Chemical Properties of 3-Heptanone (CAS 106-35-4)

InChI

InChI=1S/C7H14O/c1-3-5-6-7(8)4-2/h3-6H2,1-2H3

InChI Key

NGAZZOYFWWSOGK-UHFFFAOYSA-N

Formula

C7H14O

SMILES

CCCCC(=O)CC

Molecular Weight¹

114.19

CAS

106-35-4

Other Names

• 3-Oxoheptane
• Aethylbutylketon
• Eptan-3-one
• Ethyl n-butyl ketone
• Ethylbutylcetone
• Ethylbutylketon
• Etilbutilchetone
• Heptan-3-on
• Heptan-3-one
• NSC 8448
• butyl ethyl ketone
• ethyl butyl ketone
• n-Butyl ethyl ketone
• n-C4H9COC2H5
• n-Heptan-3-one

• ω : Acentric Factor.
• 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_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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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	[0.4076; 0.4346]
ω	0.4346		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4076		ChemSep v8.3 pure component data Compiled value
μ	2.81	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-119.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-301.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	15.48	kJ/mol	Joback Calculated Property
ΔvapH°	42.53	kJ/mol	Relay (1.0) Calculated Property
IE	[9.02; 9.26]	eV
IE	9.15 ± 0.09	eV	NIST
IE	9.18	eV	NIST
IE	9.26	eV	NIST
IE	9.02 ± 0.02	eV	NIST
IE	9.15 ± 0.02	eV	NIST
log10WS	-1.53		Relay (1.0) Calculated Property
logPoct/wat	2.156		Crippen Calculated Property
McVol	111.060	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	1		KDB
Pc	[2920.19; 3010.00]	kPa
Pc	2920.19	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3010.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	2.30e-03	kPa	ChemSep v8.3 pure component data Compiled value
ρc	263.77 ± 3.43	kg/m3	NIST
Inp	[847.00; 899.00]
Inp	865.80		NIST
Inp	867.00		NIST
Inp	865.00		NIST
Inp	865.00		NIST
Inp	867.00		NIST
Inp	866.20		NIST
Inp	866.50		NIST
Inp	887.50		NIST
Inp	887.40		NIST
Inp	852.00		NIST
Inp	863.00		NIST
Inp	847.00		NIST
Inp	847.00		NIST
Inp	852.00		NIST
Inp	887.00		NIST
Inp	885.00		NIST
Inp	884.10		NIST
Inp	895.00		NIST
Inp	894.00		NIST
Inp	859.00		NIST
Inp	888.00		NIST
Inp	896.00		NIST
Inp	865.00		NIST
Inp	886.00		NIST
Inp	889.00		NIST
Inp	871.00		NIST
Inp	886.00		NIST
Inp	886.00		NIST
Inp	887.00		NIST
Inp	869.42		NIST
Inp	888.00		NIST
Inp	865.00		NIST
Inp	890.00		NIST
Inp	869.00		NIST
Inp	860.00		NIST
Inp	862.00		NIST
Inp	890.00		NIST
Inp	847.00		NIST
Inp	866.00		NIST
Inp	888.00		NIST
Inp	868.00		NIST
Inp	860.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	865.00		NIST
Inp	888.00		NIST
Inp	869.00		NIST
Inp	884.00		NIST
Inp	865.00		NIST
Inp	880.00		NIST
Inp	899.00		NIST
Inp	866.00		NIST
Inp	869.00		NIST
Inp	861.00		NIST
Inp	869.00		NIST
Inp	866.00		NIST
Inp	887.00		NIST
Inp	886.00		NIST
Inp	869.00		NIST
Inp	865.80		NIST
Inp	866.20		NIST
Inp	863.00		NIST
Inp	890.00		NIST
Inp	860.00		NIST
Inp	866.00		NIST
Inp	894.00		NIST
Inp	865.00		NIST
Ip	[1124.00; 1185.00]
Ip	1185.00		NIST
Ip	1167.20		NIST
Ip	1173.20		NIST
Ip	1179.90		NIST
Ip	1141.00		NIST
Ip	1148.00		NIST
Ip	1141.00		NIST
Ip	1163.00		NIST
Ip	1134.00		NIST
Ip	1171.00		NIST
Ip	1160.00		NIST
Ip	1131.00		NIST
Ip	1161.00		NIST
Ip	1163.00		NIST
Ip	1157.00		NIST
Ip	1155.00		NIST
Ip	1162.00		NIST
Ip	1167.00		NIST
Ip	1155.00		NIST
Ip	Outlier 1124.00		NIST
Ip	1141.00		NIST
Ip	1171.00		NIST
Ip	1161.00		NIST
Ip	1185.00		NIST
Ip	1160.00		NIST
Ip	1167.00		NIST
Tboil	[414.15; 422.65]	K
Tboil	420.55	K	ChemSep v8.3 pure component data Compiled value
Tboil	420.70	K	NIST
Tboil	420.45	K	NIST
Tboil	418.65 ± 3.00	K	NIST
Tboil	420.80 ± 0.60	K	NIST
Tboil	420.95 ± 1.00	K	NIST
Tboil	420.75 ± 0.50	K	NIST
Tboil	420.55 ± 0.50	K	NIST
Tboil	418.65 ± 3.00	K	NIST
Tboil	418.90 ± 3.00	K	NIST
Tboil	420.15 ± 3.00	K	NIST
Tboil	416.65 ± 3.00	K	NIST
Tboil	Outlier 414.15 ± 2.00	K	NIST
Tboil	420.20 ± 0.50	K	NIST
Tboil	420.65 ± 4.00	K	NIST
Tboil	422.65 ± 5.00	K	NIST
Tc	[602.00; 606.60]	K
Tc	606.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	602.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	605.00	K	ChemSep v8.3 pure component data Compiled value
Tc	606.60 ± 0.25	K	NIST
Tfus	[234.15; 420.45]	K
Tfus	234.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	234.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	420.45	K	NIST
Ttriple	234.15	K	ChemSep v8.3 pure component data Compiled value
UQi	4.50		ChemSep v8.3 pure component data Compiled value
URi	5.27		ChemSep v8.3 pure component data Compiled value
Vc	[0.421; 0.433]	m3/kmol
Vc	0.433	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.430	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.421	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2510000		ChemSep v8.3 pure component data Compiled value
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔfusH	17.53	kJ/mol	236.00	NIST
Pvap	[11.05; 90.50]	kPa	[354.82; 416.50]
Pvap	11.05	kPa	354.82	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	12.93	kPa	358.58	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	15.51	kPa	363.03	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	18.75	kPa	367.95	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	23.27	kPa	373.60	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	27.11	kPa	377.99	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	32.58	kPa	383.09	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.00	kPa	388.11	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.00	kPa	388.36	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	39.13	kPa	388.62	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	40.00	kPa	388.67	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	45.12	kPa	393.02	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	54.02	kPa	398.84	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	64.03	kPa	404.44	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	74.50	kPa	409.63	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	82.00	kPa	412.95	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap	90.50	kPa	416.50	Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[139.65; 413.62]	J/mol×K	[200.00; 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			1.22140e+02
Coefficient B			-6.68770e+02
Coefficient C			6.20924e+00
Coefficient D			-6.49860e-06
Coefficient E			-3.49690e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	139.65	J/mol×K	200.00	Calculated Property
Cp,gas	193.04	J/mol×K	344.44	Calculated Property
Cp,gas	247.32	J/mol×K	488.89	Calculated Property
Cp,gas	292.03	J/mol×K	633.33	Calculated Property
Cp,gas	327.18	J/mol×K	777.78	Calculated Property
Cp,gas	354.51	J/mol×K	922.22	Calculated Property
Cp,gas	375.69	J/mol×K	1066.67	Calculated Property
Cp,gas	392.00	J/mol×K	1211.11	Calculated Property
Cp,gas	404.40	J/mol×K	1355.56	Calculated Property
Cp,gas	413.62	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[234.90; 323.07]	J/mol×K	[234.15; 480.00]	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			2.15140e+02
Coefficient B			4.47780e+02
Coefficient C			-2.99716e+00
Coefficient D			2.05390e-02
Coefficient E			-1.35110e-05
Temperature range, min.			234.15
Temperature range, max.			480.00
Cp,liquid	234.90	J/mol×K	234.15	Calculated Property
Cp,liquid	238.76	J/mol×K	261.47	Calculated Property
Cp,liquid	243.87	J/mol×K	288.78	Calculated Property
Cp,liquid	250.37	J/mol×K	316.10	Calculated Property
Cp,liquid	258.38	J/mol×K	343.42	Calculated Property
Cp,liquid	268.03	J/mol×K	370.73	Calculated Property
Cp,liquid	279.38	J/mol×K	398.05	Calculated Property
Cp,liquid	292.43	J/mol×K	425.37	Calculated Property
Cp,liquid	307.06	J/mol×K	452.68	Calculated Property
Cp,liquid	323.07	J/mol×K	480.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0024263; 0.0001170]	Pa×s	[234.15; 505.00]	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			-1.19820e+01
Coefficient B			1.28420e+03
Coefficient C			9.54910e-02
Coefficient D			-8.18940e-07
Coefficient E			2.00000e+00
Temperature range, min.			234.15
Temperature range, max.			505.00
η	0.0024263	Pa×s	234.15	Calculated Property
η	0.0012982	Pa×s	264.24	Calculated Property
η	0.0007871	Pa×s	294.34	Calculated Property
η	0.0005220	Pa×s	324.43	Calculated Property
η	0.0003700	Pa×s	354.53	Calculated Property
η	0.0002758	Pa×s	384.62	Calculated Property
η	0.0002138	Pa×s	414.72	Calculated Property
η	0.0001709	Pa×s	444.81	Calculated Property
η	0.0001400	Pa×s	474.91	Calculated Property
η	0.0001170	Pa×s	505.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[51.67; 15.37]	kJ/mol	[234.15; 587.00]	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			6.72690e+01
Coefficient B			8.30475e-01
Coefficient C			-1.25639e+00
Coefficient D			1.59272e+00
Coefficient E			-7.56362e-01
Critical temperature, Tc (K)			6.05000e+02
Temperature range, min.			234.15
Temperature range, max.			587.00
ΔvapH	51.67	kJ/mol	234.15	Calculated Property
ΔvapH	49.26	kJ/mol	273.36	Calculated Property
ΔvapH	46.69	kJ/mol	312.56	Calculated Property
ΔvapH	43.91	kJ/mol	351.77	Calculated Property
ΔvapH	40.87	kJ/mol	390.97	Calculated Property
ΔvapH	37.51	kJ/mol	430.18	Calculated Property
ΔvapH	33.75	kJ/mol	469.38	Calculated Property
ΔvapH	29.41	kJ/mol	508.59	Calculated Property
ΔvapH	23.99	kJ/mol	547.79	Calculated Property
ΔvapH	15.37	kJ/mol	587.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[313.94; 445.72]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50665e+01
Coefficient B			-3.78159e+03
Coefficient C			-5.80630e+01
Temperature range, min.			313.94
Temperature range, max.			445.72
Pvap	1.33	kPa	313.94	Calculated Property
Pvap	2.97	kPa	328.58	Calculated Property
Pvap	6.08	kPa	343.22	Calculated Property
Pvap	11.62	kPa	357.87	Calculated Property
Pvap	20.91	kPa	372.51	Calculated Property
Pvap	35.71	kPa	387.15	Calculated Property
Pvap	58.26	kPa	401.79	Calculated Property
Pvap	91.32	kPa	416.44	Calculated Property
Pvap	138.19	kPa	431.08	Calculated Property
Pvap	202.66	kPa	445.72	Calculated Property
Pvap	[2.73e-03; 2791.43]	kPa	[234.15; 605.00]	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			5.30322e+01
Coefficient B			-7.15697e+03
Coefficient C			-5.20128e+00
Coefficient D			1.28894e-07
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 606.6 K.
Temperature range, min.			234.15
Temperature range, max.			605.00
Pvap	2.73e-03	kPa	234.15	Calculated Property
Pvap	0.11	kPa	275.36	Calculated Property
Pvap	1.63	kPa	316.56	Calculated Property
Pvap	11.72	kPa	357.77	Calculated Property
Pvap	52.68	kPa	398.97	Calculated Property
Pvap	170.17	kPa	440.18	Calculated Property
Pvap	431.83	kPa	481.38	Calculated Property
Pvap	914.57	kPa	522.59	Calculated Property
Pvap	1686.49	kPa	563.79	Calculated Property
Pvap	2791.43	kPa	605.00	Calculated Property
Pvap	[10.79; 63.73]	kPa	[354.15; 404.15]	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			8.40676e+01
Coefficient B			-8.19745e+03
Coefficient C			-1.01131e+01
Coefficient D			6.53118e-06
Coefficient E			0.00000e+00
Temperature range, min.			354.15
Temperature range, max.			404.15
Pvap	10.79	kPa	354.15	Calculated Property
Pvap	13.53	kPa	359.71	Calculated Property
Pvap	16.83	kPa	365.26	Calculated Property
Pvap	20.76	kPa	370.82	Calculated Property
Pvap	25.44	kPa	376.37	Calculated Property
Pvap	30.95	kPa	381.93	Calculated Property
Pvap	37.41	kPa	387.48	Calculated Property
Pvap	44.94	kPa	393.04	Calculated Property
Pvap	53.67	kPa	398.59	Calculated Property
Pvap	63.73	kPa	404.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[865.55; 445.11]	kg/m3	[234.15; 587.00]	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			7.48417e+01
Coefficient B			2.69580e-01
Coefficient C			6.05000e+02
Coefficient D			2.90590e-01
Temperature range, min.			234.15
Temperature range, max.			587.00
ρl	865.55	kg/m3	234.15	Calculated Property
ρl	834.67	kg/m3	273.36	Calculated Property
ρl	802.33	kg/m3	312.56	Calculated Property
ρl	768.20	kg/m3	351.77	Calculated Property
ρl	731.79	kg/m3	390.97	Calculated Property
ρl	692.39	kg/m3	430.18	Calculated Property
ρl	648.81	kg/m3	469.38	Calculated Property
ρl	598.85	kg/m3	508.59	Calculated Property
ρl	537.44	kg/m3	547.79	Calculated Property
ρl	445.11	kg/m3	587.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 7.76e-04]	N/m	[234.15; 587.00]	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			-1.12180e-02
Coefficient B			4.89200e+01
Coefficient C			-3.26120e+00
Coefficient D			8.08360e-04
Coefficient E			-4.99170e-06
Temperature range, min.			234.15
Temperature range, max.			587.00
γ	0.03	N/m	234.15	Calculated Property
γ	0.03	N/m	273.36	Calculated Property
γ	0.02	N/m	312.56	Calculated Property
γ	0.02	N/m	351.77	Calculated Property
γ	0.02	N/m	390.97	Calculated Property
γ	0.01	N/m	430.18	Calculated Property
γ	0.01	N/m	469.38	Calculated Property
γ	0.01	N/m	508.59	Calculated Property
γ	0.00	N/m	547.79	Calculated Property
γ	7.76e-04	N/m	587.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.11]	W/m×K	[234.15; 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			1.20180e+03
Coefficient B			1.03980e+00
Coefficient C			1.41130e+10
Coefficient D			-9.61620e+10
Temperature range, min.			234.15
Temperature range, max.			1000.00
λgas	0.01	W/m×K	234.15	Calculated Property
λgas	0.01	W/m×K	319.24	Calculated Property
λgas	0.02	W/m×K	404.34	Calculated Property
λgas	0.03	W/m×K	489.43	Calculated Property
λgas	0.04	W/m×K	574.53	Calculated Property
λgas	0.05	W/m×K	659.62	Calculated Property
λgas	0.06	W/m×K	744.72	Calculated Property
λgas	0.08	W/m×K	829.81	Calculated Property
λgas	0.09	W/m×K	914.91	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.08]	W/m×K	[234.15; 553.15]	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			-2.57280e-02
Coefficient B			-6.18930e+01
Coefficient C			-9.78520e-01
Coefficient D			-2.16040e-03
Coefficient E			1.26830e-07
Temperature range, min.			234.15
Temperature range, max.			553.15
λliquid	0.15	W/m×K	234.15	Calculated Property
λliquid	0.14	W/m×K	269.59	Calculated Property
λliquid	0.13	W/m×K	305.04	Calculated Property
λliquid	0.13	W/m×K	340.48	Calculated Property
λliquid	0.12	W/m×K	375.93	Calculated Property
λliquid	0.11	W/m×K	411.37	Calculated Property
λliquid	0.10	W/m×K	446.82	Calculated Property
λliquid	0.09	W/m×K	482.26	Calculated Property
λliquid	0.09	W/m×K	517.71	Calculated Property
λliquid	0.08	W/m×K	553.15	Calculated Property

Similar Compounds

Find more compounds similar to 3-Heptanone.

Mixtures

• 3-Heptanone + Water
• 3-Heptanone + Phenol + Water
• 3-Heptanone + Octane
• 3-Heptanone + Nonane
• 3-Heptanone + Decane

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.
• Cheméo Relay (1.0)
• 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
• Crippen Method
• Measurements and correlation of liquid-liquid equilibrium data for the ternary (3-heptanone + phenol + water) system
• Experimental Determination and Modeling of Liquid-Liquid Equilibrium for Ternary Mixtures of Ethylene Glycol + 1,2-Butanediol + 3-Heptanone or Anisole
• Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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