Chemical Properties of Cyclohexanone (CAS 108-94-1)

InChI

InChI=1S/C6H10O/c7-6-4-2-1-3-5-6/h1-5H2

InChI Key

JHIVVAPYMSGYDF-UHFFFAOYSA-N

Formula

C6H10O

SMILES

O=C1CCCCC1

Molecular Weight¹

98.14

CAS

108-94-1

Other Names

• Anon
• Anone
• Cicloesanone
• Cyclohexanon
• Cyclohexyl ketone
• Cykloheksanon
• Hexanon
• Hytrol O
• Ketohexamethylene
• NCI-C55005
• NSC 5711
• Nadone
• Pimelic ketone
• Pimelin ketone
• Rcra waste number U057
• Sextone
• UN 1915

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower 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°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• 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.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (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	[0.1837; 0.4420]
ω	0.1837		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2990		ChemSep v8.3 pure component data Compiled value
ω	0.4420		KDB
PAff	841.00	kJ/mol	NIST
Tig	[693.15; 693.15]	K
Tig	693.15	K	KDB
Tig	693.15	K	NCMS SOLV-DB
BasG	811.20	kJ/mol	NIST
ΔcH°liquid	[-3536.00; -3499.00]	kJ/mol
ΔcH°liquid	-3517.60 ± 1.70	kJ/mol	NIST
ΔcH°liquid	-3536.00 ± 2.00	kJ/mol	NIST
ΔcH°liquid	-3518.90 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-3499.00 ± 0.80	kJ/mol	NIST
μ	[3.09; 3.10]	debye
μ	3.09	debye	ChemSep v8.3 pure component data Compiled value
μ	3.10	debye	KDB
η	0.0020200	Pa×s	Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
EA	0.00	eV	NIST
εr	16.10		NCMS SOLV-DB
LFL	1.10	% in Air	KDB
Tflash,cc	[317.15; 327.04]	K
Tflash,cc	327.04	K	KDB
Tflash,cc	317.15	K	NCMS SOLV-DB
Tflash,oc	317.04	K	KDB
ΔfG°	[-90.81; -90.28]	kJ/mol
ΔfG°	-90.28	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-90.81	kJ/mol	KDB
Rg	3.4100		KDB
ΔfH°gas	[-231.10; -225.70]	kJ/mol
ΔfH°gas	-226.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-230.30	kJ/mol	KDB
ΔfH°gas	-231.10 ± 0.88	kJ/mol	NIST
ΔfH°gas	-225.70	kJ/mol	NIST
ΔfH°gas	-227.70 ± 1.90	kJ/mol	NIST
ΔfH°gas	-226.30	kJ/mol	NIST
ΔfH°liquid	[-276.10; -254.00]	kJ/mol
ΔfH°liquid	-276.10 ± 0.84	kJ/mol	NIST
ΔfH°liquid	-272.60 ± 1.80	kJ/mol	NIST
ΔfH°liquid	-254.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-271.40	kJ/mol	NIST
ΔfusH°	1.57	kJ/mol	Joback Calculated Property
ΔvapH°	[39.80; 46.60]	kJ/mol
ΔvapH°	44.89	kJ/mol	NCMS SOLV-DB
ΔvapH°	45.09	kJ/mol	NIST
ΔvapH°	46.60 ± 0.40	kJ/mol	NIST
ΔvapH°	44.89 ± 0.63	kJ/mol	NIST
ΔvapH°	44.90 ± 0.60	kJ/mol	NIST
ΔvapH°	45.10 ± 0.10	kJ/mol	NIST
ΔvapH°	45.06	kJ/mol	NIST
ΔvapH°	Outlier 39.80	kJ/mol	NIST
IE	[9.14; 9.50]	eV
IE	9.16 ± 0.02	eV	NIST
IE	9.18	eV	NIST
IE	Outlier 9.50 ± 0.20	eV	NIST
IE	9.16 ± 0.01	eV	NIST
IE	9.14 ± 0.01	eV	NIST
IE	9.14 ± 0.03	eV	NIST
IE	9.29	eV	NIST
IE	9.18	eV	NIST
IE	9.28	eV	NIST
IE	9.14 ± 0.02	eV	NIST
log10WS	[-0.60; -0.60]
log10WS	-0.60		Aq. Solubility Prediction
log10WS	-0.60		Estimated Solubility
logPoct/wat	0.810		NCMS SOLV-DB
McVol	86.110	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=2); %!d(float64=2)]
NFPA Fire	2		KDB
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[3850.35; 4600.00]	kPa
Pc	4600.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3850.35	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4000.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4000.00	kPa	KDB
Pc	4600.00 ± 100.00	kPa	NIST
Pc	4000.00 ± 50.00	kPa	NIST
Pc	3850.35 ± 202.65	kPa	NIST
Ptriple	6.80e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[139.80; 903.00]
Inp	896.00		NIST
Inp	854.10		NIST
Inp	881.00		NIST
Inp	883.00		NIST
Inp	874.00		NIST
Inp	877.00		NIST
Inp	853.90		NIST
Inp	861.00		NIST
Inp	857.00		NIST
Inp	895.00		NIST
Inp	883.00		NIST
Inp	851.00		NIST
Inp	884.00		NIST
Inp	886.00		NIST
Inp	855.10		NIST
Inp	888.00		NIST
Inp	867.00		NIST
Inp	886.00		NIST
Inp	869.00		NIST
Inp	872.00		NIST
Inp	874.00		NIST
Inp	875.00		NIST
Inp	895.00		NIST
Inp	851.70		NIST
Inp	896.80		NIST
Inp	894.00		NIST
Inp	894.00		NIST
Inp	891.00		NIST
Inp	881.00		NIST
Inp	896.00		NIST
Inp	881.00		NIST
Inp	876.00		NIST
Inp	866.00		NIST
Inp	871.00		NIST
Inp	874.00		NIST
Inp	882.00		NIST
Inp	890.00		NIST
Inp	867.00		NIST
Inp	879.00		NIST
Inp	862.00		NIST
Inp	864.00		NIST
Inp	865.00		NIST
Inp	866.00		NIST
Inp	860.00		NIST
Inp	894.00		NIST
Inp	896.00		NIST
Inp	897.00		NIST
Inp	864.00		NIST
Inp	903.00		NIST
Inp	854.00		NIST
Inp	858.00		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	858.00		NIST
Inp	894.00		NIST
Inp	854.00		NIST
Inp	858.00		NIST
Inp	875.00		NIST
Inp	894.00		NIST
Inp	895.00		NIST
Inp	871.00		NIST
Inp	875.00		NIST
Inp	898.00		NIST
Inp	878.00		NIST
Inp	862.00		NIST
Inp	878.00		NIST
Inp	875.00		NIST
Inp	857.00		NIST
Inp	875.00		NIST
Inp	900.00		NIST
Inp	855.00		NIST
Inp	Outlier 139.80		NIST
Inp	895.00		NIST
Inp	891.00		NIST
Inp	869.00		NIST
Inp	Outlier 139.80		NIST
Inp	854.10		NIST
Inp	853.90		NIST
Inp	851.00		NIST
Inp	867.00		NIST
Ip	[1273.00; 1333.00]
Ip	1281.00		NIST
Ip	1273.00		NIST
Ip	1301.00		NIST
Ip	1310.00		NIST
Ip	1287.00		NIST
Ip	1282.00		NIST
Ip	1280.00		NIST
Ip	1281.00		NIST
Ip	1291.00		NIST
Ip	1291.00		NIST
Ip	1275.00		NIST
Ip	1311.00		NIST
Ip	1280.00		NIST
Ip	1280.00		NIST
Ip	1315.00		NIST
Ip	1314.00		NIST
Ip	1314.00		NIST
Ip	1291.00		NIST
Ip	1296.00		NIST
Ip	Outlier 1333.00		NIST
Ip	1282.00		NIST
Ip	1302.00		NIST
Ip	1281.00		NIST
Ip	1281.00		NIST
Ip	1320.00		NIST
Ip	1285.00		NIST
Ip	1299.00		NIST
Ip	1273.00		NIST
Ip	1285.00		NIST
Ip	1311.00		NIST
Ip	1314.00		NIST
Ip	1306.00		NIST
Ip	1306.00		NIST
Ip	1289.00		NIST
Ip	1306.00		NIST
Ip	1275.00		NIST
Ip	1282.00		NIST
Ip	1301.00		NIST
Ip	1302.00		NIST
Ip	1291.00		NIST
Ip	1280.00		NIST
Ip	1296.00		NIST
Ip	1285.00		NIST
Ip	1289.00		NIST
S°gas	335.53	J/mol×K	NIST
S°liquid	229.03	J/mol×K	NIST
Tboil	[383.05; 429.90]	K
Tboil	428.69	K	(Liquid + liquid) equilibria of (water + propionic acid + cyclohexanone) at several temperatures
Tboil	428.84	K	Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
Tboil	428.57	K	Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
Tboil	428.58	K	ChemSep v8.3 pure component data Compiled value
Tboil	428.58	K	KDB
Tboil	428.80	K	NCMS SOLV-DB
Tboil	Outlier 383.05 ± 0.15	K	NIST
Tboil	428.70	K	NIST
Tboil	428.70 ± 0.30	K	NIST
Tboil	428.70 ± 0.50	K	NIST
Tboil	428.55 ± 0.50	K	NIST
Tboil	428.75 ± 0.40	K	NIST
Tboil	428.40 ± 0.50	K	NIST
Tboil	428.15 ± 1.50	K	NIST
Tboil	428.70 ± 0.40	K	NIST
Tboil	428.75 ± 0.50	K	NIST
Tboil	429.15 ± 1.50	K	NIST
Tboil	428.90 ± 0.50	K	NIST
Tboil	426.65 ± 0.50	K	NIST
Tboil	428.80 ± 0.20	K	NIST
Tboil	428.80 ± 0.50	K	NIST
Tboil	427.00 ± 3.00	K	NIST
Tboil	429.90 ± 2.00	K	NIST
Tboil	426.00 ± 10.00	K	NIST
Tboil	424.00 ± 4.00	K	NIST
Tboil	428.15 ± 2.00	K	NIST
Tboil	428.60 ± 2.00	K	NIST
Tboil	429.00 ± 5.00	K	NIST
Tboil	426.15 ± 3.00	K	NIST
Tc	[629.15; 665.50]	K
Tc	665.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	665.50	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	653.00	K	ChemSep v8.3 pure component data Compiled value
Tc	653.00	K	KDB
Tc	664.30 ± 3.00	K	NIST
Tc	653.00 ± 3.00	K	NIST
Tc	Outlier 629.15 ± 1.50	K	NIST
Tfus	[233.00; 256.75]	K
Tfus	245.90	K	Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
Tfus	243.12	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	242.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	242.00	K	KDB
Tfus	241.05	K	NCMS SOLV-DB
Tfus	242.45 ± 1.00	K	NIST
Tfus	241.05 ± 0.50	K	NIST
Tfus	244.85 ± 0.30	K	NIST
Tfus	241.95 ± 0.60	K	NIST
Tfus	241.20 ± 0.40	K	NIST
Tfus	233.00 ± 5.00	K	NIST
Tfus	241.80 ± 0.60	K	NIST
Tfus	Outlier 256.75 ± 0.50	K	NIST
Ttriple	[242.00; 245.21]	K
Ttriple	242.00	K	ChemSep v8.3 pure component data Compiled value
Ttriple	245.21 ± 0.01	K	NIST
Ttriple	242.40 ± 0.50	K	NIST
Ttriple	245.21 ± 0.01	K	NIST
UQi	3.11		ChemSep v8.3 pure component data Compiled value
URi	4.07		ChemSep v8.3 pure component data Compiled value
Vc	[0.311; 0.312]	m3/kmol
Vc	0.312	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.311	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2290000		ChemSep v8.3 pure component data Compiled value
Zra	[0.25; 0.25]
Zra	0.25		ChemSep v8.3 pure component data Compiled value
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[155.20; 190.18]	J/mol×K	[385.00; 480.00]
Cp,gas	155.20	J/mol×K	385.00	NIST
Cp,gas	161.07	J/mol×K	400.00	NIST
Cp,gas	168.98	J/mol×K	420.00	NIST
Cp,gas	175.81	J/mol×K	440.00	NIST
Cp,gas	183.65	J/mol×K	460.00	NIST
Cp,gas	190.18	J/mol×K	480.00	NIST
Cp,liquid	[177.20; 200.40]	J/mol×K	[290.00; 304.20]
Cp,liquid	177.80	J/mol×K	290.00	NIST
Cp,liquid	177.20	J/mol×K	300.00	NIST
Cp,liquid	200.40	J/mol×K	304.20	NIST
η	[0.0013730; 0.0025990]	Pa×s	[288.15; 318.15]
η	0.0025990	Pa×s	288.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0023318	Pa×s	293.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0019740	Pa×s	298.15	Excess Molar Volumes and Viscosities for Binary Mixtures of Cyclohexanone with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
η	0.0021016	Pa×s	298.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0024530	Pa×s	298.15	NCMS SOLV-DB
η	0.0020190	Pa×s	298.15	Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η	0.0020570	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0020212	Pa×s	298.15	Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
η	0.0018160	Pa×s	303.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
η	0.0019045	Pa×s	303.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0018057	Pa×s	303.15	Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
η	0.0018470	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0018170	Pa×s	303.15	Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η	0.0017338	Pa×s	308.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0016320	Pa×s	308.15	Excess Molar Volumes and Viscosities for Binary Mixtures of Cyclohexanone with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
η	0.0016570	Pa×s	308.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
η	0.0016310	Pa×s	308.15	Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η	0.0015849	Pa×s	308.15	Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
η	0.0016940	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0015842	Pa×s	313.15	Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η	0.0015460	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0015420	Pa×s	313.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
η	0.0014760	Pa×s	313.15	Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
η	0.0013730	Pa×s	318.15	Excess Molar Volumes and Viscosities for Binary Mixtures of Cyclohexanone with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
εr	[14.89; 19.75]		[243.15; 313.15]
εr	19.75		243.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	19.54		245.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	19.34		248.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	19.13		250.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	18.93		253.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	18.73		255.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	18.54		258.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	18.34		260.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	18.15		263.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	17.96		265.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	17.78		268.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	17.60		270.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	17.42		273.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	17.24		275.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	17.07		278.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	16.90		280.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	16.73		283.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	16.56		285.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	16.40		288.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	16.24		290.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	16.08		293.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	15.92		295.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	15.81		298.15	Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
εr	15.77		298.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	15.62		300.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	15.46		303.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	15.32		305.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	15.17		308.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	15.03		310.65	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
εr	14.89		313.15	Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
ΔfusH	[1.25; 8.66]	kJ/mol	[220.80; 245.20]
ΔfusH	8.66	kJ/mol	220.80	NIST
ΔfusH	8.66	kJ/mol	220.80	NIST
ΔfusH	8.51	kJ/mol	221.00	NIST
ΔfusH	1.25	kJ/mol	242.60	NIST
ΔfusH	1.33	kJ/mol	245.20	NIST
ΔfusH	1.33	kJ/mol	245.20	NIST
ΔfusH	1.33	kJ/mol	245.20	NIST
ΔsubH	49.30	kJ/mol	254.00	NIST
ΔvapH	[39.75; 45.13]	kJ/mol	[285.50; 428.80]
ΔvapH	40.30	kJ/mol	285.50	NIST
ΔvapH	44.40 ± 0.10	kJ/mol	308.00	NIST
ΔvapH	44.00 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	43.40 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	43.10 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	42.20 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	41.80 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	41.40 ± 0.10	kJ/mol	348.00	NIST
ΔvapH	44.00	kJ/mol	373.00	NIST
ΔvapH	43.10	kJ/mol	385.00	NIST
ΔvapH	41.50	kJ/mol	400.50	NIST
ΔvapH	42.20	kJ/mol	401.50	NIST
ΔvapH	40.40	kJ/mol	410.50	NIST
ΔvapH	39.75	kJ/mol	428.20	KDB
ΔvapH	45.13	kJ/mol	428.80	NIST
Pvap	[0.58; 101.30]	kPa	[298.15; 428.57]
Pvap	0.64	kPa	298.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	0.58	kPa	298.15	NCMS SOLV-DB
Pvap	1.16	kPa	308.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	1.92	kPa	318.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	95.30	kPa	426.25	Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
Pvap	99.00	kPa	428.01	Vapor-Liquid Equilibria of Cyclohexanone + 2-Cyclohexen-1-one and Cyclohexanol + 2-Cyclohexen-1-one, Validated in a Packed Column Distillation.
Pvap	101.30	kPa	428.57	Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
n0	[1.44400; 1.45100]		[293.10; 308.15]
n0	1.45070		293.10	Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
n0	1.45100		293.15	Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
n0	1.45070		293.15	Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
n0	1.45010		298.15	Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
n0	1.44820		298.15	Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
n0	1.44810		298.15	Isothermal (vapour + liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15) K
n0	1.45100		298.15	Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
n0	1.44860		298.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
n0	1.44980		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
n0	1.45000		298.15	NCMS SOLV-DB
n0	1.45030		298.20	Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
n0	1.44610		303.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
n0	1.44400		308.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
ρl	[920.70; 951.69]	kg/m3	[288.00; 323.15]
ρl	951.00	kg/m3	288.00	KDB
ρl	951.69	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	951.18	kg/m3	288.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	947.60	kg/m3	293.10	Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
ρl	947.38	kg/m3	293.15	Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl	946.71	kg/m3	293.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	948.80	kg/m3	293.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	942.24	kg/m3	298.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	942.92	kg/m3	298.15	Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl	942.76	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	941.10	kg/m3	298.15	Isobaric Vapor-Liquid Phase Equilibrium Measurements, Correlation, and Prediction for Separation of the Mixtures of Cyclohexanone and Alcohols
ρl	943.10	kg/m3	298.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	942.20	kg/m3	298.15	Excess molar enthalpies for binary mixtures of cyclopentanone, cyclohexanone, or cycloheptanone with n-nonane at T = 298.15 K and atmospheric pressure
ρl	937.77	kg/m3	303.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	937.55	kg/m3	303.15	Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
ρl	938.07	kg/m3	303.15	Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl	938.20	kg/m3	303.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	933.28	kg/m3	308.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	933.50	kg/m3	308.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	933.19	kg/m3	308.15	Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl	933.80	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	928.80	kg/m3	313.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	928.79	kg/m3	313.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	924.40	kg/m3	318.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	924.82	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	920.70	kg/m3	323.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ΔfusS	[5.20; 39.22]	J/mol×K	[220.80; 245.20]
ΔfusS	39.22	J/mol×K	220.80	NIST
ΔfusS	39.22	J/mol×K	220.80	NIST
ΔfusS	38.50	J/mol×K	221.00	NIST
ΔfusS	5.20	J/mol×K	242.60	NIST
ΔfusS	5.42	J/mol×K	245.20	NIST
γ	0.04	N/m	298.15	NCMS SOLV-DB

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	320.20	K	2.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[77.75; 347.64]	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			6.39310e+01
Coefficient B			-7.72150e+02
Coefficient C			6.56024e+00
Coefficient D			-3.80980e-04
Coefficient E			7.73060e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	77.75	J/mol×K	200.00	Calculated Property
Cp,gas	130.38	J/mol×K	344.44	Calculated Property
Cp,gas	187.04	J/mol×K	488.89	Calculated Property
Cp,gas	233.08	J/mol×K	633.33	Calculated Property
Cp,gas	267.89	J/mol×K	777.78	Calculated Property
Cp,gas	293.77	J/mol×K	922.22	Calculated Property
Cp,gas	313.05	J/mol×K	1066.67	Calculated Property
Cp,gas	327.59	J/mol×K	1211.11	Calculated Property
Cp,gas	338.78	J/mol×K	1355.56	Calculated Property
Cp,gas	347.64	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[147.91; 298.45]	J/mol×K	[250.90; 489.75]	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			1.79870e+01
Coefficient B			-7.25390e+01
Coefficient C			3.88624e+00
Coefficient D			6.30560e-03
Coefficient E			-4.96070e-06
Temperature range, min.			250.90
Temperature range, max.			489.75
Cp,liquid	147.91	J/mol×K	250.90	Calculated Property
Cp,liquid	165.27	J/mol×K	277.44	Calculated Property
Cp,liquid	182.99	J/mol×K	303.98	Calculated Property
Cp,liquid	200.89	J/mol×K	330.52	Calculated Property
Cp,liquid	218.75	J/mol×K	357.06	Calculated Property
Cp,liquid	236.31	J/mol×K	383.59	Calculated Property
Cp,liquid	253.34	J/mol×K	410.13	Calculated Property
Cp,liquid	269.55	J/mol×K	436.67	Calculated Property
Cp,liquid	284.67	J/mol×K	463.21	Calculated Property
Cp,liquid	298.45	J/mol×K	489.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0089640; 0.0004457]	Pa×s	[242.00; 428.58]	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			-3.78770e+01
Coefficient B			3.01280e+03
Coefficient C			3.75010e+00
Coefficient D			2.19940e-06
Coefficient E			2.00000e+00
Temperature range, min.			242.00
Temperature range, max.			428.58
η	0.0089640	Pa×s	242.00	Calculated Property
η	0.0046744	Pa×s	262.73	Calculated Property
η	0.0027543	Pa×s	283.46	Calculated Property
η	0.0017866	Pa×s	304.19	Calculated Property
η	0.0012515	Pa×s	324.92	Calculated Property
η	0.0009331	Pa×s	345.66	Calculated Property
η	0.0007323	Pa×s	366.39	Calculated Property
η	0.0005998	Pa×s	387.12	Calculated Property
η	0.0005092	Pa×s	407.85	Calculated Property
η	0.0004457	Pa×s	428.58	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[48.29; 15.89]	kJ/mol	[242.00; 631.37]	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			6.76300e+01
Coefficient B			1.06660e+00
Coefficient C			-1.06470e+00
Coefficient D			3.96330e-01
Coefficient E			1.92580e-02
Critical temperature, Tc (K)			6.53000e+02
Temperature range, min.			242.00
Temperature range, max.			631.37
ΔvapH	48.29	kJ/mol	242.00	Calculated Property
ΔvapH	45.80	kJ/mol	285.26	Calculated Property
ΔvapH	43.42	kJ/mol	328.53	Calculated Property
ΔvapH	41.06	kJ/mol	371.79	Calculated Property
ΔvapH	38.62	kJ/mol	415.05	Calculated Property
ΔvapH	35.99	kJ/mol	458.32	Calculated Property
ΔvapH	32.98	kJ/mol	501.58	Calculated Property
ΔvapH	29.29	kJ/mol	544.84	Calculated Property
ΔvapH	24.30	kJ/mol	588.11	Calculated Property
ΔvapH	15.89	kJ/mol	631.37	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[315.32; 454.86]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.55797e+01
Coefficient B			-4.36137e+03
Coefficient C			-3.01140e+01
Temperature range, min.			315.32
Temperature range, max.			454.86
Pvap	1.33	kPa	315.32	Calculated Property
Pvap	2.93	kPa	330.82	Calculated Property
Pvap	5.97	kPa	346.33	Calculated Property
Pvap	11.38	kPa	361.83	Calculated Property
Pvap	20.47	kPa	377.34	Calculated Property
Pvap	35.02	kPa	392.84	Calculated Property
Pvap	57.33	kPa	408.35	Calculated Property
Pvap	90.27	kPa	423.85	Calculated Property
Pvap	137.34	kPa	439.36	Calculated Property
Pvap	202.66	kPa	454.86	Calculated Property
Pvap	[6.70e-03; 4000.00]	kPa	[241.45; 641.45]	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			6.30311e+01
Coefficient B			-7.28053e+03
Coefficient C			-6.94311e+00
Coefficient D			3.62465e-06
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 653 K.
Temperature range, min.			241.45
Temperature range, max.			641.45
Pvap	6.70e-03	kPa	241.45	Calculated Property
Pvap	0.25	kPa	285.89	Calculated Property
Pvap	3.05	kPa	330.34	Calculated Property
Pvap	19.43	kPa	374.78	Calculated Property
Pvap	79.54	kPa	419.23	Calculated Property
Pvap	240.70	kPa	463.67	Calculated Property
Pvap	588.76	kPa	508.12	Calculated Property
Pvap	1235.43	kPa	552.56	Calculated Property
Pvap	2317.22	kPa	597.01	Calculated Property
Pvap	4000.00	kPa	641.45	Calculated Property
Pvap	[7.24e-03; 4053.12]	kPa	[242.00; 629.15]	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			1.05154e+02
Coefficient B			-8.84188e+03
Coefficient C			-1.35148e+01
Coefficient D			1.08668e-05
Coefficient E			0.00000e+00
Temperature range, min.			242.00
Temperature range, max.			629.15
Pvap	7.24e-03	kPa	242.00	Calculated Property
Pvap	0.25	kPa	285.02	Calculated Property
Pvap	2.93	kPa	328.03	Calculated Property
Pvap	17.51	kPa	371.05	Calculated Property
Pvap	68.22	kPa	414.07	Calculated Property
Pvap	201.10	kPa	457.08	Calculated Property
Pvap	492.54	kPa	500.10	Calculated Property
Pvap	1066.76	kPa	543.12	Calculated Property
Pvap	2132.17	kPa	586.13	Calculated Property
Pvap	4053.12	kPa	629.15	Calculated Property
Pvap	[12.72; 131.43]	kPa	[362.78; 438.92]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40534e+01
Coefficient B			-3.44354e+03
Coefficient C			-6.35980e+01
Reference			Meyer and Hotz, 1973
Comment			NIST log10(P/bar) coefficients: A=4.1033 ± 0.00099, B=1495.51 ± 0.67, C=-63.598 ± 0.075
Temperature range, min.			362.78
Temperature range, max.			438.92
Pvap	12.72	kPa	362.78	Calculated Property
Pvap	17.46	kPa	371.24	Calculated Property
Pvap	23.56	kPa	379.70	Calculated Property
Pvap	31.30	kPa	388.16	Calculated Property
Pvap	40.98	kPa	396.62	Calculated Property
Pvap	52.95	kPa	405.08	Calculated Property
Pvap	67.56	kPa	413.54	Calculated Property
Pvap	85.23	kPa	422.00	Calculated Property
Pvap	106.37	kPa	430.46	Calculated Property
Pvap	131.43	kPa	438.92	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[989.79; 506.68]	kg/m3	[242.00; 631.37]	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			8.44128e+01
Coefficient B			2.68290e-01
Coefficient C			6.53000e+02
Coefficient D			2.98080e-01
Temperature range, min.			242.00
Temperature range, max.			631.37
ρl	989.79	kg/m3	242.00	Calculated Property
ρl	953.48	kg/m3	285.26	Calculated Property
ρl	915.54	kg/m3	328.53	Calculated Property
ρl	875.60	kg/m3	371.79	Calculated Property
ρl	833.13	kg/m3	415.05	Calculated Property
ρl	787.33	kg/m3	458.32	Calculated Property
ρl	736.90	kg/m3	501.58	Calculated Property
ρl	679.42	kg/m3	544.84	Calculated Property
ρl	609.42	kg/m3	588.11	Calculated Property
ρl	506.68	kg/m3	631.37	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[242.15; 428.85]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			7.15952e-02
Coefficient B			-1.24200e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			242.15
Temperature range, max.			428.85
γ	0.04	N/m	242.15	Calculated Property
γ	0.04	N/m	262.89	Calculated Property
γ	0.04	N/m	283.64	Calculated Property
γ	0.03	N/m	304.38	Calculated Property
γ	0.03	N/m	325.13	Calculated Property
γ	0.03	N/m	345.87	Calculated Property
γ	0.03	N/m	366.62	Calculated Property
γ	0.02	N/m	387.36	Calculated Property
γ	0.02	N/m	408.11	Calculated Property
γ	0.02	N/m	428.85	Calculated Property
γ	[0.04; 8.97e-04]	N/m	[242.00; 631.37]	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			-1.16990e-02
Coefficient B			6.71230e+01
Coefficient C			-3.17130e+00
Coefficient D			1.01740e-03
Coefficient E			-4.89610e-06
Temperature range, min.			242.00
Temperature range, max.			631.37
γ	0.04	N/m	242.00	Calculated Property
γ	0.04	N/m	285.26	Calculated Property
γ	0.03	N/m	328.53	Calculated Property
γ	0.03	N/m	371.79	Calculated Property
γ	0.02	N/m	415.05	Calculated Property
γ	0.02	N/m	458.32	Calculated Property
γ	0.01	N/m	501.58	Calculated Property
γ	0.01	N/m	544.84	Calculated Property
γ	0.00	N/m	588.11	Calculated Property
γ	8.97e-04	N/m	631.37	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.13]	W/m×K	[242.00; 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			-1.10490e+03
Coefficient B			-1.83960e-02
Coefficient C			4.79160e+05
Coefficient D			-8.13920e+09
Temperature range, min.			242.00
Temperature range, max.			1000.00
λgas	0.01	W/m×K	242.00	Calculated Property
λgas	0.01	W/m×K	326.22	Calculated Property
λgas	0.02	W/m×K	410.44	Calculated Property
λgas	0.03	W/m×K	494.67	Calculated Property
λgas	0.04	W/m×K	578.89	Calculated Property
λgas	0.06	W/m×K	663.11	Calculated Property
λgas	0.07	W/m×K	747.33	Calculated Property
λgas	0.09	W/m×K	831.56	Calculated Property
λgas	0.11	W/m×K	915.78	Calculated Property
λgas	0.13	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.12]	W/m×K	[242.00; 428.58]	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			1.15070e-01
Coefficient B			-8.53650e+02
Coefficient C			4.79460e+00
Coefficient D			-2.17220e-02
Coefficient E			9.19540e-06
Temperature range, min.			242.00
Temperature range, max.			428.58
λliquid	0.15	W/m×K	242.00	Calculated Property
λliquid	0.14	W/m×K	262.73	Calculated Property
λliquid	0.14	W/m×K	283.46	Calculated Property
λliquid	0.14	W/m×K	304.19	Calculated Property
λliquid	0.13	W/m×K	324.92	Calculated Property
λliquid	0.13	W/m×K	345.66	Calculated Property
λliquid	0.13	W/m×K	366.39	Calculated Property
λliquid	0.13	W/m×K	387.12	Calculated Property
λliquid	0.12	W/m×K	407.85	Calculated Property
λliquid	0.12	W/m×K	428.58	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexanone.

Mixtures

• Cyclohexanone + Water
• Pentanoic acid, 4-oxo- + Cyclohexanone + Water
• Cyclohexanone + Cyclohexane + Water
• Hexanedioic acid + Cyclohexanone
• Cyclohexanone + Phenol + Water
• Benzene + Cyclohexanone
• Toluene + Cyclohexanone
• Benzene, ethyl- + Cyclohexanone
• Styrene + Cyclohexanone
• Cyclohexanone + Propanoic acid + Water
• 2-Propenenitrile + Cyclohexanone
• Cyclohexanone + Carbon Tetrachloride
• Cyclohexanone + Cyanopyrazine
• Cyclohexanone + Cyclohexane
• Pyrazine, methyl- + Cyclohexanone
• Decane + Cyclohexanone
• Cyclohexanone + Ethene-1,1-diamine, 2,2-dinitro-
• Hexanedioic acid + Cyclohexanone + Cyclohexane
• Cyclohexanol + Hexanedioic acid + Cyclohexanone
• Cyclohexanone + o-Xylene

Find more mixtures with Cyclohexanone.

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.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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.
• Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
• Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
• Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Measurement on the solubility of adipic acid in various solvents at high temperature and its thermodynamics parameters.
• Liquid-liquid equilibria for ternary system water + acetic acid+ cyclohexanone at (293.2 to 323.2) K
• Distribution of cyclohexanol and cyclohexanone between water and cyclohexane
• Solubilities of adipic acid in binary cyclohexanone + cyclohexanol, cyclohexane + cyclohexanol, and cyclohexane + cyclohexanone solvent mixtures
• Solubility of 1,1-diamino-2,2-dinitroethylene in different pure solvents and binary mixtures (dimethyl sulfoxide p water) and (N,N-dimethylformamide p water) at different temperatures
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
• Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
• Phase equilibria for ternary liquid systems of (water + levulinic acid + cyclic solvent) at T = 298.2 K: Thermodynamic modeling
• (Liquid + liquid) equilibria of (water + propionic acid + cyclohexanone) at several temperatures
• Isothermal (vapour + liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15) K
• 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
• (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
• Partial molar volumes of organic solutes in water. XXIII. Cyclic ketones at T = (298 to 573) K and pressures up to 30 MPa
• Measurement and correlation of phase equilibrium data of the mixtures consisting of butyric acid, water, cyclohexanone at different temperatures
• Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Excess molar enthalpies for binary mixtures of cyclopentanone, cyclohexanone, or cycloheptanone with n-nonane at T = 298.15 K and atmospheric pressure
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Thermodynamic properties of ternary mixtures containing 1-ethyl-3-methylimidazolium tetrafluoroborate with cyclic amides and cyclopentanone or cyclohexanone at T = (293.15, 298.15, 303.15 and 308.15) K
• Excess molar volumes and excess isentropic compressibilities of ternary mixtures containing ionic liquids and cyclic alkanone
• Excess molar volumes and excess isentropic compressibilities of mixtures containing lactam, cyclic ethers and cyclic alkanones
• Enthalpic interactions between some amino acids and cyclohexanone in aqueous solutions at 298.15K
• Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
• Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures
• Measurement and Correlation for Solubilities of Adipic Acid in Acetic Acid + e-Caprolactone Mixtures and Cyclohexanone + e-Caprolactone Mixtures
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Determination and Correlation for the Solubility of Glutaric Acid in Cyclohexane + Cyclohexanol + Cyclohexanone Solvent Mixtures
• Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
• Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
• Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid and Succinic Acid in Acetic Acid + Cyclohexanone Mixtures
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Cyclohexanone + Benzene, Cyclohexanone + Toluene, and Cyclohexanone + p-Xylene at 101.3 kPa
• Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid, and Succinic Acid in Dimethyl Adipate + Methanol Mixtures
• Experimental Determination and Correlation of Liquid Liquid Equilibria for Water + Cyclohexanone + Solvents (Toluene or p-Xylene) Ternary Systems at 303.15 and 323.15 K under 101.3 kPa
• Measurement and Correlation for the Solubility of Adipic Acid and Succinic Acid in Glutaric Acid + Cyclohexanone and Glutaric Acid + Acetic Acid Mixtures
• Liquid-Liquid Equilibrium in the Ternary Systems Water + Cyclohexanone + Benzene or Methyl Isobutyl Carbinol at 303.15 and 323.15 K: Experimental Data and Correlation
• Measurement and Correlation for Solubilities of Succinic Acid and Glutaric Acid in e-Caprolactone + Acetic Acid Mixtures and e-Caprolactone + Cyclohexanone Mixtures
• Measurement and Correlation of Ternary (Liquid + Liquid) Equilibria for Separation of Cyclohexanone from Water via Isophorone or Mesityl Oxide
• Determination and Correlation for the Solubilities of Succinic Acid in Cyclohexanol + Cyclohexanone + Cyclohexane Solvent Mixtures
• Isobaric Vapor-Liquid Phase Equilibrium Measurements, Correlation, and Prediction for Separation of the Mixtures of Cyclohexanone and Alcohols
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
• Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
• Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
• Thermodynamics of mixtures involving some linear or cyclic ketones and cyclic ethers. 2. Systems containing tetrahydropyran
• Thermodynamics of Mixtures Involving Some Linear or Cyclic Ketones and Cyclic Ethers. 3. Systems Containing 1,4-Dioxane
• Thermodynamics of Mixtures Involving Some Linear or Cyclic Ketones and Cyclic Ethers. 4. Systems Containing 1,3-Dioxolane
• Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
• Thermodynamic Properties for 2-(1'-Hydroxycyclohexyl)cyclohexanone and Equilibrium of Dimerization of Cyclohexanone
• Excess Molar Volumes and Viscosities for Binary Mixtures of Cyclohexanone with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
• Vapor-Liquid Equilibrium Measurements and Modeling for Cyclohexane + Cyclohexanone
• Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
• Partial Molar Volumes of Cyclic Ketones at Infinite Dilution in Water at Temperatures T = (278 to 373) K and Low Pressure
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
• Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Different Organic Solvents
• Gas Solubility in Binary Liquid Mixtures: Carbon Dioxide in Cyclohexane + Cyclohexanone
• Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
• Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
• Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
• Solubility of 6-Chloropyridazin-3-amine in Different Solvents
• Measurements and Correlation of Liquid Liquid Equilibria for the Ternary System Water + Cyclohexanol + Cyclohexanone
• Vapor-Liquid Equilibria of Cyclohexanone + 2-Cyclohexen-1-one and Cyclohexanol + 2-Cyclohexen-1-one, Validated in a Packed Column Distillation.
• Solid-Liquid Equilibrium and Activity Coefficients for Caprolactam + 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide and Cyclohexanone Oxime + 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide
• Solubility of Cyclotrimethylenetrinitramine (RDX) in Binary Solvent Mixtures
• Phase Behavior of the Reactant and Products of Cyclohexane Oxidation in Compressed CO2
• Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
• Solubilities of Terephthalic Acid, Phthalic Acid, and Isophthalic Acid in Tetrahydrofuran, Cyclohexanone, 1,2-Diethoxyethane, and Acetophenone
• Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
• (Liquid + Liquid) Equilibria of (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanone) and (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanol) at T = 303.2 K
• Solubility of 1,1'-(Ethane-1,2-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents
• Solubilities of 1,1?-(Propane-1,3-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Different Solvents
• Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Water, Acetophenone, Cyclohexanone, Acetylacetone, and 2-Butanone
• Solubility of Anthracene in Binary and Ternary Mixtures of Cyclohexanone, Ethyl Acetate, and Methanol at 298.2 K
• Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents from (288.15 to 333.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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