl methacrylate + Cyclohexane
• Benzene + 1-Pentanol + Methyl methacrylate

Find more mixtures with Methyl methacrylate.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Volumetric Properties of 3-Methylbutyl Ethanoate with Ethyl Acrylate, Butyl Acrylate, Methyl Methacrylate, and Styrene at 25 C
• Liquid liquid equilibria for the ternary systems water + 1-propanol + methyl methacrylate, +butyl methacrylate, and +isobutyl methacrylate
• Liquid liquid equilibria of water + 1-butanol + methyl methacrylate or butyl methacrylate or isobutyl methacrylate at 288.15K and 318.15K
• Activity coefficients and partial molar excess enthalpies at infinite dilution for four esters in water
• Liquid-liquid equilibria for systems of water + methanol + methyl anthranilate at several temperatures
• Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
• Combined effects of salinity and temperature on the solubility of organic compounds
• Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
• Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
• Densities, speeds of sound and excess properties of (benzonitrile + methyl methacrylate, or + ethyl methacrylate, or + n-butyl methacrylate) binary mixtures at temperatures from 293.15 K to 318.15 K
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
• Methyl Methacrylate + Carbon Dioxide Phase Equilibria at High Pressures
• Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Liquid-Liquid Equilibria for the Ternary Systems Water + 2-Propanol + Methyl Methacrylate, + Butyl Methacrylate, and + Isobutyl Methacrylate
• Liquid-Liquid Equilibria of Water + 2-Butanol + (Methyl Methacrylate or Butyl Methacrylate or Isobutyl Methacrylate) at (288.2 and 318.2) K
• Phase Behavior Studies of 2-Hydroxyethyl Methacrylate and Methyl Methacrylate in High-Pressure Carbon Dioxide
• Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
• Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook

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