Chemical Properties of Cyclopentanone (CAS 120-92-3)

InChI

InChI=1S/C5H8O/c6-5-3-1-2-4-5/h1-4H2

InChI Key

BGTOWKSIORTVQH-UHFFFAOYSA-N

Formula

C5H8O

SMILES

O=C1CCCC1

Molecular Weight¹

84.12

CAS

120-92-3

Other Names

• Adipic ketone
• Adipinketon
• Dumasin
• Ketocyclopentane
• Ketopentamethylene
• NSC 4122
• UN 2245

• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• ε_r : Dielectric Constant (Relative permittivity).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_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).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2730; 0.3500]
ω	0.2730		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3500		KDB
PAff	[823.70; 828.00]	kJ/mol
PAff	823.70	kJ/mol	NIST
PAff	828.00 ± 4.00	kJ/mol	NIST
BasG	794.00	kJ/mol	NIST
ΔcH°liquid	[-2874.00; -2870.00]	kJ/mol
ΔcH°liquid	-2873.50 ± 1.60	kJ/mol	NIST
ΔcH°liquid	-2874.00 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-2870.00 ± 0.80	kJ/mol	NIST
μ	3.00	debye	KDB
EA	0.00	eV	NIST
ΔfG°	-87.11	kJ/mol	Joback Calculated Property
ΔfH°gas	[-197.40; -192.80]	kJ/mol
ΔfH°gas	-192.80	kJ/mol	KDB
ΔfH°gas	-197.40 ± 1.30	kJ/mol	NIST
ΔfH°gas	-194.80 ± 1.70	kJ/mol	NIST
ΔfH°gas	-193.00 ± 1.80	kJ/mol	NIST
ΔfH°liquid	[-240.20; -236.50]	kJ/mol
ΔfH°liquid	-240.20 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-237.40 ± 1.70	kJ/mol	NIST
ΔfH°liquid	-236.50	kJ/mol	NIST
ΔfusH°	1.08	kJ/mol	Joback Calculated Property
ΔvapH°	[42.10; 42.77]	kJ/mol
ΔvapH°	42.77	kJ/mol	NIST
ΔvapH°	Outlier 42.10 ± 0.20	kJ/mol	NIST
ΔvapH°	42.63 ± 0.42	kJ/mol	NIST
ΔvapH°	42.60 ± 0.40	kJ/mol	NIST
ΔvapH°	42.70 ± 0.10	kJ/mol	NIST
ΔvapH°	42.72	kJ/mol	NIST
IE	[9.10; 9.42]	eV
IE	9.26 ± 0.01	eV	NIST
IE	9.28 ± 0.01	eV	NIST
IE	9.25 ± 0.02	eV	NIST
IE	9.26 ± 0.01	eV	NIST
IE	Outlier 9.42 ± 0.03	eV	NIST
IE	9.30	eV	NIST
IE	Outlier 9.10	eV	NIST
IE	9.28	eV	NIST
IE	9.28	eV	NIST
IE	9.25 ± 0.02	eV	NIST
log10WS	-0.11		Relay (1.0) Calculated Property
logPoct/wat	1.129		Crippen Calculated Property
McVol	72.020	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	[4600.00; 4600.00]	kPa
Pc	4600.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	4600.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4600.00	kPa	KDB
Pc	4600.00 ± 50.00	kPa	NIST
Inp	[116.00; 811.00]
Inp	741.10		NIST
Inp	740.90		NIST
Inp	744.00		NIST
Inp	770.00		NIST
Inp	780.00		NIST
Inp	766.00		NIST
Inp	734.00		NIST
Inp	766.00		NIST
Inp	752.00		NIST
Inp	759.00		NIST
Inp	797.00		NIST
Inp	795.00		NIST
Inp	749.60		NIST
Inp	793.80		NIST
Inp	766.00		NIST
Inp	798.00		NIST
Inp	808.00		NIST
Inp	811.00		NIST
Inp	771.00		NIST
Inp	764.00		NIST
Inp	767.00		NIST
Inp	769.00		NIST
Inp	775.00		NIST
Inp	780.00		NIST
Inp	764.00		NIST
Inp	793.00		NIST
Inp	794.00		NIST
Inp	791.00		NIST
Inp	791.00		NIST
Inp	789.00		NIST
Inp	747.00		NIST
Inp	767.00		NIST
Inp	761.00		NIST
Inp	796.00		NIST
Inp	802.00		NIST
Inp	788.00		NIST
Inp	767.00		NIST
Inp	766.00		NIST
Inp	789.00		NIST
Inp	791.00		NIST
Inp	794.00		NIST
Inp	754.00		NIST
Inp	761.10		NIST
Inp	754.00		NIST
Inp	Outlier 116.00		NIST
Inp	796.00		NIST
Inp	789.00		NIST
Inp	754.00		NIST
Inp	798.00		NIST
Inp	771.00		NIST
Inp	780.00		NIST
Inp	797.00		NIST
Inp	Outlier 116.00		NIST
Inp	793.00		NIST
Inp	747.00		NIST
Ip	[1142.00; 1211.70]
Ip	1176.00		NIST
Ip	1200.00		NIST
Ip	1144.00		NIST
Ip	1150.00		NIST
Ip	1164.00		NIST
Ip	1211.70		NIST
Ip	1200.00		NIST
Ip	1203.10		NIST
Ip	1200.00		NIST
Ip	1206.30		NIST
Ip	1166.00		NIST
Ip	1170.00		NIST
Ip	1192.00		NIST
Ip	1172.00		NIST
Ip	1154.00		NIST
Ip	1142.00		NIST
Ip	1144.00		NIST
Ip	1202.00		NIST
Ip	1170.00		NIST
Ip	1176.00		NIST
Ip	1154.00		NIST
Ip	1186.00		NIST
Ip	1187.00		NIST
Ip	1167.00		NIST
Ip	1167.00		NIST
Ip	1168.00		NIST
Ip	1168.00		NIST
Ip	1185.00		NIST
Ip	1176.00		NIST
Ip	1211.70		NIST
Ip	1166.00		NIST
Ip	1154.00		NIST
Ip	1168.00		NIST
Tboil	[402.15; 403.90]	K
Tboil	403.72	K	KDB
Tboil	403.50 ± 0.50	K	NIST
Tboil	403.80	K	NIST
Tboil	403.70	K	NIST
Tboil	403.90 ± 0.50	K	NIST
Tboil	403.50 ± 0.50	K	NIST
Tboil	403.90 ± 0.50	K	NIST
Tboil	402.15 ± 2.00	K	NIST
Tboil	402.15 ± 1.50	K	NIST
Tboil	403.90 ± 0.40	K	NIST
Tboil	403.80 ± 0.20	K	NIST
Tboil	403.60 ± 3.00	K	NIST
Tboil	403.40 ± 2.00	K	NIST
Tboil	402.15 ± 2.00	K	NIST
Tc	[624.00; 626.00]	K
Tc	624.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	626.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	624.50	K	KDB
Tc	624.50 ± 2.00	K	NIST
Tfus	[220.05; 222.60]	K
Tfus	222.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	221.80	K	KDB
Tfus	221.70 ± 0.30	K	NIST
Tfus	Outlier 220.05 ± 0.50	K	NIST
Tfus	222.60 ± 0.60	K	NIST
Tfus	221.85 ± 0.40	K	NIST
Tfus	221.85 ± 0.50	K	NIST
Ttriple	[220.77; 221.44]	K
Ttriple	220.77	K	Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
Ttriple	221.44 ± 0.02	K	NIST
Vc	[0.268; 0.268]	m3/kmol
Vc	0.268	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.268	m3/kmol	KDB
Zc	0.2374230		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[116.90; 149.22]	J/mol×K	[360.00; 480.00]
Cp,gas	116.90	J/mol×K	360.00	NIST
Cp,gas	121.16	J/mol×K	375.00	NIST
Cp,gas	128.03	J/mol×K	400.00	NIST
Cp,gas	133.86	J/mol×K	420.00	NIST
Cp,gas	139.31	J/mol×K	440.00	NIST
Cp,gas	144.04	J/mol×K	460.00	NIST
Cp,gas	149.22	J/mol×K	480.00	NIST
η	[0.0008610; 0.0010840]	Pa×s	[298.15; 313.15]
η	0.0010840	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	0.0009990	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	0.0009980	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	0.0009270	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	0.0009230	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	0.0008650	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	0.0008610	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
εr	[12.95; 15.66]		[243.15; 313.15]
εr	15.66		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	15.56		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	15.46		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	15.36		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	15.26		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	15.15		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	15.05		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	14.95		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	14.85		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	14.75		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	14.65		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	14.55		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	14.45		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	14.35		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	14.25		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	14.15		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	14.06		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	13.96		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	13.86		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	13.77		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	13.67		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	13.58		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	13.52		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	13.49		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	13.39		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	13.30		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	13.22		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	13.13		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	13.04		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	12.95		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	[11.40; 11.40]	kJ/mol	[221.20; 221.20]
ΔfusH	11.40	kJ/mol	221.20	NIST
ΔfusH	11.40	kJ/mol	221.20	NIST
ΔvapH	[36.35; 43.60]	kJ/mol	[286.00; 403.70]
ΔvapH	43.60	kJ/mol	286.00	NIST
ΔvapH	42.60	kJ/mol	348.50	NIST
ΔvapH	41.50	kJ/mol	363.00	NIST
ΔvapH	40.60	kJ/mol	372.00	NIST
ΔvapH	39.60	kJ/mol	377.00	NIST
ΔvapH	36.35	kJ/mol	403.70	NIST
n0	[1.43470; 1.43490]		[298.15; 298.15]
n0	1.43470		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	1.43470		298.15	Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
n0	1.43490		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	1.43470		298.15	Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K
n0	1.43470		298.15	Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
ρl	[924.99; 969.10]	kg/m3	[273.15; 318.15]
ρl	969.10	kg/m3	273.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	964.30	kg/m3	278.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	959.50	kg/m3	283.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	954.70	kg/m3	288.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	953.99	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	950.00	kg/m3	293.00	KDB
ρl	949.90	kg/m3	293.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	945.00	kg/m3	298.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	944.30	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	944.35	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	934.69	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	924.99	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
γ	0.03	N/m	298.15	Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[298.15; 429.12]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.54060e+01
Coefficient B			-3.97854e+03
Coefficient C			-3.49970e+01
Temperature range, min.			298.15
Temperature range, max.			429.12
Pvap	1.33	kPa	298.15	Calculated Property
Pvap	2.94	kPa	312.70	Calculated Property
Pvap	6.01	kPa	327.25	Calculated Property
Pvap	11.46	kPa	341.81	Calculated Property
Pvap	20.61	kPa	356.36	Calculated Property
Pvap	35.24	kPa	370.91	Calculated Property
Pvap	57.62	kPa	385.46	Calculated Property
Pvap	90.60	kPa	400.02	Calculated Property
Pvap	137.60	kPa	414.57	Calculated Property
Pvap	202.63	kPa	429.12	Calculated Property
Pvap	[2.80e-03; 5798.48]	kPa	[221.85; 626.00]	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			1.04761e+02
Coefficient B			-8.53493e+03
Coefficient C			-1.34566e+01
Coefficient D			1.06922e-05
Coefficient E			0.00000e+00
Temperature range, min.			221.85
Temperature range, max.			626.00
Pvap	2.80e-03	kPa	221.85	Calculated Property
Pvap	0.19	kPa	266.76	Calculated Property
Pvap	3.15	kPa	311.66	Calculated Property
Pvap	22.34	kPa	356.57	Calculated Property
Pvap	94.75	kPa	401.47	Calculated Property
Pvap	290.11	kPa	446.38	Calculated Property
Pvap	719.30	kPa	491.28	Calculated Property
Pvap	1555.53	kPa	536.19	Calculated Property
Pvap	3083.56	kPa	581.09	Calculated Property
Pvap	5798.48	kPa	626.00	Calculated Property
Pvap	[0.30; 1.56]	kPa	[273.09; 298.79]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			7.09898e+00
Coefficient B			-8.66734e+02
Coefficient C			-1.68499e+02
Reference			Benson and Kistiakowsky, 1942
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			273.09
Temperature range, max.			298.79
Pvap	0.30	kPa	273.09	Calculated Property
Pvap	0.38	kPa	275.95	Calculated Property
Pvap	0.47	kPa	278.80	Calculated Property
Pvap	0.57	kPa	281.66	Calculated Property
Pvap	0.69	kPa	284.51	Calculated Property
Pvap	0.82	kPa	287.37	Calculated Property
Pvap	0.98	kPa	290.22	Calculated Property
Pvap	1.15	kPa	293.08	Calculated Property
Pvap	1.35	kPa	295.93	Calculated Property
Pvap	1.56	kPa	298.79	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[222.15; 403.75]	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			6.55965e-02
Coefficient B			-1.10000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			222.15
Temperature range, max.			403.75
γ	0.04	N/m	222.15	Calculated Property
γ	0.04	N/m	242.33	Calculated Property
γ	0.04	N/m	262.51	Calculated Property
γ	0.03	N/m	282.68	Calculated Property
γ	0.03	N/m	302.86	Calculated Property
γ	0.03	N/m	323.04	Calculated Property
γ	0.03	N/m	343.22	Calculated Property
γ	0.03	N/m	363.39	Calculated Property
γ	0.02	N/m	383.57	Calculated Property
γ	0.02	N/m	403.75	Calculated Property

Similar Compounds

Find more compounds similar to Cyclopentanone.

Mixtures

• Trichloromethane + Cyclopentanone
• Butane, 1-chloro- + Cyclopentanone
• Cyclopentanone + Propane, 1,3-dichloro-
• Butane, 1,4-dichloro- + Cyclopentanone
• Cyclopentanone + Nonane
• Ethane, 1,2-dichloro- + Cyclopentanone
• Ethane, 1,1,1-trichloro- + Cyclopentanone
• Cyclopentanone + Ethane, 1,1,2,2-tetrachloro-
• 2-Pyrrolidinone, 1-methyl- + Cyclopentanone
• Cyclopentanone + Water
• Cyclopentanone + Cyclohexane, methyl- + Water
• Acetic acid, propyl ester + Cyclopentanone + Water
• Tetrahydropyran + Cyclopentanone
• Benzenesulfonamide + Cyclopentanone
• Benzenesulfonamide, 2-methyl- + Cyclopentanone
• 1,3-Dioxolane + Cyclopentanone
• Acetic acid, butyl ester + Cyclopentanone
• Cyclopentanone + 1,4-Dioxane
• Cyclopentanone + Cyclohexane
• Cyclohexanol + Cyclopentanone

Find more mixtures with Cyclopentanone.

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.
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• 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
• Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
• Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
• Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• 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
• Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K 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 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
• Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
• Liquid-Liquid Extraction of Cyclopentanone from Aqueous Solution with Methylcyclohexane or Propyl Acetate at Different Temperatures
• Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
• 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
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 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
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• 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
• Odd Even Effects in the Static Dielectric Permittivity of a Homologous Series of Liquid Cycloalkanones, (CH2)n-1C-O, n = 4 to 8
• Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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