Chemical Properties of 3-Penten-2-one, 4-methyl- (CAS 141-79-7)

InChI

InChI=1S/C6H10O/c1-5(2)4-6(3)7/h4H,1-3H3

InChI Key

SHOJXDKTYKFBRD-UHFFFAOYSA-N

Formula

C6H10O

SMILES

CC(=O)C=C(C)C

Molecular Weight¹

98.14

CAS

141-79-7

Other Names

• (CH3)2C=CHC(=O)CH3
• 2,2-Dimethylvinyl methyl ketone
• 2-Methyl-2-penten-4-one
• 2-Methyl-2-pentenone-4
• 2-Methyl-4-oxo-2-pentene
• 2-Methylpent-2-en-4-one
• 3-Isohexen-2-one
• 4-Methyl-3-penten-2-on
• 4-Methyl-3-pentene-2-one
• 4-Methylpent-3-en-2-one
• 4-Metil-3-penten-2-one
• 4-methyl-3-penten-2-one
• 4-methyl-3-penten-2-one (mesityl oxide)
• Acetone, isopropylidene-
• Isobutenyl methyl ketone
• Isopropylideneacetone
• MIBK
• Mesityloxid
• Mesityloxyde
• Methyl 2,2-dimethylvinyl ketone
• Methyl 2-methyl-1-propenyl ketone
• Methyl isobutenyl ketone
• NSC 38717
• Ossido di mesitile
• Oxyde de mesityle
• UN 1229
• mesityl oxide

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• 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).
• 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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• 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	[0.3254; 0.4004]
ω	0.4004		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3254		ChemSep v8.3 pure component data Compiled value
PAff	878.70	kJ/mol	NIST
BasG	846.90	kJ/mol	NIST
ΔcH°liquid	[-3571.00; -3540.00]	kJ/mol
ΔcH°liquid	-3569.23 ± 0.48	kJ/mol	NIST
ΔcH°liquid	-3571.00 ± 0.80	kJ/mol	NIST
ΔcH°liquid	-3540.00	kJ/mol	NIST
ΔcH°liquid	-3549.00	kJ/mol	NIST
μ	3.21	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-78.81	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-195.60; -178.28]	kJ/mol
ΔfH°gas	-195.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-178.28 ± 0.64	kJ/mol	NIST
ΔfH°gas	-184.50 ± 2.50	kJ/mol	NIST
ΔfH°liquid	[-220.98; -219.00]	kJ/mol
ΔfH°liquid	-220.98 ± 0.58	kJ/mol	NIST
ΔfH°liquid	-219.00 ± 0.80	kJ/mol	NIST
ΔfusH°	11.79	kJ/mol	Joback Calculated Property
ΔvapH°	[42.70; 44.80]	kJ/mol
ΔvapH°	42.70 ± 0.28	kJ/mol	NIST
ΔvapH°	42.70 ± 0.30	kJ/mol	NIST
ΔvapH°	44.80	kJ/mol	NIST
ΔvapH°	43.30	kJ/mol	NIST
ΔvapH°	42.70 ± 0.28	kJ/mol	NIST
IE	[8.89; 9.11]	eV
IE	9.10 ± 0.02	eV	NIST
IE	9.11	eV	NIST
IE	9.08 ± 0.03	eV	NIST
IE	8.89 ± 0.05	eV	NIST
logPoct/wat	1.045		NCMS SOLV-DB
McVol	92.670	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	3		KDB
Pc	[3410.00; 4000.00]	kPa
Pc	4000.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3749.03	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3410.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4000.00 ± 150.00	kPa	NIST
Pc	4000.00 ± 150.00	kPa	NIST
Ptriple	2.51e-03	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[277.74; 277.74]	kg/m3
ρc	277.74 ± 9.81	kg/m3	NIST
ρc	277.74 ± 9.81	kg/m3	NIST
Inp	[771.00; 804.00]
Inp	Outlier 771.00		NIST
Inp	782.00		NIST
Inp	778.00		NIST
Inp	792.00		NIST
Inp	798.00		NIST
Inp	801.10		NIST
Inp	778.00		NIST
Inp	792.00		NIST
Inp	800.00		NIST
Inp	780.00		NIST
Inp	787.00		NIST
Inp	798.00		NIST
Inp	804.00		NIST
Inp	782.00		NIST
Inp	797.00		NIST
Inp	798.00		NIST
Inp	798.00		NIST
Inp	802.00		NIST
Inp	798.00		NIST
Inp	798.00		NIST
Inp	783.00		NIST
Inp	804.00		NIST
Inp	783.00		NIST
Inp	778.00		NIST
Inp	798.00		NIST
Inp	804.00		NIST
Ip	[1110.00; 1159.00]
Ip	1125.00		NIST
Ip	1118.00		NIST
Ip	1118.00		NIST
Ip	Outlier 1159.00		NIST
Ip	1131.00		NIST
Ip	1136.00		NIST
Ip	1125.00		NIST
Ip	1114.00		NIST
Ip	Outlier 1152.00		NIST
Ip	1129.00		NIST
Ip	1113.00		NIST
Ip	1110.00		NIST
Ip	1110.00		NIST
Ip	1127.00		NIST
Ip	1140.00		NIST
Ip	1131.00		NIST
Ip	1111.00		NIST
Ip	1127.00		NIST
Ip	1128.00		NIST
Ip	1125.00		NIST
Ip	1137.00		NIST
Ip	1140.00		NIST
Ip	1118.00		NIST
Ip	1114.00		NIST
Ip	1110.00		NIST
Tboil	[401.40; 403.15]	K
Tboil	402.95	K	ChemSep v8.3 pure component data Compiled value
Tboil	403.15	K	NCMS SOLV-DB
Tboil	402.90	K	NIST
Tboil	402.95	K	NIST
Tboil	402.05 ± 1.00	K	NIST
Tboil	403.15 ± 1.50	K	NIST
Tboil	401.40 ± 1.50	K	NIST
Tboil	402.60 ± 0.50	K	NIST
Tboil	402.60 ± 0.50	K	NIST
Tboil	401.54 ± 0.30	K	NIST
Tboil	403.15 ± 1.00	K	NIST
Tc	[597.00; 605.00]	K
Tc	605.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	597.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	600.00	K	ChemSep v8.3 pure component data Compiled value
Tc	605.00 ± 2.00	K	NIST
Tc	605.00 ± 2.00	K	NIST
Tfus	[214.15; 226.75]	K
Tfus	214.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	226.75	K	ChemSep v8.3 pure component data Compiled value
Tfus	216.15	K	NCMS SOLV-DB
Tfus	226.75	K	NIST
Tfus	220.30 ± 0.30	K	NIST
Ttriple	220.15	K	ChemSep v8.3 pure component data Compiled value
UQi	3.86		ChemSep v8.3 pure component data Compiled value
URi	4.36		ChemSep v8.3 pure component data Compiled value
Vc	[0.278; 0.355]	m3/kmol
Vc	0.353	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.278	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.355	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	[0.2430000; 0.2810000]
Zc	0.2810000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc	0.2430000		ChemSep v8.3 pure component data Compiled value
Zra	0.24		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	0.0005800	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	12.10	kJ/mol	229.60	NIST
ΔvapH	[33.50; 41.50]	kJ/mol	[359.00; 435.00]
ΔvapH	41.50	kJ/mol	359.00	NIST
ΔvapH	41.40 ± 0.30	kJ/mol	372.50	NIST
ΔvapH	39.10 ± 0.30	kJ/mol	372.50	NIST
ΔvapH	36.50 ± 0.30	kJ/mol	372.50	NIST
ΔvapH	33.50 ± 0.60	kJ/mol	372.50	NIST
ΔvapH	35.20	kJ/mol	401.00	NIST
ΔvapH	37.80	kJ/mol	435.00	NIST
Pvap	1.09	kPa	298.15	NCMS SOLV-DB
n0	1.44500		298.15	NCMS SOLV-DB
ρl	857.60	kg/m3	298.15	Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
γ	0.03	N/m	298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[123.62; 334.50]	J/mol×K	[255.00; 1500.00]	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			7.20686e+01
Coefficient B			-5.00000e+02
Coefficient C			5.90331e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	123.62	J/mol×K	255.00	Calculated Property
Cp,gas	174.80	J/mol×K	393.33	Calculated Property
Cp,gas	215.07	J/mol×K	531.67	Calculated Property
Cp,gas	245.72	J/mol×K	670.00	Calculated Property
Cp,gas	269.38	J/mol×K	808.33	Calculated Property
Cp,gas	288.04	J/mol×K	946.67	Calculated Property
Cp,gas	303.08	J/mol×K	1085.00	Calculated Property
Cp,gas	315.44	J/mol×K	1223.33	Calculated Property
Cp,gas	325.76	J/mol×K	1361.67	Calculated Property
Cp,gas	334.50	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[210.79; 240.20]	J/mol×K	[292.48; 402.95]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.32950e+02
Coefficient B			2.66150e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			292.48
Temperature range, max.			402.95
Cp,liquid	210.79	J/mol×K	292.48	Calculated Property
Cp,liquid	214.06	J/mol×K	304.75	Calculated Property
Cp,liquid	217.33	J/mol×K	317.03	Calculated Property
Cp,liquid	220.59	J/mol×K	329.30	Calculated Property
Cp,liquid	223.86	J/mol×K	341.58	Calculated Property
Cp,liquid	227.13	J/mol×K	353.85	Calculated Property
Cp,liquid	230.39	J/mol×K	366.13	Calculated Property
Cp,liquid	233.66	J/mol×K	378.40	Calculated Property
Cp,liquid	236.93	J/mol×K	390.68	Calculated Property
Cp,liquid	240.20	J/mol×K	402.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0025628; 0.0002072]	Pa×s	[220.15; 480.00]	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			-3.81070e+01
Coefficient B			3.38240e+03
Coefficient C			3.37060e+01
Coefficient D			-7.34840e+01
Coefficient E			1.50000e-01
Temperature range, min.			220.15
Temperature range, max.			480.00
η	0.0025628	Pa×s	220.15	Calculated Property
η	0.0012639	Pa×s	249.02	Calculated Property
η	0.0007643	Pa×s	277.89	Calculated Property
η	0.0005296	Pa×s	306.77	Calculated Property
η	0.0004031	Pa×s	335.64	Calculated Property
η	0.0003278	Pa×s	364.51	Calculated Property
η	0.0002797	Pa×s	393.38	Calculated Property
η	0.0002471	Pa×s	422.26	Calculated Property
η	0.0002241	Pa×s	451.13	Calculated Property
η	0.0002072	Pa×s	480.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[46.59; 0.00]	kJ/mol	[220.15; 600.00]	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			5.58140e+01
Coefficient B			3.95240e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.00000e+02
Temperature range, min.			220.15
Temperature range, max.			600.00
ΔvapH	46.59	kJ/mol	220.15	Calculated Property
ΔvapH	44.47	kJ/mol	262.36	Calculated Property
ΔvapH	42.18	kJ/mol	304.56	Calculated Property
ΔvapH	39.69	kJ/mol	346.77	Calculated Property
ΔvapH	36.93	kJ/mol	388.97	Calculated Property
ΔvapH	33.81	kJ/mol	431.18	Calculated Property
ΔvapH	30.18	kJ/mol	473.38	Calculated Property
ΔvapH	25.71	kJ/mol	515.59	Calculated Property
ΔvapH	19.55	kJ/mol	557.79	Calculated Property
ΔvapH	0.00	kJ/mol	600.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[295.47; 429.29]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43990e+01
Coefficient B			-3.41585e+03
Coefficient C			-5.34050e+01
Temperature range, min.			295.47
Temperature range, max.			429.29
Pvap	1.33	kPa	295.47	Calculated Property
Pvap	3.02	kPa	310.34	Calculated Property
Pvap	6.24	kPa	325.21	Calculated Property
Pvap	11.98	kPa	340.08	Calculated Property
Pvap	21.56	kPa	354.95	Calculated Property
Pvap	36.72	kPa	369.81	Calculated Property
Pvap	59.61	kPa	384.68	Calculated Property
Pvap	92.83	kPa	399.55	Calculated Property
Pvap	139.38	kPa	414.42	Calculated Property
Pvap	202.66	kPa	429.29	Calculated Property
Pvap	[2.51e-03; 3408.10]	kPa	[220.15; 600.00]	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			5.57712e+01
Coefficient B			-6.81500e+03
Coefficient C			-5.71030e+00
Coefficient D			5.34520e-18
Coefficient E			6.00000e+00
Temperature range, min.			220.15
Temperature range, max.			600.00
Pvap	2.51e-03	kPa	220.15	Calculated Property
Pvap	0.13	kPa	262.36	Calculated Property
Pvap	2.10	kPa	304.56	Calculated Property
Pvap	15.33	kPa	346.77	Calculated Property
Pvap	67.75	kPa	388.97	Calculated Property
Pvap	212.38	kPa	431.18	Calculated Property
Pvap	523.28	kPa	473.38	Calculated Property
Pvap	1086.99	kPa	515.59	Calculated Property
Pvap	2003.38	kPa	557.79	Calculated Property
Pvap	3408.10	kPa	600.00	Calculated Property
Pvap	[2.36e-03; 3355.54]	kPa	[220.15; 600.00]	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			6.11275e+01
Coefficient B			-6.98731e+03
Coefficient C			-6.58940e+00
Coefficient D			2.18991e-06
Coefficient E			0.00000e+00
Temperature range, min.			220.15
Temperature range, max.			600.00
Pvap	2.36e-03	kPa	220.15	Calculated Property
Pvap	0.13	kPa	262.36	Calculated Property
Pvap	2.02	kPa	304.56	Calculated Property
Pvap	14.91	kPa	346.77	Calculated Property
Pvap	66.64	kPa	388.97	Calculated Property
Pvap	211.60	kPa	431.18	Calculated Property
Pvap	527.29	kPa	473.38	Calculated Property
Pvap	1101.75	kPa	515.59	Calculated Property
Pvap	2019.94	kPa	557.79	Calculated Property
Pvap	3355.54	kPa	600.00	Calculated Property
Pvap	[0.74; 102.58]	kPa	[287.00; 403.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42611e+01
Coefficient B			-3.30336e+03
Coefficient C			-6.00880e+01
Reference			Fuge, Bowden, et al., 1952
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			287.00
Temperature range, max.			403.10
Pvap	0.74	kPa	287.00	Calculated Property
Pvap	1.63	kPa	299.90	Calculated Property
Pvap	3.29	kPa	312.80	Calculated Property
Pvap	6.20	kPa	325.70	Calculated Property
Pvap	11.03	kPa	338.60	Calculated Property
Pvap	18.64	kPa	351.50	Calculated Property
Pvap	30.14	kPa	364.40	Calculated Property
Pvap	46.87	kPa	377.30	Calculated Property
Pvap	70.41	kPa	390.20	Calculated Property
Pvap	102.58	kPa	403.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[919.57; 276.47]	kg/m3	[220.15; 600.00]	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			7.03293e+01
Coefficient B			2.54380e-01
Coefficient C			6.00000e+02
Coefficient D			2.84840e-01
Temperature range, min.			220.15
Temperature range, max.			600.00
ρl	919.57	kg/m3	220.15	Calculated Property
ρl	883.82	kg/m3	262.36	Calculated Property
ρl	846.31	kg/m3	304.56	Calculated Property
ρl	806.59	kg/m3	346.77	Calculated Property
ρl	764.05	kg/m3	388.97	Calculated Property
ρl	717.69	kg/m3	431.18	Calculated Property
ρl	665.80	kg/m3	473.38	Calculated Property
ρl	604.94	kg/m3	515.59	Calculated Property
ρl	525.75	kg/m3	557.79	Calculated Property
ρl	276.47	kg/m3	600.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.00]	N/m	[220.15; 600.00]	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 γ in N/m, T in K
Coefficient A			6.61200e-02
Coefficient B			1.25600e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.00000e+02
Temperature range, min.			220.15
Temperature range, max.			600.00
γ	0.04	N/m	220.15	Calculated Property
γ	0.03	N/m	262.36	Calculated Property
γ	0.03	N/m	304.56	Calculated Property
γ	0.02	N/m	346.77	Calculated Property
γ	0.02	N/m	388.97	Calculated Property
γ	0.01	N/m	431.18	Calculated Property
γ	0.01	N/m	473.38	Calculated Property
γ	0.01	N/m	515.59	Calculated Property
γ	0.00	N/m	557.79	Calculated Property
γ	0.00	N/m	600.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.08]	W/m×K	[402.95; 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			1.77700e-04
Coefficient B			9.62200e-01
Coefficient C			6.84700e+02
Coefficient D			0.00000e+00
Temperature range, min.			402.95
Temperature range, max.			1000.00
λgas	0.02	W/m×K	402.95	Calculated Property
λgas	0.03	W/m×K	469.29	Calculated Property
λgas	0.03	W/m×K	535.63	Calculated Property
λgas	0.04	W/m×K	601.97	Calculated Property
λgas	0.05	W/m×K	668.31	Calculated Property
λgas	0.05	W/m×K	734.64	Calculated Property
λgas	0.06	W/m×K	800.98	Calculated Property
λgas	0.07	W/m×K	867.32	Calculated Property
λgas	0.07	W/m×K	933.66	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.18; 0.13]	W/m×K	[220.15; 402.95]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.40530e-01
Coefficient B			-2.84300e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			220.15
Temperature range, max.			402.95
λliquid	0.18	W/m×K	220.15	Calculated Property
λliquid	0.17	W/m×K	240.46	Calculated Property
λliquid	0.17	W/m×K	260.77	Calculated Property
λliquid	0.16	W/m×K	281.08	Calculated Property
λliquid	0.15	W/m×K	301.39	Calculated Property
λliquid	0.15	W/m×K	321.71	Calculated Property
λliquid	0.14	W/m×K	342.02	Calculated Property
λliquid	0.14	W/m×K	362.33	Calculated Property
λliquid	0.13	W/m×K	382.64	Calculated Property
λliquid	0.13	W/m×K	402.95	Calculated Property

Similar Compounds

Find more compounds similar to 3-Penten-2-one, 4-methyl-.

Mixtures

• 3-Penten-2-one, 4-methyl- + Phenol, 2-methyl- + Water
• 3-Penten-2-one, 4-methyl- + Phenol, 3-methyl- + Water
• 3-Penten-2-one, 4-methyl- + PHENOL, 4-METHYL- + Water
• 3-Penten-2-one, 4-methyl- + Phenol + Water
• 3-Penten-2-one, 4-methyl- + Propanoic acid + Water
• 3-Penten-2-one, 4-methyl- + Butanoic acid + Water
• 3-Penten-2-one, 4-methyl- + 1,2-Benzenediol + Water
• Cyclohexanol + 3-Penten-2-one, 4-methyl- + Water
• 3-Penten-2-one, 4-methyl- + Water
• 3-Penten-2-one, 4-methyl- + Cyclohexanone + Water

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.
• Crippen Method
• Measurement, correlation and COSMO-SAC prediction of liquid-liquid equilibrium for the ternary systems, mesityl oxide + o-, m-, p-cresol + water, at 333.2 K and 353.2 K
• Screening solvents to extract phenol from aqueous solutions by the COSMO-SAC model and extraction process simulation
• Liquid phase equilibrium of the ternary systems, water + propionic or butyric acid + mesityl oxide, at (298.2 and 323.2) K
• Liquid-Liquid Equilibria for the Ternary System Mesityl Oxide + Phenol + Water at 298.15, 313.15, and 323.15 K
• Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
• Measurement and Correlation of Ternary (Liquid + Liquid) Equilibria for Separation of Cyclohexanone from Water via Isophorone or Mesityl Oxide
• Liquid-Liquid Equilibrium for Ternary Systems of 2-Pentanone/Mesityl Oxide + Catechol + Water at 298.2, 318.2, and 333.2 K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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