Chemical Properties of Methyl Isobutyl Ketone (CAS 108-10-1)

InChI

InChI=1S/C6H12O/c1-5(2)4-6(3)7/h5H,4H2,1-3H3

InChI Key

NTIZESTWPVYFNL-UHFFFAOYSA-N

Formula

C6H12O

SMILES

CC(=O)CC(C)C

Molecular Weight¹

100.16

CAS

108-10-1

Other Names

• 2-Methyl-4-pentanal
• 2-Methyl-4-pentanone
• 2-Methylpropyl methyl ketone
• 2-Pentanone, 4-methyl-
• 4-Methyl-2-oxopentane
• 4-Methyl-2-pentanon
• 4-Methyl-pentan-2-on
• 4-Metilpentan-2-one
• 4-methyl-2-pentanone
• 4-methyl-2-pentanone (MIBK; methyl isobutyl ketone)
• 4-methylpentan-2-one
• Hexon
• Hexone
• Isobutyl-methylketon
• Isopropylacetone
• Ketone, isobutyl methyl
• METHYL-ISO-BUTYL KETONE
• MIBK
• MIK
• Methyl i-butyl ketone
• Methyl-2-pentanon,4-
• Methyl-isobutyl-cetone
• Methylisobutylketon
• Metilisobutilchetone
• Metyloizobutyloketon
• NSC 5712
• Rcra waste number U161
• Shell MIBK
• UN 1245
• ethyl iso-butyl ketone
• iso-C4H9COCH3
• isobutyl methyl ketone
• isopropyl acetone

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3520; 0.4000]
ω	0.4000		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3520		ChemSep v8.3 pure component data Compiled value
ω	0.3850		KDB
Tig	[721.15; 729.82]	K
Tig	729.82	K	KDB
Tig	721.15	K	NCMS SOLV-DB
ΔcH°solid	-3694.60	kJ/mol	NIST
μ	[2.70; 2.80]	debye
μ	2.70	debye	ChemSep v8.3 pure component data Compiled value
μ	2.80	debye	KDB
η	[0.0005500; 0.0005600]	Pa×s
η	0.0005500	Pa×s	Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K
η	0.0005600	Pa×s	Viscosity of the Tributyl Phosphate + Methyl Isobutyl Ketone + Phosphoric Acid System
εr	13.11		NCMS SOLV-DB
LFL	1.40	% in Air	KDB
UFL	7.50	% in Air	KDB
Tflash,cc	[289.15; 297.04]	K
Tflash,cc	297.04	K	KDB
Tflash,cc	289.15	K	NCMS SOLV-DB
Tflash,oc	295.93	K	KDB
ΔfG°	-135.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
Rg	3.7400		KDB
ΔfH°gas	[-291.20; -284.00]	kJ/mol
ΔfH°gas	-288.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-284.00	kJ/mol	KDB
ΔfH°gas	-291.20 ± 1.40	kJ/mol	NIST
ΔfH°solid	-381.50	kJ/mol	NIST
ΔfusH°	9.37	kJ/mol	Joback Calculated Property
ΔvapH°	[40.56; 42.50]	kJ/mol
ΔvapH°	41.00	kJ/mol	NCMS SOLV-DB
ΔvapH°	40.65	kJ/mol	NIST
ΔvapH°	40.56	kJ/mol	NIST
ΔvapH°	42.50 ± 0.10	kJ/mol	NIST
ΔvapH°	41.00	kJ/mol	NIST
IE	[9.30; 9.42]	eV
IE	9.30 ± 0.01	eV	NIST
IE	9.30 ± 0.01	eV	NIST
IE	Outlier 9.42	eV	NIST
IE	9.34 ± 0.01	eV	NIST
IE	9.30 ± 0.02	eV	NIST
IE	9.30 ± 0.03	eV	NIST
log10WS	[-0.96; -0.74]
log10WS	-0.96		Aq. Solubility Prediction
log10WS	-0.74		Estimated Solubility
logPoct/wat	1.160		NCMS SOLV-DB
McVol	96.970	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=3); %!d(float64=3)]
NFPA Fire	3		KDB
NFPA Fire	3		NCMS SOLV-DB
NFPA Health	[%!d(float64=2); %!d(float64=2)]
NFPA Health	2		KDB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[3270.00; 3390.00]	kPa
Pc	3270.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3272.80	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3270.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3270.00	kPa	KDB
Pc	Outlier 3390.00 ± 20.00	kPa	NIST
Pc	3270.00 ± 5.00	kPa	NIST
Pc	3280.00 ± 96.50	kPa	NIST
Ptriple	6.99e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[698.00; 759.00]
Inp	721.20		NIST
Inp	722.94		NIST
Inp	719.78		NIST
Inp	720.12		NIST
Inp	720.65		NIST
Inp	721.70		NIST
Inp	723.00		NIST
Inp	720.00		NIST
Inp	721.00		NIST
Inp	722.00		NIST
Inp	730.00		NIST
Inp	726.00		NIST
Inp	724.00		NIST
Inp	727.00		NIST
Inp	727.00		NIST
Inp	Outlier 703.00		NIST
Inp	705.00		NIST
Inp	706.00		NIST
Inp	724.00		NIST
Inp	728.00		NIST
Inp	736.00		NIST
Inp	734.70		NIST
Inp	729.60		NIST
Inp	730.00		NIST
Inp	729.50		NIST
Inp	716.00		NIST
Inp	733.30		NIST
Inp	723.00		NIST
Inp	738.00		NIST
Inp	719.00		NIST
Inp	742.00		NIST
Inp	720.00		NIST
Inp	709.00		NIST
Inp	714.00		NIST
Inp	728.00		NIST
Inp	Outlier 753.00		NIST
Inp	721.00		NIST
Inp	739.00		NIST
Inp	739.00		NIST
Inp	723.00		NIST
Inp	741.00		NIST
Inp	732.00		NIST
Inp	735.00		NIST
Inp	725.00		NIST
Inp	730.00		NIST
Inp	Outlier 749.00		NIST
Inp	Outlier 759.00		NIST
Inp	732.00		NIST
Inp	728.00		NIST
Inp	740.00		NIST
Inp	Outlier 698.00		NIST
Inp	721.00		NIST
Inp	730.00		NIST
Inp	730.00		NIST
Inp	722.00		NIST
Inp	713.00		NIST
Inp	733.00		NIST
Inp	720.00		NIST
Inp	725.00		NIST
Inp	720.00		NIST
Inp	715.83		NIST
Inp	726.00		NIST
Inp	721.00		NIST
Inp	723.00		NIST
Inp	726.00		NIST
Inp	720.00		NIST
Inp	720.00		NIST
Inp	723.00		NIST
Inp	724.00		NIST
Inp	740.00		NIST
Inp	720.00		NIST
Inp	720.00		NIST
Inp	742.00		NIST
Inp	724.00		NIST
Inp	721.20		NIST
Inp	721.70		NIST
Inp	730.00		NIST
Inp	Outlier 703.00		NIST
Inp	728.00		NIST
Inp	723.00		NIST
Ip	[994.00; 1059.00]
Ip	1039.50		NIST
Ip	1025.20		NIST
Ip	1029.00		NIST
Ip	1033.90		NIST
Ip	1034.00		NIST
Ip	1007.00		NIST
Ip	1015.00		NIST
Ip	994.00		NIST
Ip	Outlier 1059.00		NIST
Ip	1010.00		NIST
Ip	Outlier 1059.00		NIST
Ip	1021.20		NIST
Ip	1012.00		NIST
Ip	1009.00		NIST
Ip	1010.00		NIST
Ip	1010.00		NIST
Ip	1010.00		NIST
Ip	1008.00		NIST
Ip	999.00		NIST
Ip	1010.00		NIST
Ip	1028.00		NIST
Ip	1013.00		NIST
Ip	1006.00		NIST
Ip	1008.00		NIST
Ip	1013.00		NIST
Ip	1000.00		NIST
Ip	1020.00		NIST
Ip	1000.00		NIST
Ip	1000.00		NIST
Ip	1007.00		NIST
Ip	1000.00		NIST
Ip	1007.00		NIST
Ip	1008.00		NIST
Ip	1008.00		NIST
Ip	1017.00		NIST
Ip	1008.00		NIST
Ip	999.00		NIST
Ip	1017.00		NIST
Ip	1025.00		NIST
Ip	1002.00		NIST
Ip	1000.00		NIST
Ip	1012.00		NIST
Ip	1019.00		NIST
Ip	1008.00		NIST
Ip	1017.00		NIST
Ip	1019.00		NIST
Ip	1007.00		NIST
Ip	Outlier 1059.00		NIST
Ip	1009.00		NIST
Tboil	[386.65; 392.30]	K
Tboil	Outlier 392.30	K	Liquid-liquid equilibria of water + lactic acid + methyl isobutyl ketone
Tboil	390.50	K	Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
Tboil	390.54	K	Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
Tboil	389.15	K	Vapor-Liquid Equilibrium for Binary of 1-Butanol + N,N-Dimethylacetamide and Methyl Isobutyl Ketone + N,N-Dimethylacetamide at 101.3 kPa
Tboil	389.45	K	Measurements of Quaternary Liquid-Liquid Equilibrium for Water + Acetic Acid + Propionic Acid + Solvent (Butyronitrile, Benzyl Acetate, or Methyl Isobutyl Ketone) at 298.15 K
Tboil	387.35	K	Conductivity and Dissociation Constants of Quaternary Ammonium Perchlorates and Picrates in 4-Methyl-pentan-2-one
Tboil	389.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	389.60	K	KDB
Tboil	390.55	K	NCMS SOLV-DB
Tboil	390.00	K	NIST
Tboil	389.40 ± 0.30	K	NIST
Tboil	390.35 ± 0.50	K	NIST
Tboil	389.40	K	NIST
Tboil	389.20 ± 0.40	K	NIST
Tboil	389.00 ± 0.40	K	NIST
Tboil	389.45 ± 0.30	K	NIST
Tboil	389.10 ± 0.30	K	NIST
Tboil	388.43 ± 0.20	K	NIST
Tboil	389.00 ± 1.50	K	NIST
Tboil	389.35	K	NIST
Tboil	390.40 ± 0.50	K	NIST
Tboil	388.65 ± 2.00	K	NIST
Tboil	387.85 ± 2.00	K	NIST
Tboil	389.10 ± 3.00	K	NIST
Tboil	Outlier 392.00 ± 3.00	K	NIST
Tboil	387.65 ± 2.00	K	NIST
Tboil	388.15 ± 1.00	K	NIST
Tboil	389.05 ± 1.00	K	NIST
Tboil	388.15 ± 1.00	K	NIST
Tboil	388.25 ± 1.00	K	NIST
Tboil	389.70 ± 0.11	K	NIST
Tboil	388.95 ± 0.50	K	NIST
Tboil	389.35 ± 0.50	K	NIST
Tboil	389.06 ± 0.50	K	NIST
Tboil	387.15 ± 2.00	K	NIST
Tboil	390.90 ± 1.00	K	NIST
Tboil	391.15 ± 1.00	K	NIST
Tboil	389.20 ± 1.00	K	NIST
Tboil	390.65 ± 2.00	K	NIST
Tboil	389.20 ± 0.40	K	NIST
Tboil	389.20 ± 0.20	K	NIST
Tboil	388.15 ± 2.00	K	NIST
Tboil	388.95 ± 1.00	K	NIST
Tboil	390.15 ± 2.00	K	NIST
Tboil	389.05 ± 0.50	K	NIST
Tboil	388.80 ± 1.00	K	NIST
Tboil	389.15 ± 1.50	K	NIST
Tboil	389.89 ± 0.10	K	NIST
Tboil	390.65 ± 0.50	K	NIST
Tboil	388.15 ± 0.50	K	NIST
Tboil	388.60 ± 1.00	K	NIST
Tboil	Outlier 386.85 ± 0.50	K	NIST
Tboil	389.40 ± 0.50	K	NIST
Tboil	388.65 ± 1.00	K	NIST
Tboil	390.15 ± 2.00	K	NIST
Tboil	389.65 ± 0.50	K	NIST
Tboil	387.15 ± 2.00	K	NIST
Tboil	389.40 ± 0.50	K	NIST
Tboil	388.15 ± 1.00	K	NIST
Tboil	389.40 ± 0.20	K	NIST
Tboil	387.65 ± 1.00	K	NIST
Tboil	390.00 ± 0.20	K	NIST
Tboil	388.65 ± 1.00	K	NIST
Tboil	Outlier 386.65 ± 3.00	K	NIST
Tboil	388.65 ± 1.00	K	NIST
Tboil	390.15 ± 2.00	K	NIST
Tboil	388.00 ± 5.00	K	NIST
Tboil	388.15 ± 1.00	K	NIST
Tc	[571.00; 575.50]	K
Tc	574.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	571.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	574.60	K	ChemSep v8.3 pure component data Compiled value
Tc	571.00	K	KDB
Tc	575.50 ± 0.50	K	NIST
Tc	574.60 ± 0.50	K	NIST
Tc	571.00	K	NIST
Tc	571.00 ± 1.11	K	NIST
Tfus	[189.00; 189.15]	K
Tfus	189.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	189.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	189.00	K	KDB
Tfus	189.15	K	NCMS SOLV-DB
Tfus	189.15	K	NIST
Ttriple	189.15	K	ChemSep v8.3 pure component data Compiled value
UQi	3.95		ChemSep v8.3 pure component data Compiled value
URi	4.60		ChemSep v8.3 pure component data Compiled value
Vc	[0.341; 0.371]	m3/kmol
Vc	0.371	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.341	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2560000		ChemSep v8.3 pure component data Compiled value
Zra	[0.26; 0.26]
Zra	0.26		ChemSep v8.3 pure component data Compiled value
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[180.50; 187.90]	J/mol×K	[394.30; 415.75]
Cp,gas	180.50 ± 0.27	J/mol×K	394.30	NIST
Cp,gas	182.26 ± 0.27	J/mol×K	399.44	NIST
Cp,gas	184.31 ± 0.28	J/mol×K	405.15	NIST
Cp,gas	186.06 ± 0.28	J/mol×K	410.70	NIST
Cp,gas	187.90 ± 0.28	J/mol×K	415.75	NIST
Cp,liquid	211.90	J/mol×K	298.15	NIST
η	0.0005463	Pa×s	298.15	NCMS SOLV-DB
ΔvapH	[34.49; 42.50]	kJ/mol	[308.00; 389.40]
ΔvapH	40.10 ± 0.10	kJ/mol	308.00	NIST
ΔvapH	39.00 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	38.00 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	42.50	kJ/mol	340.50	NIST
ΔvapH	41.20	kJ/mol	342.00	NIST
ΔvapH	37.60	kJ/mol	347.00	NIST
ΔvapH	37.40 ± 0.10	kJ/mol	348.00	NIST
ΔvapH	38.70	kJ/mol	359.00	NIST
ΔvapH	39.20	kJ/mol	362.50	NIST
ΔvapH	37.00	kJ/mol	369.00	NIST
ΔvapH	40.61	kJ/mol	388.90	NIST
ΔvapH	34.49	kJ/mol	389.40	NIST
Pvap	[2.65; 114.12]	kPa	[298.15; 393.15]
Pvap	2.65	kPa	298.15	NCMS SOLV-DB
Pvap	3.89	kPa	303.15	Density, viscosity, isothermal (vapour + liquid) equilibrium, excess molar volume, viscosity deviation, and their correlations for chloroform + methyl isobutyl ketone binary system
Pvap	5.88	kPa	313.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	9.42	kPa	323.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	13.85	kPa	331.98	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	14.56	kPa	333.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	19.35	kPa	340.18	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	19.78	kPa	340.66	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	20.72	kPa	341.81	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	21.82	kPa	343.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	21.92	kPa	343.42	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	30.01	kPa	351.55	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	30.29	kPa	351.81	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	31.12	kPa	352.71	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	31.71	kPa	353.11	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	31.80	kPa	353.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	39.35	kPa	359.22	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	39.63	kPa	359.39	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	40.05	kPa	359.58	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	43.51	kPa	362.04	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	44.70	kPa	362.88	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	45.19	kPa	363.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	49.68	kPa	365.90	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	50.66	kPa	366.61	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	53.01	kPa	368.06	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	53.42	kPa	368.07	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	53.26	kPa	368.14	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	53.24	kPa	368.15	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	54.29	kPa	368.70	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	59.43	kPa	371.34	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	59.75	kPa	371.64	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	60.19	kPa	371.91	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	60.56	kPa	372.03	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	62.78	kPa	373.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	65.18	kPa	374.37	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	69.16	kPa	376.26	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	69.98	kPa	376.49	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	74.83	kPa	378.80	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	79.56	kPa	380.65	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	80.16	kPa	381.06	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	82.62	kPa	382.04	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	84.16	kPa	382.66	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	85.44	kPa	383.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	90.58	kPa	384.99	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	98.70	kPa	388.07	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	99.40	kPa	388.31	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	100.35	kPa	388.63	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	100.41	kPa	388.65	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	101.85	kPa	389.06	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	101.30	kPa	389.15	Vapor-Liquid Equilibrium for Binary of 1-Butanol + N,N-Dimethylacetamide and Methyl Isobutyl Ketone + N,N-Dimethylacetamide at 101.3 kPa
Pvap	102.78	kPa	389.49	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	110.74	kPa	392.07	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
Pvap	114.12	kPa	393.15	Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
n0	[1.39327; 1.39586]		[293.15; 298.15]
n0	1.39586		293.15	Vapor Liquid Equilibrium for Methyl Isobutyl Ketone (MIBK) + (1-Propanol or 2-Propanol) Binary Mixtures
n0	1.39580		293.15	Distribution of Butyric Acid between Water and Several Solvents
n0	1.39355		298.15	Isobaric vapour liquid equilibria for the binary systems 4-methyl-2-pentanone + 1-butanol and + 2-butanol at 20 and 101.3 kPa
n0	1.39360		298.15	Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
n0	1.39350		298.15	Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
n0	1.39327		298.15	Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
n0	1.39420		298.15	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
n0	1.39360		298.15	Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 4-Methyl-2-pentanone + 2-Butanol + Water System
n0	1.39400		298.15	NCMS SOLV-DB
ρl	[773.00; 805.12]	kg/m3	[288.15; 323.15]
ρl	805.12	kg/m3	288.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	801.00	kg/m3	293.00	KDB
ρl	801.00	kg/m3	293.15	Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl	800.80	kg/m3	293.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	800.90	kg/m3	293.15	Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
ρl	800.00	kg/m3	293.15	Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl	799.61	kg/m3	293.20	Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl	796.10	kg/m3	298.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	795.98	kg/m3	298.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	799.80	kg/m3	298.15	Liquid liquid equilibria for the quaternary system methyl isobutyl ketone water phenol hydroquinone
ρl	799.00	kg/m3	298.15	Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + 1,2-Benzenediol + Water
ρl	798.09	kg/m3	298.15	Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
ρl	796.19	kg/m3	298.15	Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
ρl	795.94	kg/m3	298.15	Liquid liquid equilibria of 4-methyl-2-pentanone + 1-propanol or 2-propanol + water ternary systems: Measurements and correlation at different temperatures
ρl	796.50	kg/m3	298.15	Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, diisopropyl ether and 4-methyl-2-pentanone
ρl	800.59	kg/m3	298.15	Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
ρl	796.23	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	796.03	kg/m3	298.15	Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
ρl	799.80	kg/m3	298.20	Phase Equilibrium Measurement and Thermodynamic Modeling of the 4-Methylpentan-2-one/3-Methylphenol, and 4-Methylphenol/Water Ternary Systems at 298.2, 313.2, and 323.2 K and 0.1 MPa
ρl	791.60	kg/m3	303.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	796.33	kg/m3	303.15	Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
ρl	791.25	kg/m3	303.15	Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
ρl	792.00	kg/m3	303.15	Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl	786.90	kg/m3	308.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	786.75	kg/m3	308.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	782.30	kg/m3	313.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	782.00	kg/m3	313.15	Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl	781.11	kg/m3	313.20	Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl	777.46	kg/m3	318.15	Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
ρl	777.60	kg/m3	318.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl	773.00	kg/m3	323.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
csound,fluid	[1138.00; 1175.00]	m/s	[303.15; 313.15]
csound,fluid	1175.00	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	1156.00	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	1138.00	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	N/m	298.15	NCMS SOLV-DB

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
308.15	101.30	0.0005
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[112.10; 365.72]	J/mol×K	[189.15; 1500.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			9.75400e+01
Coefficient B			-6.34680e+02
Coefficient C			6.03124e+00
Coefficient D			1.84970e-05
Coefficient E			-1.96650e-08
Temperature range, min.			189.15
Temperature range, max.			1500.15
Cp,gas	112.10	J/mol×K	189.15	Calculated Property
Cp,gas	160.32	J/mol×K	334.82	Calculated Property
Cp,gas	209.11	J/mol×K	480.48	Calculated Property
Cp,gas	249.18	J/mol×K	626.15	Calculated Property
Cp,gas	280.91	J/mol×K	771.82	Calculated Property
Cp,gas	306.03	J/mol×K	917.48	Calculated Property
Cp,gas	326.08	J/mol×K	1063.15	Calculated Property
Cp,gas	342.19	J/mol×K	1208.82	Calculated Property
Cp,gas	355.20	J/mol×K	1354.48	Calculated Property
Cp,gas	365.72	J/mol×K	1500.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[180.97; 269.07]	J/mol×K	[189.15; 450.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			9.34330e+01
Coefficient B			-8.91970e+00
Coefficient C			3.97724e+00
Coefficient D			2.99160e-03
Coefficient E			-6.67690e-07
Temperature range, min.			189.15
Temperature range, max.			450.00
Cp,liquid	180.97	J/mol×K	189.15	Calculated Property
Cp,liquid	188.74	J/mol×K	218.13	Calculated Property
Cp,liquid	196.94	J/mol×K	247.12	Calculated Property
Cp,liquid	205.60	J/mol×K	276.10	Calculated Property
Cp,liquid	214.77	J/mol×K	305.08	Calculated Property
Cp,liquid	224.46	J/mol×K	334.07	Calculated Property
Cp,liquid	234.72	J/mol×K	363.05	Calculated Property
Cp,liquid	245.55	J/mol×K	392.03	Calculated Property
Cp,liquid	257.00	J/mol×K	421.02	Calculated Property
Cp,liquid	269.07	J/mol×K	450.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0052301; 0.0001403]	Pa×s	[189.15; 474.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-9.54410e+00
Coefficient B			1.13880e+03
Coefficient C			-3.41280e-01
Coefficient D			1.65810e-06
Coefficient E			2.00000e+00
Temperature range, min.			189.15
Temperature range, max.			474.00
η	0.0052301	Pa×s	189.15	Calculated Property
η	0.0021385	Pa×s	220.80	Calculated Property
η	0.0010971	Pa×s	252.45	Calculated Property
η	0.0006557	Pa×s	284.10	Calculated Property
η	0.0004367	Pa×s	315.75	Calculated Property
η	0.0003151	Pa×s	347.40	Calculated Property
η	0.0002417	Pa×s	379.05	Calculated Property
η	0.0001944	Pa×s	410.70	Calculated Property
η	0.0001626	Pa×s	442.35	Calculated Property
η	0.0001403	Pa×s	474.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[47.78; 0.00]	kJ/mol	[189.15; 574.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			2.79290e+01
Coefficient B			-4.56470e+00
Coefficient C			1.43720e+01
Coefficient D			-1.60970e+01
Coefficient E			6.53870e+00
Critical temperature, Tc (K)			5.74600e+02
Temperature range, min.			189.15
Temperature range, max.			574.60
ΔvapH	47.78	kJ/mol	189.15	Calculated Property
ΔvapH	45.78	kJ/mol	231.98	Calculated Property
ΔvapH	42.85	kJ/mol	274.81	Calculated Property
ΔvapH	39.61	kJ/mol	317.63	Calculated Property
ΔvapH	36.43	kJ/mol	360.46	Calculated Property
ΔvapH	33.34	kJ/mol	403.29	Calculated Property
ΔvapH	30.07	kJ/mol	446.12	Calculated Property
ΔvapH	25.98	kJ/mol	488.94	Calculated Property
ΔvapH	19.82	kJ/mol	531.77	Calculated Property
ΔvapH	0.00	kJ/mol	574.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[288.82; 413.37]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49712e+01
Coefficient B			-3.51652e+03
Coefficient C			-4.93340e+01
Temperature range, min.			288.82
Temperature range, max.			413.37
Pvap	1.33	kPa	288.82	Calculated Property
Pvap	2.97	kPa	302.66	Calculated Property
Pvap	6.10	kPa	316.50	Calculated Property
Pvap	11.67	kPa	330.34	Calculated Property
Pvap	21.00	kPa	344.18	Calculated Property
Pvap	35.84	kPa	358.01	Calculated Property
Pvap	58.43	kPa	371.85	Calculated Property
Pvap	91.52	kPa	385.69	Calculated Property
Pvap	138.33	kPa	399.53	Calculated Property
Pvap	202.63	kPa	413.37	Calculated Property
Pvap	[3.79e-05; 3270.00]	kPa	[189.15; 567.53]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.45089e+02
Coefficient B			-9.95863e+03
Coefficient C			-1.96891e+01
Coefficient D			1.67819e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 574.6 K.
Temperature range, min.			189.15
Temperature range, max.			567.53
Pvap	3.79e-05	kPa	189.15	Calculated Property
Pvap	0.01	kPa	231.19	Calculated Property
Pvap	0.57	kPa	273.24	Calculated Property
Pvap	6.62	kPa	315.28	Calculated Property
Pvap	37.20	kPa	357.32	Calculated Property
Pvap	133.49	kPa	399.36	Calculated Property
Pvap	361.98	kPa	441.41	Calculated Property
Pvap	824.52	kPa	483.45	Calculated Property
Pvap	1690.67	kPa	525.49	Calculated Property
Pvap	3270.00	kPa	567.53	Calculated Property
Pvap	[2.17; 100.82]	kPa	[295.15; 389.15]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.58031e+02
Coefficient B			-1.05457e+04
Coefficient C			-2.16516e+01
Coefficient D			1.85635e-05
Coefficient E			0.00000e+00
Temperature range, min.			295.15
Temperature range, max.			389.15
Pvap	2.17	kPa	295.15	Calculated Property
Pvap	3.89	kPa	305.59	Calculated Property
Pvap	6.64	kPa	316.04	Calculated Property
Pvap	10.82	kPa	326.48	Calculated Property
Pvap	16.93	kPa	336.93	Calculated Property
Pvap	25.58	kPa	347.37	Calculated Property
Pvap	37.46	kPa	357.82	Calculated Property
Pvap	53.36	kPa	368.26	Calculated Property
Pvap	74.15	kPa	378.71	Calculated Property
Pvap	100.82	kPa	389.15	Calculated Property
Pvap	[2.18; 101.47]	kPa	[294.90; 389.30]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37072e+01
Coefficient B			-2.88766e+03
Coefficient C			-7.15370e+01
Reference			Fuge, Bowden, et al., 1952
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			294.90
Temperature range, max.			389.30
Pvap	2.18	kPa	294.90	Calculated Property
Pvap	3.89	kPa	305.39	Calculated Property
Pvap	6.61	kPa	315.88	Calculated Property
Pvap	10.76	kPa	326.37	Calculated Property
Pvap	16.84	kPa	336.86	Calculated Property
Pvap	25.47	kPa	347.34	Calculated Property
Pvap	37.37	kPa	357.83	Calculated Property
Pvap	53.38	kPa	368.32	Calculated Property
Pvap	74.41	kPa	378.81	Calculated Property
Pvap	101.47	kPa	389.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[887.98; 269.12]	kg/m3	[189.15; 574.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.05499e+01
Coefficient B			2.62150e-01
Coefficient C			5.74600e+02
Coefficient D			2.87200e-01
Temperature range, min.			189.15
Temperature range, max.			574.60
ρl	887.98	kg/m3	189.15	Calculated Property
ρl	853.41	kg/m3	231.98	Calculated Property
ρl	817.15	kg/m3	274.81	Calculated Property
ρl	778.78	kg/m3	317.63	Calculated Property
ρl	737.68	kg/m3	360.46	Calculated Property
ρl	692.92	kg/m3	403.29	Calculated Property
ρl	642.86	kg/m3	446.12	Calculated Property
ρl	584.18	kg/m3	488.94	Calculated Property
ρl	507.91	kg/m3	531.77	Calculated Property
ρl	269.12	kg/m3	574.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 1.19e-05]	N/m	[189.15; 570.75]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-5.38250e-03
Coefficient B			2.38910e+02
Coefficient C			-5.43410e+00
Coefficient D			8.05830e-03
Coefficient E			-1.47540e-05
Comment			Range stopped where the equation turns negative; ChemSep gives it to 574.6 K.
Temperature range, min.			189.15
Temperature range, max.			570.75
γ	0.04	N/m	189.15	Calculated Property
γ	0.03	N/m	231.55	Calculated Property
γ	0.03	N/m	273.95	Calculated Property
γ	0.02	N/m	316.35	Calculated Property
γ	0.02	N/m	358.75	Calculated Property
γ	0.01	N/m	401.15	Calculated Property
γ	0.01	N/m	443.55	Calculated Property
γ	0.01	N/m	485.95	Calculated Property
γ	0.00	N/m	528.35	Calculated Property
γ	1.19e-05	N/m	570.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.12]	W/m×K	[189.15; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			-8.74190e+05
Coefficient B			2.04640e-02
Coefficient C			1.79110e+07
Coefficient D			-8.12740e+12
Temperature range, min.			189.15
Temperature range, max.			1000.00
λgas	0.00	W/m×K	189.15	Calculated Property
λgas	0.01	W/m×K	279.24	Calculated Property
λgas	0.02	W/m×K	369.34	Calculated Property
λgas	0.03	W/m×K	459.43	Calculated Property
λgas	0.04	W/m×K	549.53	Calculated Property
λgas	0.05	W/m×K	639.62	Calculated Property
λgas	0.07	W/m×K	729.72	Calculated Property
λgas	0.08	W/m×K	819.81	Calculated Property
λgas	0.10	W/m×K	909.91	Calculated Property
λgas	0.12	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.10]	W/m×K	[171.42; 451.42]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			5.08500e-02
Coefficient B			-9.63200e+01
Coefficient C			-9.50780e-01
Coefficient D			-3.16610e-03
Coefficient E			-2.05470e-06
Temperature range, min.			171.42
Temperature range, max.			451.42
λliquid	0.17	W/m×K	171.42	Calculated Property
λliquid	0.17	W/m×K	202.53	Calculated Property
λliquid	0.16	W/m×K	233.64	Calculated Property
λliquid	0.15	W/m×K	264.75	Calculated Property
λliquid	0.14	W/m×K	295.86	Calculated Property
λliquid	0.13	W/m×K	326.98	Calculated Property
λliquid	0.12	W/m×K	358.09	Calculated Property
λliquid	0.12	W/m×K	389.20	Calculated Property
λliquid	0.11	W/m×K	420.31	Calculated Property
λliquid	0.10	W/m×K	451.42	Calculated Property

Similar Compounds

Find more compounds similar to Methyl Isobutyl Ketone.

Mixtures

• Methyl Isobutyl Ketone + Water
• Methyl Isobutyl Ketone + Lithium chloride + Water
• Methyl Isobutyl Ketone + sodium chloride + Water
• potassium chloride + Methyl Isobutyl Ketone + Water
• Methyl Isobutyl Ketone + Water + Lithium sulfate
• Methyl Isobutyl Ketone + sodium sulphate + Water
• Methyl Isobutyl Ketone + Sodium nitrate + Water
• Methyl Isobutyl Ketone + Water + Acetic acid, lithium salt
• Methyl Isobutyl Ketone + Acetic acid, sodium salt + Water
• Methyl Isobutyl Ketone + Furan, 2,5-dimethyl-
• Methyl Isobutyl Ketone + Phenol, 2-methyl- + Water
• Methyl Isobutyl Ketone + Phenol, 3-methyl- + Water
• Methyl Isobutyl Ketone + PHENOL, 4-METHYL- + Water
• Methyl Isobutyl Ketone + 1-Propanol, 2-methyl-
• Methyl Isobutyl Ketone + Pentane, 2,2,4-trimethyl-
• Methyl Isobutyl Ketone + 1-Propanol, 2-methyl- + Pentane, 2,2,4-trimethyl-
• Methyl Isobutyl Ketone + 5-Hydroxymethylfurfural + Water
• Methyl Isobutyl Ketone + Trichloromethane
• Methyl Isobutyl Ketone + sodium chloride + Maleic acid
• Methyl Isobutyl Ketone + Furfural

Find more mixtures with Methyl Isobutyl Ketone.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, diisopropyl ether and 4-methyl-2-pentanone
• Liquid liquid equilibria for the quaternary system methyl isobutyl ketone water phenol hydroquinone
• Isobaric vapour liquid equilibria for the binary systems 4-methyl-2-pentanone + 1-butanol and + 2-butanol at 20 and 101.3 kPa
• Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
• Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2,2,4-trimethylpentane, 2-methyl-1-propanol, and 4-methyl-2-pentanone
• Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
• Measurements and correlation of liquid-liquid equilibria of 4-methyl-2-pentanone + ethanol + water and 4-methyl-2-pentanone + n-butanol + water ternary systems between 283.2 and 323.2 K
• Solubility of lansoprazole in different solvents
• 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
• Liquid liquid equilibria of 4-methyl-2-pentanone + 1-propanol or 2-propanol + water ternary systems: Measurements and correlation at different temperatures
• Isothermal vapor-liquid equilibrium and excess molar enthalpies of the binary mixtures furfural + methyl isobutyl ketone, + 2-butanol and + 2-methyl-2-butanol
• Liquid-liquid equilibria of water + lactic acid + methyl isobutyl ketone
• Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Salt influence on MIBK/water liquid-liquid equilibrium: Measuring and modeling with ePC-SAFT and COSMO-RS
• Liquid-liquid equilibria for methyl isobutyl ketone + cresols + water at 333.15K, 343.15K and 353.15K: Experimental results and data correlation
• Liquid-liquid equilibrium for ternary systems, methyl isobutyl ketone +(catechol, resorcinol and hydroquinone) + water at 333.15 K, 343.15 K and 353.15 K
• Measurement of the solubility of the salt of 2- mercaptobenzothiazole with cyclohexylamine and tert-butylamine in various solvents at low temperatures: Models and thermodynamic parameters
• The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
• Liquid-liquid equilibria of ternary and quaternary systems involving 5-hydroxymethylfurfural, water, organic solvents, and salts at 313.15 K and atmospheric pressure
• Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
• Salt effect on liquid-liquid equilibria of tetrahydrofuran/water/5-hydroxymethylfurfural systems
• Salting-out effect of NaCl and KCl on the ternary LLE data for the systems of (water + propionic acid + isopropyl methyl ketone) and of (water + propionic acid + isobutyl methyl ketone)
• 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
• Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
• Density, viscosity, isothermal (vapour + liquid) equilibrium, excess molar volume, viscosity deviation, and their correlations for chloroform + methyl isobutyl ketone binary system
• Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
• Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
• Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
• Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
• Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
• Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
• Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
• Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
• Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
• Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
• Influence of Salt on the Solubility and Tie-Line Data for Water + Formic Acid + Methyl Isobutyl Ketone at T = 298.15 K
• Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
• Phase Equilibrium Measurement and Thermodynamic Modeling of the 4-Methylpentan-2-one/3-Methylphenol, and 4-Methylphenol/Water Ternary Systems at 298.2, 313.2, and 323.2 K and 0.1 MPa
• Liquid-Liquid Equilibria of Ionic Liquids-Water-Acetic Acid Mixtures
• Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
• Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
• Determination and Thermodynamic Modeling of Solid Liquid Phase Equilibrium for Esomeprazole Sodium in Monosolvents and in the (Ethanol + Ethyl Acetate) Binary Solvent Mixtures
• Vapor Liquid Equilibrium for Methyl Isobutyl Ketone (MIBK) + (1-Propanol or 2-Propanol) Binary Mixtures
• Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
• Measurement and Thermodynamic Modeling of Ternary (Liquid + Liquid) Equilibrium for Extraction of N,N-Dimethylacetamide from Aqueous Solution with Different Solvents
• Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
• Liquid-Liquid Equilibrium Data and Correlation for the Quaternary Systems Water + Polyphenol (Hydroquinone, Catechol, and Resorcinol) + Methyl Isobutyl Ketone + Methylbenzene
• Liquid-Liquid Equilibria for the Ternary Systems Water + Cyclohexanol + Methyl Isobutyl Carbinol and Water + Cyclohexanol + Methyl Isobutyl Ketone at Different Temperatures
• Liquid-Liquid Equilibrium of Water + 2-Methoxyphenol + Methyl Isobutyl Ketone and Water + 1,2-Benzenediol + Methyl Isobutyl Ketone at 303.15 K and 328.15 K
• Solubility of 2,5-Furandicarboxylic Acid in Eight Pure Solvents and Two Binary Solvent Systems at 313.15-363.15 K
• Liquid-Liquid Equilibrium for the Ternary Systems (Methyl Isobutyl Ketone + Quinoline or Isoquinoline + Water) at 298.15, 318.15, and 338.15 K
• Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
• Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
• Experimental Study on Reactive Extraction of Malonic Acid with Validation by Fourier Transform Infrared Spectroscopy
• Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
• Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
• Experiments and COSMO-SAC Modeling of Methyl Isobutyl Ketone + Dimethylphenols + Water Mixtures
• Vapor-Liquid Equilibrium for Binary of 1-Butanol + N,N-Dimethylacetamide and Methyl Isobutyl Ketone + N,N-Dimethylacetamide at 101.3 kPa
• Air-Water Partitioning of C5 and C6 Alkanones: Measurement, Critical Compilation, Correlation, and Recommended Data
• Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K
• Measurements of Quaternary Liquid-Liquid Equilibrium for Water + Acetic Acid + Propionic Acid + Solvent (Butyronitrile, Benzyl Acetate, or Methyl Isobutyl Ketone) at 298.15 K
• Distribution of Butyric Acid between Water and Several Solvents
• Liquid-Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + Water + Hydroquinone
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
• Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 4-Methyl-2-pentanone + 2-Butanol + Water System
• Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• Liquid Liquid Equilibria for the System Water + 4-Methylpentan-2-one + Acetic Acid at Several Temperatures
• Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + m-Benzenediol + Water
• Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + 1,2-Benzenediol + Water
• Liquid Liquid Equilibria of the Ternary System Water + Acrylic Acid + 4-Methyl-2-pentanone at 298.15 K
• Liquid Liquid Equilibria for the Ternary System Water + Methyl Isobutyl Ketone + tert-Butyl Alcohol at Several Temperatures
• Viscosity of the Tributyl Phosphate + Methyl Isobutyl Ketone + Phosphoric Acid System
• Volumetric and Transport Properties of Binary Liquid Mixtures of Aliphatic Ketones with Phenylacetonitrile at T = 308.15 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
• Solubility of Penicillin Sulfoxide in Different Solvents
• Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
• Conductivity and Dissociation Constants of Quaternary Ammonium Perchlorates and Picrates in 4-Methyl-pentan-2-one
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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