Chemical Properties of Cyclopentane,methoxy-

InChI

InChI=1S/C6H12O/c1-7-6-4-2-3-5-6/h6H,2-5H2,1H3

InChI Key

SKTCDJAMAYNROS-UHFFFAOYSA-N

Formula

C6H12O

SMILES

COC1CCCC1

Molecular Weight¹

100.16

Other Names

• cyclopentyl methyl ether
• methoxycyclopentane

• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (K).
• T_fus : Normal melting (fusion) point (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.40; 7.43]	kPa	[258.55; 308.25]
Pvap	0.40	kPa	258.55	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	0.79	kPa	268.45	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	1.10	kPa	273.45	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	1.50	kPa	278.55	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	2.02	kPa	283.45	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	2.68	kPa	288.35	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	3.52	kPa	293.35	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	4.57	kPa	298.35	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	5.88	kPa	303.35	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap	7.43	kPa	308.25	Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
n0	[1.41820; 1.41992]		[298.00; 298.15]
n0	1.41833		298.00	Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
n0	1.41820		298.15	Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
n0	1.41992		298.15	Experimental Determination of Isobaric Vapor-Liquid Equilibrium and Isothermal Interfacial Tensions for the Binary Ethanol + Cyclopentyl Methyl Ether Mixture
ρl	[860.13; 860.43]	kg/m3	[293.15; 293.15]
ρl	860.13	kg/m3	293.15	Liquid-Liquid Phase Equilibria for Quinary, Quaternary, and Ternary Systems {Water + Furfural + Acetic Acid + Cyclopentyl Methyl Ether + CaCl2}: Measurement, Effect of Salt ,and Comparative Study
ρl	860.43	kg/m3	293.15	Measurements and Comparative Study of Ternary Liquid Liquid Equilibria for Water + Acrylic Acid + Cyclopentyl Methyl Ether at (293.15, 303.15, and 313.15) K and 100.249 kPa

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[368.20; 379.20]	K	[72.04; 101.39]
Tboil(P)	368.20	K	72.04	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil(P)	371.20	K	78.83	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil(P)	373.40	K	85.94	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil(P)	375.40	K	89.82	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
Tboil(P)	379.20	K	101.39	Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[114.94; 330.67]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-3.75500e+01
Coefficient B			6.42320e-01
Coefficient C			-3.19000e-04
Coefficient D			4.49000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	114.94	J/mol×K	273.00	Calculated Property
Cp,gas	151.75	J/mol×K	353.78	Calculated Property
Cp,gas	185.02	J/mol×K	434.56	Calculated Property
Cp,gas	214.89	J/mol×K	515.33	Calculated Property
Cp,gas	241.50	J/mol×K	596.11	Calculated Property
Cp,gas	265.00	J/mol×K	676.89	Calculated Property
Cp,gas	285.52	J/mol×K	757.67	Calculated Property
Cp,gas	303.21	J/mol×K	838.44	Calculated Property
Cp,gas	318.21	J/mol×K	919.22	Calculated Property
Cp,gas	330.67	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0219516; 0.0002331]	Pa×s	[133.15; 398.92]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.06412e+01
Coefficient B			9.08390e+02
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			133.15
Temperature range, max.			398.92
η	0.0219516	Pa×s	133.15	Calculated Property
η	0.0063626	Pa×s	162.68	Calculated Property
η	0.0026981	Pa×s	192.21	Calculated Property
η	0.0014379	Pa×s	221.74	Calculated Property
η	0.0008884	Pa×s	251.27	Calculated Property
η	0.0006075	Pa×s	280.80	Calculated Property
η	0.0004465	Pa×s	310.33	Calculated Property
η	0.0003462	Pa×s	339.86	Calculated Property
η	0.0002796	Pa×s	369.39	Calculated Property
η	0.0002331	Pa×s	398.92	Calculated Property

Similar Compounds

Find more compounds similar to Cyclopentane,methoxy-.

Mixtures

• Acetic acid + Cyclopentane,methoxy- + Water
• Cyclopentane,methoxy- + Water
• Furfural + Cyclopentane,methoxy- + Water
• Cyclopentane,methoxy- + Methyl Alcohol + Water
• Ethanol + Cyclopentane,methoxy- + Water
• 1-Propanol + Cyclopentane,methoxy- + Water
• 2-Propanol + Cyclopentane,methoxy- + Water
• Ethanol + Cyclopentane,methoxy-
• 2-Propenoic acid + Cyclopentane,methoxy- + Water
• Cyclopentanol + Cyclopentane,methoxy-

Sources

• 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).
• Cheméo Relay (1.0)
• Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
• Crippen Method
• Crippen Method
• Liquid-liquid phase equilibria of the quaternary system {water (1) + acrylic acid (2) + acetic acid (3) + cyclopentyl methyl ether (4)}: Measurement, correlation, and comparative study
• Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
• Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
• Liquid-Liquid Equilibria for Ternary Systems of Water + Methoxycyclopentane (CPME) + Alcohol; Methanol, Ethanol, 1-Propanol, or 2-Propanol
• Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
• Liquid-Liquid Phase Equilibria for Quinary, Quaternary, and Ternary Systems {Water + Furfural + Acetic Acid + Cyclopentyl Methyl Ether + CaCl2}: Measurement, Effect of Salt ,and Comparative Study
• Measurement and Correlation of Isobaric Vapor Liquid Equilibrium Data for Cyclopentyl Methyl Ether and Cyclopentanol
• Experimental Determination of Isobaric Vapor-Liquid Equilibrium and Isothermal Interfacial Tensions for the Binary Ethanol + Cyclopentyl Methyl Ether Mixture
• Liquid Liquid Equilibria of Water + Acetic Acid + Cyclopentyl Methyl Ether (CPME) System at Different Temperatures
• Measurements and Comparative Study of Ternary Liquid Liquid Equilibria for Water + Acrylic Acid + Cyclopentyl Methyl Ether at (293.15, 303.15, and 313.15) K and 100.249 kPa
• Joback Method
• McGowan Method
• NIST Webbook

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