Chemical Properties of Cyclopentanol (CAS 96-41-3)

InChI

InChI=1S/C5H10O/c6-5-3-1-2-4-5/h5-6H,1-4H2

InChI Key

XCIXKGXIYUWCLL-UHFFFAOYSA-N

Formula

C5H10O

SMILES

OC1CCCC1

Molecular Weight¹

86.13

CAS

96-41-3

Other Names

• CYCOLPENTYL ALCOHOL
• Hydroxycyclopentane
• UN 2244
• cyclopentyl alcohol

• ω : Acentric Factor.
• PAff : Proton affinity (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).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• 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 : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4840		Relay (1.0) Calculated Property
PAff	798.00 ± 6.00	kJ/mol	NIST
ΔcH°liquid	[-3096.70; -3096.50]	kJ/mol
ΔcH°liquid	-3096.70 ± 1.70	kJ/mol	NIST
ΔcH°liquid	-3096.50 ± 1.50	kJ/mol	NIST
ΔfG°	-109.05	kJ/mol	Joback Calculated Property
ΔfH°gas	[-243.00; -242.60]	kJ/mol
ΔfH°gas	-243.00	kJ/mol	NIST
ΔfH°gas	-242.60 ± 1.70	kJ/mol	NIST
ΔfH°gas	-242.90	kJ/mol	NIST
ΔfH°liquid	[-300.40; -300.00]	kJ/mol
ΔfH°liquid	-300.40 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-300.00 ± 1.70	kJ/mol	NIST
ΔfH°liquid	-300.30 ± 0.20	kJ/mol	NIST
ΔfusH°	6.73	kJ/mol	Joback Calculated Property
ΔvapH°	[56.10; 57.63]	kJ/mol
ΔvapH°	57.63	kJ/mol	NIST
ΔvapH°	57.10	kJ/mol	NIST
ΔvapH°	56.10	kJ/mol	NIST
ΔvapH°	56.40	kJ/mol	NIST
ΔvapH°	57.50 ± 0.20	kJ/mol	NIST
ΔvapH°	57.50 ± 0.30	kJ/mol	NIST
ΔvapH°	57.49	kJ/mol	NIST
ΔvapH°	57.40	kJ/mol	NIST
IE	[9.58; 9.72]	eV
IE	9.72	eV	NIST
IE	9.58 ± 0.06	eV	NIST
log10WS	-0.10		Relay (1.0) Calculated Property
logPoct/wat	0.921		Crippen Calculated Property
McVol	76.320	ml/mol	McGowan Calculated Property
Pc	[4900.00; 4900.00]	kPa
Pc	4900.00	kPa	KDB
Pc	4900.00 ± 100.00	kPa	NIST
Pc	4900.00 ± 100.00	kPa	NIST
Inp	[765.00; 805.00]
Inp	792.00		NIST
Inp	768.00		NIST
Inp	781.00		NIST
Inp	768.00		NIST
Inp	782.00		NIST
Inp	767.00		NIST
Inp	768.00		NIST
Inp	773.00		NIST
Inp	765.00		NIST
Inp	781.00		NIST
Inp	765.00		NIST
Inp	781.00		NIST
Inp	774.00		NIST
Inp	774.00		NIST
Inp	795.00		NIST
Inp	802.00		NIST
Inp	805.00		NIST
Inp	792.00		NIST
Inp	805.00		NIST
I	[1278.00; 1339.00]
I	1298.00		NIST
I	1283.00		NIST
I	1300.00		NIST
I	1314.00		NIST
I	1314.00		NIST
I	1309.00		NIST
I	1323.00		NIST
I	1278.00		NIST
I	1281.00		NIST
I	1328.00		NIST
I	1300.00		NIST
I	1290.00		NIST
I	1303.00		NIST
I	1283.00		NIST
I	1289.00		NIST
I	1292.00		NIST
I	1289.00		NIST
I	1292.00		NIST
I	1323.00		NIST
I	Outlier 1339.00		NIST
I	1280.00		NIST
I	1283.00		NIST
I	1327.00		NIST
I	1297.00		NIST
I	1327.00		NIST
I	1283.00		NIST
I	1300.00		NIST
I	1278.00		NIST
I	1323.00		NIST
I	1297.00		NIST
S°liquid	206.30	J/mol×K	NIST
Tboil	[410.00; 414.00]	K
Tboil	412.50	K	Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
Tboil	413.38	K	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil	413.57	K	KDB
Tboil	412.70	K	NIST
Tboil	414.00 ± 0.50	K	NIST
Tboil	412.00 ± 4.00	K	NIST
Tboil	Outlier 410.00 ± 4.00	K	NIST
Tboil	412.30 ± 1.00	K	NIST
Tboil	414.00 ± 0.50	K	NIST
Tboil	414.00 ± 0.50	K	NIST
Tboil	413.30 ± 0.60	K	NIST
Tboil	414.00 ± 0.20	K	NIST
Tboil	413.90 ± 1.50	K	NIST
Tc	[619.50; 620.00]	K
Tc	619.50	K	KDB
Tc	620.00 ± 1.00	K	NIST
Tc	619.50 ± 1.00	K	NIST
Tfus	[253.00; 254.15]	K
Tfus	254.00	K	KDB
Tfus	254.15 ± 1.00	K	NIST
Tfus	253.00 ± 2.00	K	NIST
Ttriple	[255.60; 257.40]	K
Ttriple	255.60 ± 0.30	K	NIST
Ttriple	256.00 ± 0.50	K	NIST
Ttriple	257.40 ± 0.20	K	NIST
Ttriple	257.40 ± 0.20	K	NIST

Cheméo can also estimate Critical Volume for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[149.90; 207.53]	J/mol×K	[421.26; 610.59]
Cp,gas	149.90	J/mol×K	421.26	Joback Calculated Property
Cp,gas	160.80	J/mol×K	452.81	Joback Calculated Property
Cp,gas	171.16	J/mol×K	484.37	Joback Calculated Property
Cp,gas	181.00	J/mol×K	515.92	Joback Calculated Property
Cp,gas	190.32	J/mol×K	547.48	Joback Calculated Property
Cp,gas	199.16	J/mol×K	579.03	Joback Calculated Property
Cp,gas	207.53	J/mol×K	610.59	Joback Calculated Property
Cp,liquid	[157.60; 234.10]	J/mol×K	[265.06; 357.78]
Cp,liquid	157.60	J/mol×K	265.06	Heat capacities of selected cycloalcohols
Cp,liquid	157.60	J/mol×K	265.06	Heat capacities of selected cycloalcohols
Cp,liquid	160.70	J/mol×K	270.00	Heat capacities of selected cycloalcohols
Cp,liquid	160.70	J/mol×K	270.00	Heat capacities of selected cycloalcohols
Cp,liquid	164.20	J/mol×K	275.00	Heat capacities of selected cycloalcohols
Cp,liquid	164.20	J/mol×K	275.00	Heat capacities of selected cycloalcohols
Cp,liquid	167.80	J/mol×K	280.00	Heat capacities of selected cycloalcohols
Cp,liquid	167.90	J/mol×K	280.00	Heat capacities of selected cycloalcohols
Cp,liquid	171.60	J/mol×K	285.00	Heat capacities of selected cycloalcohols
Cp,liquid	171.70	J/mol×K	285.00	Heat capacities of selected cycloalcohols
Cp,liquid	175.70	J/mol×K	290.00	Heat capacities of selected cycloalcohols
Cp,liquid	175.90	J/mol×K	290.00	Heat capacities of selected cycloalcohols
Cp,liquid	180.00	J/mol×K	295.00	Heat capacities of selected cycloalcohols
Cp,liquid	180.10	J/mol×K	295.00	Heat capacities of selected cycloalcohols
Cp,liquid	185.40	J/mol×K	298.00	NIST
Cp,liquid	181.57	J/mol×K	298.15	NIST
Cp,liquid	184.14	J/mol×K	298.15	NIST
Cp,liquid	181.57	J/mol×K	298.15	NIST
Cp,liquid	184.30	J/mol×K	300.00	Heat capacities of selected cycloalcohols
Cp,liquid	184.40	J/mol×K	300.00	Heat capacities of selected cycloalcohols
Cp,liquid	188.60	J/mol×K	305.00	Heat capacities of selected cycloalcohols
Cp,liquid	188.70	J/mol×K	305.00	Heat capacities of selected cycloalcohols
Cp,liquid	193.00	J/mol×K	310.00	Heat capacities of selected cycloalcohols
Cp,liquid	193.10	J/mol×K	310.00	Heat capacities of selected cycloalcohols
Cp,liquid	197.40	J/mol×K	315.00	Heat capacities of selected cycloalcohols
Cp,liquid	197.60	J/mol×K	315.00	Heat capacities of selected cycloalcohols
Cp,liquid	201.80	J/mol×K	320.00	Heat capacities of selected cycloalcohols
Cp,liquid	202.00	J/mol×K	320.00	Heat capacities of selected cycloalcohols
Cp,liquid	206.20	J/mol×K	325.00	Heat capacities of selected cycloalcohols
Cp,liquid	206.40	J/mol×K	325.00	Heat capacities of selected cycloalcohols
Cp,liquid	210.50	J/mol×K	330.00	Heat capacities of selected cycloalcohols
Cp,liquid	210.70	J/mol×K	330.00	Heat capacities of selected cycloalcohols
Cp,liquid	215.00	J/mol×K	335.00	Heat capacities of selected cycloalcohols
Cp,liquid	215.10	J/mol×K	335.00	Heat capacities of selected cycloalcohols
Cp,liquid	219.50	J/mol×K	340.00	Heat capacities of selected cycloalcohols
Cp,liquid	219.50	J/mol×K	340.00	Heat capacities of selected cycloalcohols
Cp,liquid	223.70	J/mol×K	345.00	Heat capacities of selected cycloalcohols
Cp,liquid	223.80	J/mol×K	345.00	Heat capacities of selected cycloalcohols
Cp,liquid	228.00	J/mol×K	350.00	Heat capacities of selected cycloalcohols
Cp,liquid	228.10	J/mol×K	350.00	Heat capacities of selected cycloalcohols
Cp,liquid	232.00	J/mol×K	354.91	Heat capacities of selected cycloalcohols
Cp,liquid	232.00	J/mol×K	355.00	Heat capacities of selected cycloalcohols
Cp,liquid	234.10	J/mol×K	357.78	Heat capacities of selected cycloalcohols
η	[0.0003291; 0.0690807]	Pa×s	[217.83; 421.26]
η	0.0690807	Pa×s	217.83	Joback Calculated Property
η	0.0155505	Pa×s	251.73	Joback Calculated Property
η	0.0049874	Pa×s	285.64	Joback Calculated Property
η	0.0020361	Pa×s	319.54	Joback Calculated Property
η	0.0009871	Pa×s	353.45	Joback Calculated Property
η	0.0005432	Pa×s	387.36	Joback Calculated Property
η	0.0003291	Pa×s	421.26	Joback Calculated Property
ΔfusH	[1.54; 3.71]	kJ/mol	[202.80; 257.40]
ΔfusH	3.71	kJ/mol	202.80	NIST
ΔfusH	1.54	kJ/mol	257.40	NIST
ΔfusH	1.54	kJ/mol	257.40	NIST
ΔvapH	[52.70; 57.10]	kJ/mol	[296.50; 391.50]
ΔvapH	57.10	kJ/mol	296.50	NIST
ΔvapH	52.70	kJ/mol	391.50	NIST
Pvap	[0.06; 0.93]	kPa	[279.84; 314.30]
Pvap	0.06	kPa	279.84	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.08	kPa	281.97	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.09	kPa	284.15	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.14	kPa	289.03	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.15	kPa	289.76	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.20	kPa	293.47	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.22	kPa	294.55	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.29	kPa	298.19	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.31	kPa	298.87	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.47	kPa	304.53	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.55	kPa	306.93	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.74	kPa	311.04	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.93	kPa	314.30	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
n0	1.45120		298.15	Molar heat capacities for (2-methyl-2-butanol + heptane) mixtures and cyclopentanol at temperatures from (284 to 353) K
ρl	[904.99; 948.70]	kg/m3	[293.15; 343.15]
ρl	947.04	kg/m3	293.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	946.99	kg/m3	293.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	948.70	kg/m3	293.15	Correlation of Experimental Liquid Liquid Equilibrium Data for Ternary Systems Using NRTL and GMDH-Type Neural Network
ρl	943.05	kg/m3	298.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	943.08	kg/m3	298.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	939.05	kg/m3	303.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	939.08	kg/m3	303.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	935.01	kg/m3	308.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	935.03	kg/m3	308.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	930.91	kg/m3	313.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	930.92	kg/m3	313.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	926.75	kg/m3	318.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	926.76	kg/m3	318.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	922.53	kg/m3	323.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	922.53	kg/m3	323.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	918.24	kg/m3	328.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	918.24	kg/m3	328.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	913.89	kg/m3	333.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	913.89	kg/m3	333.15	Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
ρl	909.48	kg/m3	338.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ρl	904.99	kg/m3	343.15	Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
ΔfusS	[5.98; 18.28]	J/mol×K	[202.80; 257.40]
ΔfusS	18.28	J/mol×K	202.80	NIST
ΔfusS	5.98	J/mol×K	257.40	NIST
csound,fluid	1435.11	m/s	298.15	Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of Pentan-1-ol, 2-Methyl-2-butanol, and Cyclopentanol in the Pressure Range from (0.1 to 100) MPa and Temperature from (293 to 318) K
γ	0.03	N/m	298.15	Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[326.43; 413.60]	K	[2.00; 102.00]
Tboil	326.43	K	2.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil	355.30	K	10.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil	370.27	K	20.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil	398.02	K	60.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil	403.40	K	71.47	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil	406.20	K	78.36	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil	408.60	K	85.50	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil	409.40	K	89.49	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil	413.60	K	102.00	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[319.85; 434.54]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.66115e+01
Coefficient B			-4.21086e+03
Coefficient C			-6.18960e+01
Temperature range, min.			319.85
Temperature range, max.			434.54
Pvap	1.33	kPa	319.85	Calculated Property
Pvap	2.87	kPa	332.59	Calculated Property
Pvap	5.79	kPa	345.34	Calculated Property
Pvap	10.96	kPa	358.08	Calculated Property
Pvap	19.71	kPa	370.82	Calculated Property
Pvap	33.82	kPa	383.57	Calculated Property
Pvap	55.69	kPa	396.31	Calculated Property
Pvap	88.41	kPa	409.05	Calculated Property
Pvap	135.84	kPa	421.80	Calculated Property
Pvap	202.67	kPa	434.54	Calculated Property
Pvap	[0.29; 101.95]	kPa	[298.15; 414.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			9.23026e+01
Coefficient B			-9.37555e+03
Coefficient C			-1.10220e+01
Coefficient D			8.05060e-06
Temperature range, min.			298.15
Temperature range, max.			414.15
Pvap	0.29	kPa	298.15	Calculated Property
Pvap	0.72	kPa	311.04	Calculated Property
Pvap	1.63	kPa	323.93	Calculated Property
Pvap	3.45	kPa	336.82	Calculated Property
Pvap	6.83	kPa	349.71	Calculated Property
Pvap	12.79	kPa	362.59	Calculated Property
Pvap	22.82	kPa	375.48	Calculated Property
Pvap	39.01	kPa	388.37	Calculated Property
Pvap	64.15	kPa	401.26	Calculated Property
Pvap	101.95	kPa	414.15	Calculated Property

Similar Compounds

Find more compounds similar to Cyclopentanol.

Mixtures

• Methyl Isobutyl Ketone + Cyclopentanol + Water
• Cyclopentanol + Ethyl Acetate + Water
• Cyclopentanol + Furfural + Water
• Cyclopentanol + 1-Butanol + Water
• Cyclopentanol + Water
• Cyclopentanol + 1-Propanol, 2-methyl- + Water
• Cyclopentanol + Propanoic acid + Water
• Cyclopentanol + 4,7-Methano-1H-indene, octahydro-
• Cyclopentanol + Tricyclo[3.3.1.13,7]decane, 1,3-dimethyl-
• Cyclopentanol + Tricyclo[3.3.1.13,7]decane, 1,3-dimethyl- + 4,7-Methano-1H-indene, octahydro-
• Cyclohexanol + Cyclopentanol
• Cyclopentanol + Carbon dioxide
• Propane + Cyclopentanol
• Cyclopentanol + Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans-
• Cyclopentanol + Cyclohexane, methyl-
• Cyclopentanol + Cyclopentane,methoxy-

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
• Molar heat capacities for (2-methyl-2-butanol + heptane) mixtures and cyclopentanol at temperatures from (284 to 353) K
• Partial molar volumes of organic solutes in water. XIX. Cyclic alcohols(aq) at T = (298 to 573) K and at pressures up to 30 MPa
• Heat capacities of selected cycloalcohols
• Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
• Correlation of Experimental Liquid Liquid Equilibrium Data for Ternary Systems Using NRTL and GMDH-Type Neural Network
• Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
• A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
• Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
• Liquid-Liquid Extraction of Biobased Isobutanol from an Aqueous Solution
• Density and Viscosity of Ternary Mixture of Cyclopentanol + exo-Tetrahydrodicyclopentadiene + 1,3-Dimethyladamantane
• Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
• Partial Molar Volumes of Cyclic Alcohols at Infinite Dilution in Water at Temperatures T ) (298 to 373) K and Pressure of 0.5 MPa
• Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of Pentan-1-ol, 2-Methyl-2-butanol, and Cyclopentanol in the Pressure Range from (0.1 to 100) MPa and Temperature from (293 to 318) K
• High-Pressure Vapor-Liquid Equilibrium Data for (Carbon Dioxide + Cyclopentanol) and (Propane + Cyclopentanol)
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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