Chemical Properties of 2-Butanone (CAS 78-93-3)

InChI

InChI=1S/C4H8O/c1-3-4(2)5/h3H2,1-2H3

InChI Key

ZWEHNKRNPOVVGH-UHFFFAOYSA-N

Formula

C4H8O

SMILES

CCC(C)=O

Molecular Weight¹

72.11

CAS

78-93-3

Other Names

• 2-Butanal
• 2-Oxobutane
• 2-butanone (MEK)
• 2-butanone (MEK; methyl ethyl ketone)
• 3-Butanone
• Acetone, methyl-
• Aethylmethylketon
• Butanone 2
• C2H5COCH3
• Ethyl methyl cetone
• Ethylmethylketon
• Ketone, ethyl methyl
• Ketone, methyl ethyl
• MEK
• Meetco
• Methyl acetone
• Metiletilchetone
• Metyloetyloketon
• Rcra waste number U159
• UN 1193
• butan-2-one
• butanone
• ethyl methyl ketone
• methyl ethyl ketone

• 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).
• EA : Electron affinity (eV).
• 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_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.
• 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.
• 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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (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	0.3200		KDB
PAff	827.30	kJ/mol	NIST
Tig	789.26	K	KDB
BasG	795.50	kJ/mol	NIST
ΔcH°liquid	[-2444.20; -2436.30]	kJ/mol
ΔcH°liquid	-2444.20	kJ/mol	NIST
ΔcH°liquid	-2438.40	kJ/mol	NIST
ΔcH°liquid	-2436.30 ± 1.50	kJ/mol	NIST
μ	3.30	debye	KDB
η	[0.0003730; 0.0004011]	Pa×s
η	0.0003880	Pa×s	A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
η	0.0004011	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η	0.0003760	Pa×s	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K
η	0.0003730	Pa×s	Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
EA	9.99e-04	eV	NIST
LFL	1.80	% in Air	KDB
UFL	11.50	% in Air	KDB
Tflash,cc	267.59	K	KDB
Tflash,oc	266.48	K	KDB
ΔfG°	-146.20	kJ/mol	KDB
ΔfH°gas	[-238.70; -238.10]	kJ/mol
ΔfH°gas	-238.50	kJ/mol	KDB
ΔfH°gas	-238.60 ± 0.84	kJ/mol	NIST
ΔfH°gas	-238.70 ± 0.96	kJ/mol	NIST
ΔfH°gas	-238.10	kJ/mol	NIST
ΔfH°liquid	[-279.00; -273.30]	kJ/mol
ΔfH°liquid	-273.30 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-279.00	kJ/mol	NIST
ΔfusH°	7.72	kJ/mol	Joback Calculated Property
ΔvapH°	[32.00; 35.51]	kJ/mol
ΔvapH°	34.92	kJ/mol	NIST
ΔvapH°	34.73	kJ/mol	NIST
ΔvapH°	34.80 ± 0.10	kJ/mol	NIST
ΔvapH°	35.51 ± 0.08	kJ/mol	NIST
ΔvapH°	34.50 ± 0.10	kJ/mol	NIST
ΔvapH°	Outlier 32.00 ± 0.01	kJ/mol	NIST
IE	[9.46; 9.70]	eV
IE	9.52 ± 0.04	eV	NIST
IE	9.52	eV	NIST
IE	Outlier 9.70	eV	NIST
IE	9.52	eV	NIST
IE	9.53 ± 0.01	eV	NIST
IE	9.53 ± 0.01	eV	NIST
IE	9.54 ± 0.03	eV	NIST
IE	9.52	eV	NIST
IE	9.54 ± 0.01	eV	NIST
IE	9.54 ± 0.01	eV	NIST
IE	9.51	eV	NIST
IE	9.48 ± 0.02	eV	NIST
IE	9.53 ± 0.01	eV	NIST
IE	9.54 ± 0.03	eV	NIST
IE	9.50 ± 0.10	eV	NIST
IE	9.55 ± 0.03	eV	NIST
IE	9.46	eV	NIST
IE	9.49	eV	NIST
IE	9.56	eV	NIST
log10WS	[0.52; 0.52]
log10WS	0.52		Aq. Solubility Prediction
log10WS	0.52		Estimated Solubility
logPoct/wat	0.985		Crippen Calculated Property
McVol	68.790	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3998.00; 4390.00]	kPa
Pc	4207.00	kPa	KDB
Pc	4166.00 ± 15.00	kPa	NIST
Pc	4166.00 ± 3.00	kPa	NIST
Pc	4166.00 ± 3.00	kPa	NIST
Pc	4207.00 ± 10.00	kPa	NIST
Pc	4165.80 ± 20.68	kPa	NIST
Pc	4150.00 ± 34.50	kPa	NIST
Pc	3998.00 ± 202.65	kPa	NIST
Pc	Outlier 4390.00 ± 202.65	kPa	NIST
ρc	[251.65; 269.68]	kg/m3
ρc	269.68 ± 15.14	kg/m3	NIST
ρc	251.65 ± 4.33	kg/m3	NIST
Inp	[533.00; 622.00]
Inp	549.00		NIST
Inp	575.92		NIST
Inp	574.45		NIST
Inp	572.75		NIST
Inp	572.34		NIST
Inp	571.45		NIST
Inp	572.61		NIST
Inp	572.88		NIST
Inp	573.87		NIST
Inp	575.19		NIST
Inp	576.69		NIST
Inp	578.90		NIST
Inp	581.30		NIST
Inp	603.27		NIST
Inp	602.14		NIST
Inp	601.20		NIST
Inp	599.13		NIST
Inp	596.14		NIST
Inp	598.30		NIST
Inp	601.92		NIST
Inp	602.60		NIST
Inp	603.82		NIST
Inp	605.54		NIST
Inp	597.00		NIST
Inp	578.66		NIST
Inp	578.89		NIST
Inp	570.79		NIST
Inp	Outlier 538.30		NIST
Inp	607.25		NIST
Inp	598.20		NIST
Inp	609.38		NIST
Inp	548.59		NIST
Inp	575.77		NIST
Inp	575.30		NIST
Inp	575.00		NIST
Inp	574.90		NIST
Inp	574.71		NIST
Inp	574.80		NIST
Inp	574.97		NIST
Inp	574.76		NIST
Inp	576.00		NIST
Inp	575.00		NIST
Inp	575.00		NIST
Inp	575.00		NIST
Inp	585.00		NIST
Inp	587.00		NIST
Inp	582.00		NIST
Inp	583.00		NIST
Inp	570.00		NIST
Inp	Outlier 537.50		NIST
Inp	597.80		NIST
Inp	598.00		NIST
Inp	599.60		NIST
Inp	580.00		NIST
Inp	581.00		NIST
Inp	Outlier 538.00		NIST
Inp	591.00		NIST
Inp	580.00		NIST
Inp	Outlier 541.00		NIST
Inp	Outlier 542.00		NIST
Inp	Outlier 533.00		NIST
Inp	Outlier 534.00		NIST
Inp	544.00		NIST
Inp	579.00		NIST
Inp	556.00		NIST
Inp	543.00		NIST
Inp	557.00		NIST
Inp	552.30		NIST
Inp	574.00		NIST
Inp	552.00		NIST
Inp	553.00		NIST
Inp	551.00		NIST
Inp	569.00		NIST
Inp	Outlier 533.00		NIST
Inp	551.00		NIST
Inp	554.00		NIST
Inp	590.00		NIST
Inp	575.00		NIST
Inp	551.00		NIST
Inp	547.00		NIST
Inp	548.00		NIST
Inp	549.00		NIST
Inp	554.00		NIST
Inp	602.00		NIST
Inp	543.00		NIST
Inp	543.00		NIST
Inp	582.70		NIST
Inp	Outlier 622.00		NIST
Inp	600.00		NIST
Inp	601.00		NIST
Inp	605.00		NIST
Inp	604.00		NIST
Inp	597.00		NIST
Inp	602.00		NIST
Inp	581.60		NIST
Inp	596.00		NIST
Inp	560.00		NIST
Inp	594.70		NIST
Inp	605.00		NIST
Inp	605.00		NIST
Inp	606.00		NIST
Inp	604.00		NIST
Inp	604.00		NIST
Inp	569.00		NIST
Inp	602.00		NIST
Inp	600.00		NIST
Inp	603.00		NIST
Inp	575.00		NIST
Inp	577.00		NIST
Inp	585.00		NIST
Inp	572.00		NIST
Inp	579.00		NIST
Inp	570.00		NIST
Inp	601.00		NIST
Inp	611.00		NIST
Inp	576.00		NIST
Inp	577.00		NIST
Inp	576.00		NIST
Inp	577.00		NIST
Inp	575.00		NIST
Inp	580.00		NIST
Inp	577.00		NIST
Inp	576.00		NIST
Inp	578.00		NIST
Inp	575.00		NIST
Inp	555.00		NIST
Inp	559.00		NIST
Inp	560.00		NIST
Inp	573.00		NIST
Inp	602.00		NIST
Inp	592.00		NIST
Inp	592.00		NIST
Inp	578.00		NIST
Inp	578.00		NIST
Inp	600.00		NIST
Inp	598.00		NIST
Inp	598.00		NIST
Inp	591.00		NIST
Inp	601.80		NIST
Inp	589.00		NIST
Inp	597.00		NIST
Inp	600.00		NIST
Inp	600.00		NIST
Inp	571.00		NIST
Inp	569.00		NIST
Inp	570.06		NIST
Inp	604.00		NIST
Inp	575.00		NIST
Inp	613.00		NIST
Inp	603.00		NIST
Inp	564.00		NIST
Inp	576.00		NIST
Inp	592.00		NIST
Inp	570.00		NIST
Inp	572.00		NIST
Inp	575.00		NIST
Inp	577.00		NIST
Inp	580.00		NIST
Inp	580.00		NIST
Inp	Outlier 622.00		NIST
Inp	602.00		NIST
Inp	583.00		NIST
Inp	603.00		NIST
Inp	569.00		NIST
Inp	597.00		NIST
Inp	551.00		NIST
Inp	600.00		NIST
Inp	600.00		NIST
Inp	577.00		NIST
Inp	604.00		NIST
Inp	590.00		NIST
Inp	598.00		NIST
Inp	598.00		NIST
Inp	575.00		NIST
Inp	606.00		NIST
Inp	579.00		NIST
Inp	575.00		NIST
Inp	601.00		NIST
Inp	590.00		NIST
Inp	596.00		NIST
Inp	551.00		NIST
Inp	612.00		NIST
Inp	582.00		NIST
Inp	591.00		NIST
Inp	578.00		NIST
Inp	589.00		NIST
Inp	600.00		NIST
Inp	604.00		NIST
Inp	572.00		NIST
Inp	578.00		NIST
Inp	578.00		NIST
Inp	578.00		NIST
Inp	570.00		NIST
Inp	570.00		NIST
Inp	572.00		NIST
Inp	579.00		NIST
Inp	559.00		NIST
Inp	560.00		NIST
Inp	598.00		NIST
Inp	575.00		NIST
Inp	577.00		NIST
Inp	567.00		NIST
Inp	568.00		NIST
Inp	552.00		NIST
Inp	579.00		NIST
Inp	580.00		NIST
Inp	579.00		NIST
Inp	579.00		NIST
Inp	575.00		NIST
Inp	Outlier 622.00		NIST
Inp	597.00		NIST
Inp	604.00		NIST
Inp	606.00		NIST
Inp	596.00		NIST
Inp	578.00		NIST
Inp	572.00		NIST
Inp	575.00		NIST
Inp	579.00		NIST
Inp	573.00		NIST
Inp	601.80		NIST
Inp	571.00		NIST
Inp	613.00		NIST
Inp	570.00		NIST
Inp	580.00		NIST
Inp	582.70		NIST
I	[866.00; 953.00]
I	917.39		NIST
I	922.33		NIST
I	925.59		NIST
I	928.27		NIST
I	931.34		NIST
I	935.77		NIST
I	940.31		NIST
I	943.44		NIST
I	Outlier 946.71		NIST
I	Outlier 949.95		NIST
I	937.60		NIST
I	938.60		NIST
I	Outlier 947.76		NIST
I	932.30		NIST
I	919.80		NIST
I	923.70		NIST
I	927.80		NIST
I	919.00		NIST
I	930.00		NIST
I	905.00		NIST
I	881.00		NIST
I	900.00		NIST
I	900.00		NIST
I	893.00		NIST
I	908.00		NIST
I	891.00		NIST
I	923.30		NIST
I	897.00		NIST
I	903.00		NIST
I	905.00		NIST
I	926.00		NIST
I	912.70		NIST
I	885.00		NIST
I	915.00		NIST
I	894.00		NIST
I	908.00		NIST
I	888.00		NIST
I	875.00		NIST
I	905.00		NIST
I	900.00		NIST
I	893.00		NIST
I	882.00		NIST
I	905.00		NIST
I	901.00		NIST
I	907.00		NIST
I	905.00		NIST
I	908.00		NIST
I	903.00		NIST
I	904.00		NIST
I	882.00		NIST
I	924.00		NIST
I	914.00		NIST
I	908.00		NIST
I	918.00		NIST
I	893.00		NIST
I	906.00		NIST
I	906.00		NIST
I	906.00		NIST
I	918.00		NIST
I	945.00		NIST
I	920.00		NIST
I	907.00		NIST
I	899.00		NIST
I	901.00		NIST
I	914.00		NIST
I	888.00		NIST
I	Outlier 866.00		NIST
I	901.00		NIST
I	Outlier 866.00		NIST
I	Outlier 866.00		NIST
I	906.00		NIST
I	912.00		NIST
I	890.00		NIST
I	923.00		NIST
I	911.00		NIST
I	Outlier 953.00		NIST
I	912.00		NIST
I	888.00		NIST
I	888.00		NIST
I	889.00		NIST
I	903.00		NIST
I	910.00		NIST
I	894.00		NIST
I	906.00		NIST
I	909.00		NIST
I	882.00		NIST
I	901.00		NIST
I	907.00		NIST
I	909.00		NIST
I	908.00		NIST
I	894.00		NIST
I	875.00		NIST
I	881.00		NIST
I	920.00		NIST
I	904.00		NIST
I	908.00		NIST
I	908.00		NIST
I	908.00		NIST
I	930.00		NIST
I	908.00		NIST
I	917.39		NIST
I	935.77		NIST
I	937.60		NIST
I	923.70		NIST
I	891.00		NIST
I	924.00		NIST
I	914.00		NIST
I	906.00		NIST
I	907.00		NIST
I	Outlier 866.00		NIST
I	912.00		NIST
I	905.00		NIST
I	903.00		NIST
I	897.00		NIST
I	885.00		NIST
I	875.00		NIST
S°liquid	[238.82; 241.40]	J/mol×K
S°liquid	239.00	J/mol×K	NIST
S°liquid	238.82	J/mol×K	NIST
S°liquid	241.40	J/mol×K	NIST
Tboil	[350.15; 354.15]	K
Tboil	352.85	K	Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
Tboil	352.68	K	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Tboil	352.72	K	Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa
Tboil	352.69	K	Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
Tboil	352.72	K	Isobaric Vapor-Liquid Equilibrium for 2-Butanone + Ethanol System Containing Different Ionic Liquids at 101.3 kPa
Tboil	352.78	K	Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
Tboil	352.68	K	Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 2-Butanone + 2-Butanol + Water System
Tboil	352.74	K	KDB
Tboil	352.71 ± 0.10	K	NIST
Tboil	352.75 ± 0.20	K	NIST
Tboil	352.67 ± 0.20	K	NIST
Tboil	352.75 ± 0.20	K	NIST
Tboil	352.72 ± 0.10	K	NIST
Tboil	352.71 ± 0.20	K	NIST
Tboil	352.35 ± 0.50	K	NIST
Tboil	352.80	K	NIST
Tboil	352.60 ± 0.40	K	NIST
Tboil	352.15 ± 0.40	K	NIST
Tboil	352.60 ± 0.30	K	NIST
Tboil	352.15 ± 0.50	K	NIST
Tboil	352.15 ± 0.40	K	NIST
Tboil	352.65 ± 0.50	K	NIST
Tboil	352.80	K	NIST
Tboil	352.71 ± 0.20	K	NIST
Tboil	352.71 ± 0.30	K	NIST
Tboil	353.20 ± 0.40	K	NIST
Tboil	352.50 ± 0.50	K	NIST
Tboil	352.73 ± 0.30	K	NIST
Tboil	352.71 ± 0.20	K	NIST
Tboil	352.83 ± 0.20	K	NIST
Tboil	353.00 ± 0.40	K	NIST
Tboil	353.00 ± 0.20	K	NIST
Tboil	352.70 ± 0.30	K	NIST
Tboil	352.75	K	NIST
Tboil	352.65 ± 0.30	K	NIST
Tboil	352.70 ± 0.30	K	NIST
Tboil	352.50 ± 0.50	K	NIST
Tboil	353.15 ± 1.50	K	NIST
Tboil	352.65 ± 1.00	K	NIST
Tboil	352.55 ± 1.00	K	NIST
Tboil	352.75 ± 1.00	K	NIST
Tboil	352.85 ± 1.00	K	NIST
Tboil	352.75 ± 1.00	K	NIST
Tboil	352.65 ± 1.00	K	NIST
Tboil	352.75 ± 1.00	K	NIST
Tboil	352.75 ± 1.00	K	NIST
Tboil	353.15 ± 1.00	K	NIST
Tboil	352.35 ± 0.50	K	NIST
Tboil	352.55 ± 0.50	K	NIST
Tboil	351.75 ± 0.50	K	NIST
Tboil	352.77 ± 0.30	K	NIST
Tboil	352.75 ± 1.00	K	NIST
Tboil	352.40 ± 1.00	K	NIST
Tboil	352.72 ± 0.30	K	NIST
Tboil	Outlier 350.65 ± 2.00	K	NIST
Tboil	352.80 ± 1.00	K	NIST
Tboil	352.65 ± 0.20	K	NIST
Tboil	352.75 ± 0.50	K	NIST
Tboil	353.15 ± 1.00	K	NIST
Tboil	352.65 ± 2.00	K	NIST
Tboil	351.65 ± 1.00	K	NIST
Tboil	352.75 ± 1.00	K	NIST
Tboil	352.80 ± 0.40	K	NIST
Tboil	351.40 ± 1.00	K	NIST
Tboil	Outlier 350.65 ± 2.00	K	NIST
Tboil	352.65 ± 1.00	K	NIST
Tboil	351.55 ± 1.00	K	NIST
Tboil	353.15 ± 1.00	K	NIST
Tboil	Outlier 354.15 ± 2.00	K	NIST
Tboil	353.90 ± 1.00	K	NIST
Tboil	Outlier 350.15 ± 5.00	K	NIST
Tboil	351.85 ± 1.00	K	NIST
Tboil	352.68 ± 0.20	K	NIST
Tboil	351.15 ± 2.00	K	NIST
Tboil	352.70 ± 0.30	K	NIST
Tboil	352.95 ± 1.00	K	NIST
Tboil	354.00 ± 2.00	K	NIST
Tboil	354.00 ± 2.00	K	NIST
Tboil	352.65 ± 2.00	K	NIST
Tboil	352.75 ± 0.25	K	NIST
Tboil	351.15 ± 1.00	K	NIST
Tboil	352.15 ± 0.50	K	NIST
Tboil	352.85 ± 0.50	K	NIST
Tboil	352.30 ± 1.00	K	NIST
Tboil	Outlier 350.90 ± 1.00	K	NIST
Tboil	352.75 ± 0.30	K	NIST
Tboil	353.65 ± 2.00	K	NIST
Tboil	352.40 ± 1.00	K	NIST
Tboil	351.40 ± 1.00	K	NIST
Tboil	351.75 ± 1.00	K	NIST
Tboil	352.80 ± 0.30	K	NIST
Tboil	352.75 ± 0.50	K	NIST
Tboil	Outlier 354.15 ± 1.00	K	NIST
Tboil	352.00 ± 2.00	K	NIST
Tboil	353.75 ± 1.00	K	NIST
Tboil	351.75 ± 1.00	K	NIST
Tboil	351.15 ± 4.00	K	NIST
Tboil	Outlier 354.15 ± 2.00	K	NIST
Tc	[533.00; 536.80]	K
Tc	536.78	K	KDB
Tc	536.80	K	NIST
Tc	535.77 ± 0.20	K	NIST
Tc	535.77 ± 0.20	K	NIST
Tc	535.77 ± 0.20	K	NIST
Tc	536.78 ± 0.20	K	NIST
Tc	535.77 ± 0.30	K	NIST
Tc	535.70 ± 0.39	K	NIST
Tc	533.70 ± 3.00	K	NIST
Tc	Outlier 533.00 ± 3.00	K	NIST
Tfus	[186.00; 186.85]	K
Tfus	186.48	K	KDB
Tfus	186.50	K	Aq. Solubility Prediction
Tfus	186.85	K	NIST
Tfus	186.42 ± 0.02	K	NIST
Tfus	186.46 ± 0.01	K	NIST
Tfus	186.25 ± 0.30	K	NIST
Tfus	186.00 ± 2.00	K	NIST
Tfus	186.55 ± 0.30	K	NIST
Tfus	186.80 ± 0.20	K	NIST
Ttriple	[186.10; 186.50]	K
Ttriple	186.50 ± 0.01	K	NIST
Ttriple	186.47 ± 0.04	K	NIST
Ttriple	186.40 ± 0.06	K	NIST
Ttriple	186.48 ± 0.03	K	NIST
Ttriple	186.10 ± 0.10	K	NIST
Ttriple	186.47 ± 0.04	K	NIST
Ttriple	186.40 ± 0.06	K	NIST
Ttriple	186.48 ± 0.03	K	NIST
Ttriple	186.10 ± 0.10	K	NIST
Vc	0.267	m3/kmol	KDB
Zc	0.2516810		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[113.43; 138.62]	J/mol×K	[347.15; 467.15]
Cp,gas	113.43 ± 0.23	J/mol×K	347.15	NIST
Cp,gas	115.65 ± 0.17	J/mol×K	358.79	NIST
Cp,gas	118.70 ± 0.18	J/mol×K	371.90	NIST
Cp,gas	119.03 ± 0.24	J/mol×K	372.15	NIST
Cp,gas	121.75 ± 0.18	J/mol×K	385.60	NIST
Cp,gas	124.39 ± 0.25	J/mol×K	397.15	NIST
Cp,gas	124.60 ± 0.19	J/mol×K	399.55	NIST
Cp,gas	126.98 ± 0.19	J/mol×K	410.70	NIST
Cp,gas	131.71 ± 0.26	J/mol×K	432.15	NIST
Cp,gas	138.62 ± 0.28	J/mol×K	467.15	NIST
Cp,liquid	[157.91; 162.20]	J/mol×K	[293.00; 303.15]
Cp,liquid	158.00	J/mol×K	293.00	NIST
Cp,liquid	160.70	J/mol×K	297.00	NIST
Cp,liquid	160.70	J/mol×K	297.00	NIST
Cp,liquid	158.40	J/mol×K	298.10	NIST
Cp,liquid	159.20	J/mol×K	298.15	NIST
Cp,liquid	157.91	J/mol×K	298.15	NIST
Cp,liquid	159.00	J/mol×K	298.15	NIST
Cp,liquid	158.70	J/mol×K	298.15	NIST
Cp,liquid	158.40	J/mol×K	298.15	NIST
Cp,liquid	158.91	J/mol×K	298.15	NIST
Cp,liquid	158.41	J/mol×K	298.15	NIST
Cp,liquid	158.40	J/mol×K	298.15	NIST
Cp,liquid	162.20	J/mol×K	303.15	NIST
η	[0.0002545; 0.0004306]	Pa×s	[288.15; 323.15]
η	0.0004306	Pa×s	288.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0004306	Pa×s	288.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003980	Pa×s	293.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0003956	Pa×s	293.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0004136	Pa×s	293.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003980	Pa×s	293.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0004136	Pa×s	293.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003962	Pa×s	298.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003962	Pa×s	298.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0002828	Pa×s	298.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0003856	Pa×s	298.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0003780	Pa×s	298.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0003856	Pa×s	298.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0003810	Pa×s	298.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0003780	Pa×s	298.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0003600	Pa×s	303.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0003793	Pa×s	303.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003653	Pa×s	303.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0003620	Pa×s	303.15	Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
η	0.0003600	Pa×s	303.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0003653	Pa×s	303.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0003793	Pa×s	303.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0002666	Pa×s	303.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0003680	Pa×s	303.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0003626	Pa×s	308.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003520	Pa×s	308.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0003440	Pa×s	308.15	Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η	0.0003440	Pa×s	308.15	Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η	0.0003626	Pa×s	308.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0002601	Pa×s	308.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0003450	Pa×s	308.15	Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
η	0.0003461	Pa×s	313.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003300	Pa×s	313.15	Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
η	0.0003461	Pa×s	313.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0002545	Pa×s	313.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0003390	Pa×s	313.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0003303	Pa×s	318.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003303	Pa×s	318.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003160	Pa×s	318.15	Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
η	0.0003168	Pa×s	323.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003167	Pa×s	323.15	Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
η	0.0003030	Pa×s	323.15	Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
ΔfusH	[8.38; 8.48]	kJ/mol	[186.10; 186.50]
ΔfusH	8.48	kJ/mol	186.10	NIST
ΔfusH	8.48	kJ/mol	186.10	NIST
ΔfusH	8.38	kJ/mol	186.47	NIST
ΔfusH	8.38	kJ/mol	186.47	NIST
ΔfusH	8.44	kJ/mol	186.48	NIST
ΔfusH	8.44	kJ/mol	186.48	NIST
ΔfusH	8.44	kJ/mol	186.50	NIST
ΔfusH	8.44	kJ/mol	186.50	NIST
ΔvapH	[30.00; 35.60]	kJ/mol	[310.00; 505.00]
ΔvapH	35.60	kJ/mol	310.00	NIST
ΔvapH	33.80 ± 0.10	kJ/mol	314.00	NIST
ΔvapH	33.80	kJ/mol	315.00	NIST
ΔvapH	34.60	kJ/mol	318.00	NIST
ΔvapH	32.30 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	33.90	kJ/mol	339.00	NIST
ΔvapH	33.90	kJ/mol	342.00	NIST
ΔvapH	31.30 ± 0.10	kJ/mol	352.00	NIST
ΔvapH	31.21	kJ/mol	352.60	KDB
ΔvapH	31.30	kJ/mol	352.80	NIST
ΔvapH	30.50 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	30.00 ± 0.10	kJ/mol	370.00	NIST
ΔvapH	32.50	kJ/mol	378.00	NIST
ΔvapH	31.60	kJ/mol	438.00	NIST
ΔvapH	31.10	kJ/mol	505.00	NIST
Pvap	[15.74; 101.30]	kPa	[303.15; 352.72]
Pvap	15.74	kPa	303.15	Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System
Pvap	20.00	kPa	309.65	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap	30.00	kPa	319.95	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap	94.00	kPa	350.25	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	101.30	kPa	352.68	Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap	101.30	kPa	352.72	Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa
Pvap	101.30	kPa	352.72	Isobaric Vapor-Liquid Equilibrium for 2-Butanone + Ethanol System Containing Different Ionic Liquids at 101.3 kPa
n0	[1.36294; 1.38153]		[288.15; 323.15]
n0	1.38153		288.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.37879		293.15	Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n0	1.37880		293.15	Isothermal Vapor Liquid Equilibrium Data for the Butan-2-one + Methanol or Ethanol Systems Using a Static-Analytic Microcell
n0	1.37870		293.15	Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
n0	1.37879		293.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.37900		293.15	Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
n0	1.37910		293.15	Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
n0	1.37930		293.15	Distribution of Butyric Acid between Water and Several Solvents
n0	1.37892		293.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.37880		293.15	Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0	1.37690		298.15	(Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
n0	1.37618		298.15	Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n0	1.37618		298.15	Ternary Liquid-Liquid Equilibria Ethanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, 2-Propanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, and 2-Butanone + 2-Propanol + 1,3-Dimethylimidazolium Methyl Sulfate at 298.15 K
n0	1.37700		298.15	Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
n0	1.37631		298.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.37930		298.15	Isobaric Vapor Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa
n0	1.37623		298.15	Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
n0	1.37614		298.15	Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
n0	1.37623		298.15	Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
n0	1.37610		298.15	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol and 2-Propanol with 2-Butanone and Butyl Propionate at 101.3 kPa
n0	1.37500		298.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0	1.37618		298.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.37604		298.15	Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0	1.37690		298.15	Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
n0	1.37600		298.20	Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
n0	1.37355		303.15	Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n0	1.37366		303.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.37383		303.15	Density, viscosity, refractive index, excess molar enthalpy, viscosity, and refractive index deviations for the (1-butanol + 2-butanone) binary system at T = 303 K. A new adiabatic calorimeter for heat of mixing
n0	1.37355		303.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n0	1.37102		308.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.37000		308.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0	1.37140		308.20	Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
n0	1.36834		313.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.36565		318.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0	1.36570		318.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0	1.36620		318.20	Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
n0	1.36294		323.15	Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
ρl	[772.97; 810.33]	kg/m3	[288.15; 323.15]
ρl	810.26	kg/m3	288.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	810.33	kg/m3	288.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	805.00	kg/m3	293.00	KDB
ρl	808.64	kg/m3	293.15	Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl	805.06	kg/m3	293.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	805.06	kg/m3	293.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	799.80	kg/m3	293.15	(Vapour + liquid) equilibria for (2-ethoxypropene + acetone) and (2-ethoxypropene + butanone)
ρl	804.97	kg/m3	293.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	804.90	kg/m3	293.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	805.17	kg/m3	293.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	804.83	kg/m3	293.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	799.68	kg/m3	298.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	799.74	kg/m3	298.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	799.94	kg/m3	298.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	799.75	kg/m3	298.15	Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
ρl	800.30	kg/m3	298.15	Liquid-liquid equilibria for the pseudo-ternary system {aqueous sulfuric acid solution + methyl ethyl ketone or methyl isopropyl ketone + phosphonium-based ionic liquids} at 298.15 K and atmospheric pressure
ρl	799.97	kg/m3	298.15	Thermodynamics of (ketone + amine) mixtures. Part XI. Excess molar enthalpies at T = 298.15 K for the (1-propanol + N,N,N-triethylamine + 2-butanone) system
ρl	799.60	kg/m3	298.15	Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
ρl	802.03	kg/m3	298.15	Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
ρl	799.78	kg/m3	298.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	800.87	kg/m3	298.15	Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
ρl	799.75	kg/m3	298.15	Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
ρl	799.70	kg/m3	298.15	Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
ρl	799.83	kg/m3	298.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	799.62	kg/m3	298.15	Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
ρl	799.97	kg/m3	298.15	Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
ρl	799.97	kg/m3	298.15	Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
ρl	799.97	kg/m3	298.15	Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
ρl	803.24	kg/m3	298.15	Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl	799.60	kg/m3	298.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	794.67	kg/m3	303.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	794.47	kg/m3	303.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	794.41	kg/m3	303.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	794.60	kg/m3	303.15	Viscometric Behavior of Binary Mixtures of Butan-2-one with Benzene at T = (303.15, 313.15, and 323.15) K
ρl	799.71	kg/m3	303.15	Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
ρl	794.50	kg/m3	303.15	Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
ρl	797.88	kg/m3	303.15	Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl	794.60	kg/m3	303.15	Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
ρl	794.55	kg/m3	303.15	Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl	794.57	kg/m3	303.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	802.50	kg/m3	303.15	Effect of temperature on ultrasonic velocity and thermodynamic parameters of bisphenol-C-formaldehyde-acrylate resin solutions
ρl	799.69	kg/m3	303.15	Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
ρl	794.63	kg/m3	303.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	794.33	kg/m3	303.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	789.12	kg/m3	308.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	789.38	kg/m3	308.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	789.18	kg/m3	308.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	789.27	kg/m3	308.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	800.10	kg/m3	308.15	Effect of temperature on ultrasonic velocity and thermodynamic parameters of bisphenol-C-formaldehyde-acrylate resin solutions
ρl	792.45	kg/m3	308.15	Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl	789.04	kg/m3	308.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	783.85	kg/m3	313.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	783.80	kg/m3	313.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	784.00	kg/m3	313.15	Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
ρl	784.01	kg/m3	313.15	Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
ρl	786.94	kg/m3	313.15	Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
ρl	800.30	kg/m3	313.15	Effect of temperature on ultrasonic velocity and thermodynamic parameters of bisphenol-C-formaldehyde-acrylate resin solutions
ρl	784.00	kg/m3	313.15	Viscometric Behavior of Binary Mixtures of Butan-2-one with Benzene at T = (303.15, 313.15, and 323.15) K
ρl	783.95	kg/m3	313.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	783.72	kg/m3	313.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	778.44	kg/m3	318.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	778.48	kg/m3	318.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	778.36	kg/m3	318.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	773.04	kg/m3	323.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	773.09	kg/m3	323.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ρl	773.30	kg/m3	323.15	Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
ρl	773.30	kg/m3	323.15	Viscometric Behavior of Binary Mixtures of Butan-2-one with Benzene at T = (303.15, 313.15, and 323.15) K
ρl	772.97	kg/m3	323.15	Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
ΔfusS	[44.98; 45.59]	J/mol×K	[186.10; 186.48]
ΔfusS	45.59	J/mol×K	186.10	NIST
ΔfusS	45.59	J/mol×K	186.10	NIST
ΔfusS	44.98	J/mol×K	186.47	NIST
ΔfusS	44.98	J/mol×K	186.47	NIST
ΔfusS	45.25	J/mol×K	186.48	NIST
ΔfusS	45.25	J/mol×K	186.48	NIST
csound,fluid	[1136.00; 1212.30]	m/s	[293.15; 313.15]
csound,fluid	1212.30	m/s	293.15	Thermodynamics of ketone + amine mixtures Part IV. Volumetric and speed of sound data at (293.15; 298.15 and 303.15 K) for 2-butanone +dipropylamine, +dibutylamine or +triethylamine systems
csound,fluid	1212.00	m/s	293.15	Thermodynamics of Ketone + Amine Mixtures. Part III. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Butanone + Aniline, + N-Methylaniline, or + Pyridine Systems
csound,fluid	1192.00	m/s	298.15	Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
csound,fluid	1191.00	m/s	298.15	Thermodynamics of ketone + amine mixtures Part IV. Volumetric and speed of sound data at (293.15; 298.15 and 303.15 K) for 2-butanone +dipropylamine, +dibutylamine or +triethylamine systems
csound,fluid	1190.80	m/s	298.15	Thermodynamics of Ketone + Amine Mixtures. Part III. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Butanone + Aniline, + N-Methylaniline, or + Pyridine Systems
csound,fluid	1170.80	m/s	303.15	Thermodynamics of ketone + amine mixtures Part IV. Volumetric and speed of sound data at (293.15; 298.15 and 303.15 K) for 2-butanone +dipropylamine, +dibutylamine or +triethylamine systems
csound,fluid	1170.60	m/s	303.15	Thermodynamics of Ketone + Amine Mixtures. Part III. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Butanone + Aniline, + N-Methylaniline, or + Pyridine Systems
csound,fluid	1178.00	m/s	303.15	Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
csound,fluid	1158.00	m/s	308.15	Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
csound,fluid	1136.00	m/s	313.15	Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
γ	[0.02; 0.02]	N/m	[298.15; 298.20]
γ	0.02	N/m	298.15	Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
γ	0.02	N/m	298.20	KDB
λ	[0.13; 0.15]	W/m×K	[284.48; 374.56]
λ	0.15	W/m×K	284.48	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.15	W/m×K	294.42	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.15	W/m×K	305.02	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.14	W/m×K	314.26	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.14	W/m×K	323.96	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.14	W/m×K	334.71	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.14	W/m×K	344.54	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.13	W/m×K	354.33	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.13	W/m×K	364.46	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
λ	0.13	W/m×K	374.56	Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
308.15	101.30	0.0003
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.68]	kPa	[259.76; 376.05]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45436e+01
Coefficient B			-3.04648e+03
Coefficient C			-4.60570e+01
Temperature range, min.			259.76
Temperature range, max.			376.05
Pvap	1.33	kPa	259.76	Calculated Property
Pvap	3.01	kPa	272.68	Calculated Property
Pvap	6.21	kPa	285.60	Calculated Property
Pvap	11.90	kPa	298.52	Calculated Property
Pvap	21.42	kPa	311.44	Calculated Property
Pvap	36.49	kPa	324.37	Calculated Property
Pvap	59.31	kPa	337.29	Calculated Property
Pvap	92.50	kPa	350.21	Calculated Property
Pvap	139.13	kPa	363.13	Calculated Property
Pvap	202.68	kPa	376.05	Calculated Property
Pvap	[1.45e-03; 4143.73]	kPa	[186.48; 535.50]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.69787e+01
Coefficient B			-6.16017e+03
Coefficient C			-7.78365e+00
Coefficient D			6.13927e-06
Temperature range, min.			186.48
Temperature range, max.			535.50
Pvap	1.45e-03	kPa	186.48	Calculated Property
Pvap	0.11	kPa	225.26	Calculated Property
Pvap	1.96	kPa	264.04	Calculated Property
Pvap	15.33	kPa	302.82	Calculated Property
Pvap	70.44	kPa	341.60	Calculated Property
Pvap	227.74	kPa	380.38	Calculated Property
Pvap	578.94	kPa	419.16	Calculated Property
Pvap	1243.69	kPa	457.94	Calculated Property
Pvap	2369.94	kPa	496.72	Calculated Property
Pvap	4143.73	kPa	535.50	Calculated Property

Similar Compounds

Find more compounds similar to 2-Butanone.

Mixtures

• 2-Butanone + Ethanol
• 2-Butanone + Pentane, 2,2,4-trimethyl-
• 2-Butanone + Ethanol + Pentane, 2,2,4-trimethyl-
• Dimethyl phthalate + 2-Butanone
• 2-Butanone + Hexanedioic acid, dimethyl ester
• 2-Butanone + Dodecanedioic acid
• 2-Butanone + 1,2-Ethanediol + TETRAMETHYLAMMONIUM CHLORIDE
• 2-Butanone + Methylphosphonic acid
• 2-Butanone + Acetic acid
• 2-Butanone + Isopropyl acetate
• 2-Butanone + Acetic acid + Water
• 2-Butanone + Benzoic acid, 2-methyl-3-nitro-
• 2-Butanone + Ethyl Acetate
• 2-Butanone + sodium chloride + Water
• 2-Butanone + Water
• 2-Butanone + Benzenamine, 4-methyl-2-nitro-
• 2-Butanone + Triethylamine
• Diethyl carbonate + 2-Butanone + Water
• 2-Butanone + 2-ISOPROPYLIMIDAZOLE
• 2-Butanone + Methyl Alcohol

Find more mixtures with 2-Butanone.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• A relative headspace method for Henry s constants of volatile organic compounds
• Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
• Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
• Experimental isobaric vapour liquid liquid equilibrium data for the quaternary systems water (1) ethanol (2) acetone (3) n-butyl acetate (4) and water (1) ethanol (2) acetone (3) methyl ethyl ketone (4) and their partially miscible-constituent ternaries
• (Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
• Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
• Effect of temperature on ultrasonic velocity and thermodynamic parameters of bisphenol-C-formaldehyde-acrylate resin solutions
• Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
• Investigation on isobaric vapor liquid equilibrium for acetic acid +water +methyl ethyl ketone + isopropyl acetate
• Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
• Solubility of lansoprazole in different solvents
• Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
• Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
• Liquid-liquid equilibria for the pseudo-ternary system {aqueous sulfuric acid solution + methyl ethyl ketone or methyl isopropyl ketone + phosphonium-based ionic liquids} at 298.15 K and atmospheric pressure
• Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
• Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Solubility of methylphosphonic acid in selected organic solvents
• Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Densities, viscosities and refractive indices of binary mixtures containing methyl ethyl ketone. Friction theory. New UNIFAC-VISCO and ASOG-VISCO parameter determination
• Isobaric vapor-liquid equilibrium for methanol + methyl ethyl ketone + bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
• The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
• Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
• Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
• Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
• (Vapour + liquid) equilibria for (2-ethoxypropene + acetone) and (2-ethoxypropene + butanone)
• Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
• Density, viscosity, refractive index, excess molar enthalpy, viscosity, and refractive index deviations for the (1-butanol + 2-butanone) binary system at T = 303 K. A new adiabatic calorimeter for heat of mixing
• Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
• Measurement and correlation of (liquid + liquid) equilibrium of the azeotrope (cyclohexane + 2-butanone) with different ionic liquids at T = 298.15 K
• Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
• Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Combined effects of salinity and temperature on the solubility of organic compounds
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
• 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 of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Measurement and correlation of solubility of dodecanedioic acid in different pure solvents from T = (288.15 to 323.15) K
• Thermodynamics of (ketone + amine) mixtures. Part XI. Excess molar enthalpies at T = 298.15 K for the (1-propanol + N,N,N-triethylamine + 2-butanone) system
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Isobaric (vapor + liquid) equilibria for the binary systems (1-methoxy-2- propanol + 2-methoxyethanol), (2-butanone + 2-methoxyethanol) and (water + 2-methoxyethanol) at pressures of (74.5, 101.3, and 134.0) kPa
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
• Phase equilibria of the ternary systems of (water + diethyl carbonate) with acetone, or 2-butanone at four temperatures
• Thermodynamic study of the solubility of 2,4'-dihydroxydiphenyl sulfone in nine organic solvents from T = (278.15 to 313.15) K and thermodynamic properties of dissolution
• Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
• Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
• Solubility measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
• Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
• Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
• Solubility determination and thermodynamic functions of 2-chlorophenothiazine in nine organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
• Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
• Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
• Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
• Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
• Thermodynamics of ketone + amine mixtures Part IV. Volumetric and speed of sound data at (293.15; 298.15 and 303.15 K) for 2-butanone +dipropylamine, +dibutylamine or +triethylamine systems
• Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
• Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
• Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
• Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
• 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
• Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
• Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
• Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Isobaric Vapor Liquid Liquid Phase Equilibria Measurements of Three Ternary Water + 2-Butanone + Aliphatic Alcohol (Ethanol, 1-Propanol, 2-Propanol) Systems at 101.3 kPa
• Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
• Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
• Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
• Isobaric Vapor-Liquid Equilibrium for 2-Butanone + Ethanol System Containing Different Ionic Liquids at 101.3 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
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
• Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
• Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
• 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
• Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
• Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
• Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
• Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
• Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
• Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
• Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
• Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
• Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Measurement of Henry s Law Constants for Acetone, 2-Butanone, 2,3-Butanedione, and Isobutyraldehyde Using a Horizontal Flow Reactor
• Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
• Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
• Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
• Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K
• Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Distribution of Butyric Acid between Water and Several Solvents
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System
• Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
• Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 2-Butanone + 2-Butanol + Water System
• Thermodynamics of Ketone + Amine Mixtures. Part III. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Butanone + Aniline, + N-Methylaniline, or + Pyridine Systems
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Different Organic Solvents
• Solubility of Candesartan Cilexetil in Different Solvents at Various Temperatures
• Viscometric Behavior of Binary Mixtures of Butan-2-one with Benzene at T = (303.15, 313.15, and 323.15) K
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Effect of Ionic Liquids on the Isobaric Vapor-Liquid equilibrium behavior of methanol-methyl ethyl ketone (MEK)
• Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
• Isothermal Vapor Liquid Equilibrium Data for the Butan-2-one + Methanol or Ethanol Systems Using a Static-Analytic Microcell
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
• Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
• Ternary Liquid-Liquid Equilibria Ethanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, 2-Propanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, and 2-Butanone + 2-Propanol + 1,3-Dimethylimidazolium Methyl Sulfate at 298.15 K
• Solubility of Imidacloprid in Different Solvents
• Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
• Isobaric Vapor Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa
• 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
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Volumetric and Transport Properties of Binary Liquid Mixtures of Aliphatic Ketones with Phenylacetonitrile at T = 308.15 K
• Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
• Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
• Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol and 2-Propanol with 2-Butanone and Butyl Propionate at 101.3 kPa
• Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
• Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
• Solubility of 1,1'-(Ethane-1,2-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents
• Solubilities of 1,1?-(Propane-1,3-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Different Solvents
• Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Water, Acetophenone, Cyclohexanone, Acetylacetone, and 2-Butanone
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
• Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents from (288.15 to 333.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
These property values are available through the Cheméo API. A free account gives you an access key.