Chemical Properties of Cyclopentane (CAS 287-92-3)

InChI

InChI=1S/C5H10/c1-2-4-5-3-1/h1-5H2

InChI Key

RGSFGYAAUTVSQA-UHFFFAOYSA-N

Formula

C5H10

SMILES

C1CCCC1

Molecular Weight¹

70.13

CAS

287-92-3

Other Names

• Pentamethylene
• UN 1146

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• 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).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• 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_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (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_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.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• 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°_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).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.1921; 0.1960]
ω	0.1921		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1923		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.1940		ChemSep v8.3 pure component data Compiled value
ω	0.1960		KDB
Tig	653.15	K	KDB
AP	289.950	K	KDB
ΔcH°liquid	[-3291.40; -3290.90]	kJ/mol
ΔcH°liquid	-3291.40 ± 0.60	kJ/mol	NIST
ΔcH°liquid	-3291.20 ± 1.30	kJ/mol	NIST
ΔcH°liquid	-3290.90 ± 0.71	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
LFL	1.10	% in Air	KDB
UFL	8.70	% in Air	KDB
Tflash,oc	266.48	K	KDB
ΔfG°	[38.60; 38.85]	kJ/mol
ΔfG°	38.85	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	38.60	kJ/mol	KDB
Rg	3.1200		KDB
Δc,grossH	3290.93	kJ/mol	KDB
Δc,netH	3070.889	kJ/mol	KDB
ΔfH°gas	[-77.29; -76.40]	kJ/mol
ΔfH°gas	-77.03	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-77.29	kJ/mol	KDB
ΔfH°gas	-76.40 ± 0.79	kJ/mol	NIST
ΔfH°gas	-76.90	kJ/mol	NIST
ΔfH°gas	-77.24 ± 0.75	kJ/mol	NIST
ΔfH°liquid	[-105.90; -105.60]	kJ/mol
ΔfH°liquid	-105.60 ± 1.80	kJ/mol	NIST
ΔfH°liquid	-105.90 ± 0.75	kJ/mol	NIST
ΔfusH°	1.57	kJ/mol	Joback Calculated Property
ΔvapH°	[28.50; 29.20]	kJ/mol
ΔvapH°	28.72	kJ/mol	NIST
ΔvapH°	28.50	kJ/mol	NIST
ΔvapH°	28.60	kJ/mol	NIST
ΔvapH°	28.50 ± 0.10	kJ/mol	NIST
ΔvapH°	28.90	kJ/mol	NIST
ΔvapH°	29.00	kJ/mol	NIST
ΔvapH°	28.70	kJ/mol	NIST
ΔvapH°	29.20	kJ/mol	NIST
IE	[9.83; 11.01]	eV
IE	10.33 ± 0.15	eV	NIST
IE	Outlier 9.83 ± 0.05	eV	NIST
IE	10.35	eV	NIST
IE	10.33 ± 0.15	eV	NIST
IE	10.30 ± 0.10	eV	NIST
IE	10.55 ± 0.03	eV	NIST
IE	10.54 ± 0.05	eV	NIST
IE	10.48	eV	NIST
IE	10.40	eV	NIST
IE	10.49	eV	NIST
IE	10.91 ± 0.07	eV	NIST
IE	10.50 ± 0.01	eV	NIST
IE	10.49	eV	NIST
IE	10.53 ± 0.05	eV	NIST
IE	Outlier 11.01	eV	NIST
IE	10.70 ± 0.10	eV	NIST
IE	10.50	eV	NIST
log10WS	[-2.64; -2.64]
log10WS	-2.64		Aq. Solubility Prediction
log10WS	-2.64		Estimated Solubility
logPoct/wat	1.950		Crippen Calculated Property
McVol	70.450	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[4430.00; 4514.03]	kPa
Pc	4510.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Pc	4509.98	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4507.79	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	4508.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4510.00	kPa	KDB
Pc	4510.00 ± 40.00	kPa	NIST
Pc	4508.00 ± 40.53	kPa	NIST
Pc	Outlier 4430.00 ± 50.66	kPa	NIST
Pc	4514.03 ± 5.06	kPa	NIST
Ptriple	9.07e-03	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[270.01; 270.01]	kg/m3
ρc	270.01 ± 2.81	kg/m3	NIST
ρc	270.01 ± 4.21	kg/m3	NIST
ρc	270.01 ± 2.10	kg/m3	NIST
Inp	[520.00; 599.00]
Inp	572.00		NIST
Inp	587.00		NIST
Inp	587.70		NIST
Inp	558.00		NIST
Inp	572.00		NIST
Inp	573.00		NIST
Inp	574.30		NIST
Inp	582.40		NIST
Inp	Outlier 591.00		NIST
Inp	562.00		NIST
Inp	567.80		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	568.30		NIST
Inp	568.40		NIST
Inp	562.60		NIST
Inp	587.60		NIST
Inp	588.00		NIST
Inp	565.00		NIST
Inp	568.00		NIST
Inp	572.00		NIST
Inp	566.20		NIST
Inp	587.90		NIST
Inp	566.50		NIST
Inp	565.60		NIST
Inp	566.10		NIST
Inp	569.40		NIST
Inp	569.90		NIST
Inp	574.50		NIST
Inp	563.00		NIST
Inp	565.00		NIST
Inp	566.00		NIST
Inp	568.00		NIST
Inp	570.00		NIST
Inp	572.00		NIST
Inp	567.80		NIST
Inp	568.30		NIST
Inp	577.00		NIST
Inp	566.00		NIST
Inp	582.00		NIST
Inp	570.00		NIST
Inp	567.00		NIST
Inp	566.00		NIST
Inp	565.00		NIST
Inp	568.00		NIST
Inp	568.80		NIST
Inp	565.55		NIST
Inp	563.30		NIST
Inp	575.90		NIST
Inp	573.00		NIST
Inp	576.00		NIST
Inp	567.00		NIST
Inp	570.00		NIST
Inp	566.00		NIST
Inp	568.00		NIST
Inp	573.00		NIST
Inp	588.00		NIST
Inp	566.00		NIST
Inp	567.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	572.00		NIST
Inp	568.00		NIST
Inp	570.00		NIST
Inp	571.00		NIST
Inp	573.00		NIST
Inp	574.00		NIST
Inp	566.30		NIST
Inp	571.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	568.00		NIST
Inp	572.00		NIST
Inp	563.00		NIST
Inp	566.00		NIST
Inp	569.00		NIST
Inp	572.00		NIST
Inp	562.00		NIST
Inp	563.00		NIST
Inp	564.00		NIST
Inp	568.00		NIST
Inp	570.00		NIST
Inp	578.00		NIST
Inp	568.00		NIST
Inp	562.00		NIST
Inp	Outlier 599.00		NIST
Inp	587.00		NIST
Inp	571.00		NIST
Inp	557.00		NIST
Inp	576.00		NIST
Inp	566.50		NIST
Inp	563.00		NIST
Inp	553.70		NIST
Inp	580.29		NIST
Inp	563.20		NIST
Inp	556.60		NIST
Inp	554.33		NIST
Inp	554.33		NIST
Inp	554.13		NIST
Inp	554.24		NIST
Inp	554.00		NIST
Inp	557.00		NIST
Inp	559.00		NIST
Inp	564.00		NIST
Inp	564.00		NIST
Inp	565.00		NIST
Inp	571.00		NIST
Inp	566.00		NIST
Inp	566.00		NIST
Inp	569.00		NIST
Inp	Outlier 520.00		NIST
Inp	Outlier 524.00		NIST
Inp	560.00		NIST
Inp	560.00		NIST
Inp	564.00		NIST
Inp	562.00		NIST
Inp	554.50		NIST
Inp	564.00		NIST
Inp	554.00		NIST
Inp	Outlier 527.00		NIST
Inp	562.00		NIST
Inp	563.00		NIST
Inp	587.00		NIST
Inp	566.00		NIST
Inp	587.00		NIST
Inp	568.00		NIST
Inp	570.00		NIST
Inp	564.00		NIST
Inp	570.00		NIST
Inp	570.00		NIST
Inp	560.00		NIST
Inp	558.00		NIST
Inp	Outlier 533.00		NIST
Inp	572.00		NIST
Inp	557.00		NIST
Inp	570.00		NIST
Inp	577.00		NIST
Inp	573.00		NIST
Inp	564.00		NIST
Inp	573.00		NIST
Inp	564.00		NIST
Inp	559.00		NIST
Inp	553.70		NIST
Inp	554.33		NIST
Inp	566.50		NIST
Ip	[694.00; 720.00]
Ip	694.00		NIST
Ip	720.00		NIST
Ip	694.00		NIST
Ip	700.00		NIST
Ip	710.00		NIST
Ip	698.00		NIST
Ip	720.00		NIST
S°liquid	[204.14; 206.70]	J/mol×K
S°liquid	204.14	J/mol×K	NIST
S°liquid	204.47	J/mol×K	NIST
S°liquid	206.70	J/mol×K	NIST
Tboil	[317.00; 323.70]	K
Tboil	322.38	K	ChemSep v8.3 pure component data Compiled value
Tboil	322.40	K	KDB
Tboil	322.40	K	NIST
Tboil	322.40	K	NIST
Tboil	322.37 ± 0.10	K	NIST
Tboil	322.70 ± 1.00	K	NIST
Tboil	322.41 ± 0.40	K	NIST
Tboil	322.70 ± 0.20	K	NIST
Tboil	322.40 ± 0.30	K	NIST
Tboil	Outlier 317.00 ± 5.00	K	NIST
Tboil	322.35 ± 0.50	K	NIST
Tboil	322.00 ± 3.00	K	NIST
Tboil	322.48 ± 0.30	K	NIST
Tboil	322.50 ± 0.40	K	NIST
Tboil	322.50 ± 0.20	K	NIST
Tboil	322.40 ± 0.30	K	NIST
Tboil	322.35 ± 0.30	K	NIST
Tboil	321.65 ± 0.60	K	NIST
Tboil	322.41 ± 0.05	K	NIST
Tboil	322.60 ± 0.40	K	NIST
Tboil	322.40 ± 0.20	K	NIST
Tboil	322.41 ± 0.01	K	NIST
Tboil	322.41 ± 0.30	K	NIST
Tboil	322.41 ± 0.05	K	NIST
Tboil	322.50 ± 0.30	K	NIST
Tboil	322.55 ± 0.30	K	NIST
Tboil	322.41 ± 0.20	K	NIST
Tboil	322.41 ± 0.15	K	NIST
Tboil	322.65 ± 0.50	K	NIST
Tboil	322.25 ± 0.60	K	NIST
Tboil	322.41 ± 0.20	K	NIST
Tboil	322.35 ± 0.40	K	NIST
Tboil	322.60 ± 0.70	K	NIST
Tboil	322.35 ± 0.20	K	NIST
Tboil	322.45 ± 0.20	K	NIST
Tboil	323.15 ± 1.00	K	NIST
Tboil	322.10 ± 0.60	K	NIST
Tboil	322.65 ± 0.30	K	NIST
Tboil	322.70 ± 1.00	K	NIST
Tboil	322.70 ± 1.00	K	NIST
Tboil	323.70 ± 1.40	K	NIST
Tboil	323.65 ± 2.00	K	NIST
Tc	[511.60; 511.76]	K
Tc	511.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc	511.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	511.76	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	511.60	K	ChemSep v8.3 pure component data Compiled value
Tc	511.70	K	KDB
Tc	511.70 ± 0.20	K	NIST
Tc	511.60	K	NIST
Tc	511.70 ± 0.20	K	NIST
Tc	511.60 ± 0.15	K	NIST
Tc	511.75 ± 0.05	K	NIST
Tfus	[176.64; 180.05]	K
Tfus	179.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	179.31	K	ChemSep v8.3 pure component data Compiled value
Tfus	179.30	K	KDB
Tfus	179.20	K	Aq. Solubility Prediction
Tfus	Outlier 176.64 ± 0.30	K	NIST
Tfus	179.60 ± 0.30	K	NIST
Tfus	179.55 ± 0.30	K	NIST
Tfus	Outlier 177.06 ± 0.20	K	NIST
Tfus	179.25 ± 0.40	K	NIST
Tfus	179.26 ± 0.40	K	NIST
Tfus	179.69 ± 0.10	K	NIST
Tfus	179.26 ± 0.07	K	NIST
Tfus	179.38 ± 0.05	K	NIST
Tfus	179.25 ± 0.06	K	NIST
Tfus	179.26 ± 0.05	K	NIST
Tfus	179.28 ± 0.04	K	NIST
Tfus	179.35 ± 0.20	K	NIST
Tfus	179.35 ± 0.20	K	NIST
Tfus	179.23 ± 0.01	K	NIST
Tfus	179.23 ± 0.05	K	NIST
Tfus	179.25 ± 0.07	K	NIST
Tfus	179.38 ± 0.05	K	NIST
Tfus	179.23 ± 0.40	K	NIST
Tfus	179.68 ± 0.30	K	NIST
Tfus	179.31 ± 0.20	K	NIST
Tfus	178.85 ± 0.30	K	NIST
Tfus	178.85 ± 0.30	K	NIST
Tfus	178.85 ± 0.20	K	NIST
Tfus	178.85 ± 0.30	K	NIST
Tfus	178.15 ± 0.50	K	NIST
Tfus	178.35 ± 0.50	K	NIST
Tfus	180.05 ± 0.50	K	NIST
Ttriple	[179.00; 179.71]	K
Ttriple	179.71	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	179.28	K	ChemSep v8.3 pure component data Compiled value
Ttriple	179.71 ± 0.05	K	NIST
Ttriple	179.71 ± 0.01	K	NIST
Ttriple	179.69 ± 0.08	K	NIST
Ttriple	179.00 ± 0.20	K	NIST
Ttriple	179.71 ± 0.05	K	NIST
Ttriple	179.71 ± 0.01	K	NIST
Ttriple	179.00 ± 0.20	K	NIST
UQi	2.47		ChemSep v8.3 pure component data Compiled value
URi	3.30		ChemSep v8.3 pure component data Compiled value
Vc	[0.259; 0.260]	m3/kmol
Vc	0.259	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Vc	0.259	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.260	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.259	m3/kmol	KDB
Vc	0.259	m3/kmol	NIST
VCOSTALD	0.26	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.20		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2745520; 0.2760000]
Zc	0.2750000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Zc	0.2760000		ChemSep v8.3 pure component data Compiled value
Zc	0.2745520		KDB
Zra	[0.27; 0.27]
Zra	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[93.96; 160.10]	J/mol×K	[329.05; 539.00]
Cp,gas	93.96 ± 0.19	J/mol×K	329.05	NIST
Cp,gas	102.01 ± 0.84	J/mol×K	353.00	NIST
Cp,gas	108.16 ± 0.84	J/mol×K	372.00	NIST
Cp,gas	117.30 ± 1.30	J/mol×K	395.00	NIST
Cp,gas	117.09 ± 0.23	J/mol×K	395.05	NIST
Cp,gas	126.30 ± 1.30	J/mol×K	424.00	NIST
Cp,gas	138.70 ± 1.30	J/mol×K	463.00	NIST
Cp,gas	139.47 ± 0.28	J/mol×K	463.10	NIST
Cp,gas	150.70 ± 1.70	J/mol×K	503.00	NIST
Cp,gas	160.10 ± 1.70	J/mol×K	539.00	NIST
Cp,liquid	[99.82; 128.83]	J/mol×K	[180.00; 300.00]
Cp,liquid	99.82	J/mol×K	180.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	100.90	J/mol×K	190.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	102.20	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	103.70	J/mol×K	210.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	105.60	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	107.70	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	110.00	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	112.50	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	115.10	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	118.00	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	118.90	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	121.00	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	124.10	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	126.17	J/mol×K	293.15	NIST
Cp,liquid	125.90	J/mol×K	293.70	NIST
Cp,liquid	126.80	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	126.74	J/mol×K	298.15	NIST
Cp,liquid	126.87	J/mol×K	298.15	NIST
Cp,liquid	127.28	J/mol×K	298.15	NIST
Cp,liquid	126.78	J/mol×K	298.15	NIST
Cp,liquid	128.83	J/mol×K	298.15	NIST
Cp,liquid	127.40	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	127.44	J/mol×K	300.00	NIST
η	[0.0002502; 0.0007268]	Pa×s	[253.15; 353.15]
η	0.0007268	Pa×s	253.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0006786	Pa×s	258.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0006347	Pa×s	263.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0005930	Pa×s	268.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0005567	Pa×s	273.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0005224	Pa×s	278.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0005230	Pa×s	278.15	Temperature and Density Dependence of the Viscosity of Cyclopentane
η	0.0004922	Pa×s	283.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0004932	Pa×s	283.15	Temperature and Density Dependence of the Viscosity of Cyclopentane
η	0.0004646	Pa×s	288.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0004657	Pa×s	288.15	Temperature and Density Dependence of the Viscosity of Cyclopentane
η	0.0004380	Pa×s	293.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0004390	Pa×s	293.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0004382	Pa×s	293.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0004390	Pa×s	293.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0004390	Pa×s	293.15	Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
η	0.0004380	Pa×s	293.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0004405	Pa×s	293.15	Temperature and Density Dependence of the Viscosity of Cyclopentane
η	0.0004150	Pa×s	298.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0004160	Pa×s	298.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0004160	Pa×s	298.15	Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
η	0.0004160	Pa×s	298.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0004148	Pa×s	298.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0004173	Pa×s	298.15	Temperature and Density Dependence of the Viscosity of Cyclopentane
η	0.0003923	Pa×s	303.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0003940	Pa×s	303.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0003940	Pa×s	303.15	Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
η	0.0003940	Pa×s	303.15	Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η	0.0003940	Pa×s	303.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0003714	Pa×s	308.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0003740	Pa×s	308.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0003521	Pa×s	313.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0003550	Pa×s	313.15	Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
η	0.0003350	Pa×s	318.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0003190	Pa×s	323.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0003048	Pa×s	328.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0002912	Pa×s	333.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0002793	Pa×s	338.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0002690	Pa×s	343.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0002590	Pa×s	348.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
η	0.0002502	Pa×s	353.15	Saturated Liquid Viscosity of Cyclopentane and Isopentane
ΔfusH	[0.34; 4.90]	kJ/mol	[122.00; 179.70]
ΔfusH	4.90	kJ/mol	122.00	NIST
ΔfusH	0.34	kJ/mol	138.00	NIST
ΔfusH	0.60	kJ/mol	179.70	NIST
ΔfusH	0.60	kJ/mol	179.70	NIST
ΔsubH	42.60	kJ/mol	122.00	NIST
ΔvapH	[27.20; 29.21]	kJ/mol	[298.15; 481.50]
ΔvapH	29.21	kJ/mol	298.15	NIST
ΔvapH	29.20	kJ/mol	305.50	NIST
ΔvapH	29.00	kJ/mol	306.00	NIST
ΔvapH	27.90 ± 0.10	kJ/mol	310.00	NIST
ΔvapH	27.30 ± 0.10	kJ/mol	322.00	NIST
ΔvapH	27.30	kJ/mol	322.40	KDB
ΔvapH	27.30	kJ/mol	322.40	NIST
ΔvapH	27.40	kJ/mol	323.00	NIST
ΔvapH	28.00	kJ/mol	353.00	NIST
ΔvapH	27.20	kJ/mol	418.00	NIST
ΔvapH	27.50	kJ/mol	481.50	NIST
n0	[1.39456; 1.40640]		[293.15; 313.15]
n0	1.40640		293.15	Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
n0	1.40292		298.15	Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
n0	1.40363		298.15	KDB
n0	1.39456		313.15	Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
ρl	[726.57; 762.30]	kg/m3	[273.15; 308.15]
ρl	762.30	kg/m3	273.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	757.50	kg/m3	278.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	752.60	kg/m3	283.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	747.70	kg/m3	288.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	745.00	kg/m3	293.00	KDB
ρl	742.80	kg/m3	293.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	745.70	kg/m3	293.15	Correlation of Experimental Liquid Liquid Equilibrium Data for Ternary Systems Using NRTL and GMDH-Type Neural Network
ρl	739.74	kg/m3	298.15	Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
ρl	737.80	kg/m3	298.15	Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
ρl	733.63	kg/m3	298.15	Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
ρl	740.00	kg/m3	298.15	Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
ρl	726.57	kg/m3	308.15	Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
ΔfusS	[2.49; 40.13]	J/mol×K	[122.00; 179.70]
ΔfusS	40.13	J/mol×K	122.00	NIST
ΔfusS	2.49	J/mol×K	138.00	NIST
ΔfusS	3.35	J/mol×K	179.70	NIST
csound,fluid	[1129.90; 1283.50]	m/s	[283.15; 313.15]
csound,fluid	1283.50	m/s	283.15	Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid	1206.60	m/s	298.15	Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid	1129.90	m/s	313.15	Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
γ	[0.02; 0.02]	N/m	[283.15; 313.15]
γ	0.02	N/m	283.15	Thermophysical study of 1,4-dioxane with cycloalkane mixtures
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Thermophysical study of 1,4-dioxane with cycloalkane mixtures
γ	0.02	N/m	313.15	Thermophysical study of 1,4-dioxane with cycloalkane mixtures
ΔvapS	97.98	J/mol×K	298.15	NIST
λliquid	[0.12; 0.14]	W/m×K	[257.08; 316.54]
λliquid	0.14	W/m×K	257.08	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.14	W/m×K	257.27	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.14	W/m×K	257.40	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	276.13	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	276.33	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	276.47	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	293.63	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	293.83	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	293.97	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	300.67	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	300.87	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	301.01	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	316.21	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	316.40	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	316.54	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Datasets

1. Viscosity, Pa*s (1)
2. Speed of sound, m/s (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
273.15	100.00	0.0006
273.15	10000.00	0.0006
273.15	30000.00	0.0007
273.15	40000.00	0.0008
293.15	100.00	0.0004
293.15	10000.00	0.0005
293.15	30000.00	0.0006
293.15	40000.00	0.0006
298.15	100.00	0.0004
298.15	10000.00	0.0005
298.15	30000.00	0.0005
298.15	40000.00	0.0006
313.15	10000.00	0.0004
313.15	30000.00	0.0005
313.15	45000.00	0.0005
333.15	10000.00	0.0003
333.15	30000.00	0.0004
333.15	45000.00	0.0004
353.15	15000.00	0.0003
353.15	30000.00	0.0003
353.15	45000.00	0.0004
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
258.15	100.00	1419.058
258.15	5072.00	1446.07
258.15	10244.00	1473.008
258.15	15262.00	1498.119
258.15	20158.00	1521.653
258.15	25083.00	1544.511
258.15	30141.00	1567.131
273.15	100.00	1336.626
273.15	5169.00	1366.736
273.15	10059.00	1394.32
273.15	15219.00	1422.015
273.15	20251.00	1447.913
273.15	25184.00	1472.273
273.15	30227.00	1496.252
293.15	105.00	1230.093
293.15	5059.00	1262.962
293.15	10088.00	1294.375
293.15	15198.00	1324.591
293.15	20121.00	1352.283
293.15	25192.00	1379.573
293.15	30134.00	1404.98
313.15	107.00	1126.831
313.15	5113.00	1164.014
313.15	10058.00	1198.273
313.15	15132.00	1231.306
313.15	20097.00	1261.807
313.15	25098.00	1290.997
313.15	30162.00	1319.175
333.15	149.00	1026.636
333.15	5035.00	1067.634
333.15	10139.00	1106.967
333.15	15108.00	1142.542
333.15	20130.00	1176.238
333.15	25152.00	1207.969
333.15	30170.00	1238.041
353.15	261.00	929.399
353.15	5019.00	974.633
353.15	10069.00	1018.218
353.15	15107.00	1058.051
353.15	20063.00	1094.384
353.15	25009.00	1128.301
353.15	30157.00	1161.49
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[40.20; 293.49]	J/mol×K	[100.00; 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			3.97850e+01
Coefficient B			-7.04200e+02
Coefficient C			6.17424e+00
Coefficient D			-1.49130e-04
Coefficient E			2.44910e-08
Temperature range, min.			100.00
Temperature range, max.			1500.00
Cp,gas	40.20	J/mol×K	100.00	Calculated Property
Cp,gas	69.22	J/mol×K	255.56	Calculated Property
Cp,gas	121.58	J/mol×K	411.11	Calculated Property
Cp,gas	168.15	J/mol×K	566.67	Calculated Property
Cp,gas	204.51	J/mol×K	722.22	Calculated Property
Cp,gas	232.26	J/mol×K	877.78	Calculated Property
Cp,gas	253.54	J/mol×K	1033.33	Calculated Property
Cp,gas	270.05	J/mol×K	1188.89	Calculated Property
Cp,gas	283.07	J/mol×K	1344.44	Calculated Property
Cp,gas	293.49	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[99.53; 135.74]	J/mol×K	[179.28; 322.40]	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			8.47250e+01
Coefficient B			3.68500e+02
Coefficient C			-3.85186e+00
Coefficient D			3.06330e-02
Coefficient E			-3.11240e-05
Temperature range, min.			179.28
Temperature range, max.			322.40
Cp,liquid	99.53	J/mol×K	179.28	Calculated Property
Cp,liquid	101.66	J/mol×K	195.18	Calculated Property
Cp,liquid	104.28	J/mol×K	211.08	Calculated Property
Cp,liquid	107.40	J/mol×K	226.99	Calculated Property
Cp,liquid	111.02	J/mol×K	242.89	Calculated Property
Cp,liquid	115.15	J/mol×K	258.79	Calculated Property
Cp,liquid	119.74	J/mol×K	274.69	Calculated Property
Cp,liquid	124.76	J/mol×K	290.60	Calculated Property
Cp,liquid	130.13	J/mol×K	306.50	Calculated Property
Cp,liquid	135.74	J/mol×K	322.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0011223; 0.0001614]	Pa×s	[225.00; 411.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-5.18430e+00
Coefficient B			6.70870e+02
Coefficient C			-8.40820e-01
Coefficient D			-7.06560e-07
Coefficient E			2.00000e+00
Temperature range, min.			225.00
Temperature range, max.			411.00
η	0.0011223	Pa×s	225.00	Calculated Property
η	0.0008056	Pa×s	245.67	Calculated Property
η	0.0006044	Pa×s	266.33	Calculated Property
η	0.0004696	Pa×s	287.00	Calculated Property
η	0.0003753	Pa×s	307.67	Calculated Property
η	0.0003069	Pa×s	328.33	Calculated Property
η	0.0002558	Pa×s	349.00	Calculated Property
η	0.0002166	Pa×s	369.67	Calculated Property
η	0.0001859	Pa×s	390.33	Calculated Property
η	0.0001614	Pa×s	411.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[33.48; 11.45]	kJ/mol	[179.28; 494.20]	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			4.51362e+01
Coefficient B			1.24832e+00
Coefficient C			-2.31130e+00
Coefficient D			2.40107e+00
Coefficient E			-9.43348e-01
Critical temperature, Tc (K)			5.11600e+02
Temperature range, min.			179.28
Temperature range, max.			494.20
ΔvapH	33.48	kJ/mol	179.28	Calculated Property
ΔvapH	32.03	kJ/mol	214.27	Calculated Property
ΔvapH	30.58	kJ/mol	249.26	Calculated Property
ΔvapH	29.04	kJ/mol	284.25	Calculated Property
ΔvapH	27.36	kJ/mol	319.24	Calculated Property
ΔvapH	25.45	kJ/mol	354.24	Calculated Property
ΔvapH	23.23	kJ/mol	389.23	Calculated Property
ΔvapH	20.56	kJ/mol	424.22	Calculated Property
ΔvapH	17.10	kJ/mol	459.21	Calculated Property
ΔvapH	11.45	kJ/mol	494.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[232.47; 344.93]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42014e+01
Coefficient B			-2.76893e+03
Coefficient C			-3.34600e+01
Temperature range, min.			232.47
Temperature range, max.			344.93
Pvap	1.33	kPa	232.47	Calculated Property
Pvap	3.03	kPa	244.97	Calculated Property
Pvap	6.30	kPa	257.46	Calculated Property
Pvap	12.10	kPa	269.96	Calculated Property
Pvap	21.78	kPa	282.45	Calculated Property
Pvap	37.05	kPa	294.95	Calculated Property
Pvap	60.05	kPa	307.44	Calculated Property
Pvap	93.32	kPa	319.94	Calculated Property
Pvap	139.76	kPa	332.43	Calculated Property
Pvap	202.65	kPa	344.93	Calculated Property
Pvap	[0.03; 3581.81]	kPa	[179.28; 511.60]	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			-8.16792e+01
Coefficient B			-4.01058e+02
Coefficient C			1.56271e+01
Coefficient D			-2.60872e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 511.7 K.
Temperature range, min.			179.28
Temperature range, max.			511.60
Pvap	0.03	kPa	179.28	Calculated Property
Pvap	0.48	kPa	216.20	Calculated Property
Pvap	4.68	kPa	253.13	Calculated Property
Pvap	28.50	kPa	290.05	Calculated Property
Pvap	119.62	kPa	326.98	Calculated Property
Pvap	370.66	kPa	363.90	Calculated Property
Pvap	889.31	kPa	400.83	Calculated Property
Pvap	1709.85	kPa	437.75	Calculated Property
Pvap	2702.76	kPa	474.68	Calculated Property
Pvap	3581.81	kPa	511.60	Calculated Property
Pvap	[8.36e-03; 4529.34]	kPa	[179.28; 511.76]	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			6.44024e+01
Coefficient B			-5.38926e+03
Coefficient C			-7.58416e+00
Coefficient D			7.08554e-06
Coefficient E			0.00000e+00
Temperature range, min.			179.28
Temperature range, max.			511.76
Pvap	8.36e-03	kPa	179.28	Calculated Property
Pvap	0.38	kPa	216.22	Calculated Property
Pvap	4.94	kPa	253.16	Calculated Property
Pvap	30.50	kPa	290.11	Calculated Property
Pvap	117.76	kPa	327.05	Calculated Property
Pvap	333.73	kPa	363.99	Calculated Property
Pvap	766.37	kPa	400.93	Calculated Property
Pvap	1520.52	kPa	437.88	Calculated Property
Pvap	2721.67	kPa	474.82	Calculated Property
Pvap	4529.34	kPa	511.76	Calculated Property
Pvap	[28.94; 103.91]	kPa	[288.86; 323.18]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38221e+01
Coefficient B			-2.57707e+03
Coefficient C			-4.24120e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			288.86
Temperature range, max.			323.18
Pvap	28.94	kPa	288.86	Calculated Property
Pvap	33.94	kPa	292.67	Calculated Property
Pvap	39.61	kPa	296.49	Calculated Property
Pvap	46.02	kPa	300.30	Calculated Property
Pvap	53.24	kPa	304.11	Calculated Property
Pvap	61.33	kPa	307.93	Calculated Property
Pvap	70.36	kPa	311.74	Calculated Property
Pvap	80.42	kPa	315.55	Calculated Property
Pvap	91.57	kPa	319.37	Calculated Property
Pvap	103.91	kPa	323.18	Calculated Property
Pvap	[0.83; 27.25]	kPa	[225.90; 287.39]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43846e+01
Coefficient B			-2.84439e+03
Coefficient C			-3.06660e+01
Reference			Aston, Fink, et al., 1943
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			225.90
Temperature range, max.			287.39
Pvap	0.83	kPa	225.90	Calculated Property
Pvap	1.36	kPa	232.73	Calculated Property
Pvap	2.16	kPa	239.56	Calculated Property
Pvap	3.32	kPa	246.40	Calculated Property
Pvap	4.97	kPa	253.23	Calculated Property
Pvap	7.28	kPa	260.06	Calculated Property
Pvap	10.42	kPa	266.89	Calculated Property
Pvap	14.62	kPa	273.73	Calculated Property
Pvap	20.13	kPa	280.56	Calculated Property
Pvap	27.25	kPa	287.39	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[830.43; 310.02]	kg/m3	[179.28; 511.60]	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			6.48456e+01
Coefficient B			2.63050e-01
Coefficient C			5.11770e+02
Coefficient D			2.20020e-01
Comment			Range stopped at Tc; ChemSep gives it to 511.76 K.
Temperature range, min.			179.28
Temperature range, max.			511.60
ρl	830.43	kg/m3	179.28	Calculated Property
ρl	805.04	kg/m3	216.20	Calculated Property
ρl	777.94	kg/m3	253.13	Calculated Property
ρl	748.71	kg/m3	290.05	Calculated Property
ρl	716.73	kg/m3	326.98	Calculated Property
ρl	681.04	kg/m3	363.90	Calculated Property
ρl	639.94	kg/m3	400.83	Calculated Property
ρl	589.99	kg/m3	437.75	Calculated Property
ρl	521.67	kg/m3	474.68	Calculated Property
ρl	310.02	kg/m3	511.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[179.15; 323.15]	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			6.54645e-02
Coefficient B			-1.46200e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			179.15
Temperature range, max.			323.15
γ	0.04	N/m	179.15	Calculated Property
γ	0.04	N/m	195.15	Calculated Property
γ	0.03	N/m	211.15	Calculated Property
γ	0.03	N/m	227.15	Calculated Property
γ	0.03	N/m	243.15	Calculated Property
γ	0.03	N/m	259.15	Calculated Property
γ	0.03	N/m	275.15	Calculated Property
γ	0.02	N/m	291.15	Calculated Property
γ	0.02	N/m	307.15	Calculated Property
γ	0.02	N/m	323.15	Calculated Property
γ	[0.04; 5.44e-04]	N/m	[179.28; 494.20]	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			-6.93180e-03
Coefficient B			7.32760e+01
Coefficient C			-3.54490e+00
Coefficient D			2.49350e-03
Coefficient E			-1.11850e-05
Temperature range, min.			179.28
Temperature range, max.			494.20
γ	0.04	N/m	179.28	Calculated Property
γ	0.03	N/m	214.27	Calculated Property
γ	0.03	N/m	249.26	Calculated Property
γ	0.02	N/m	284.25	Calculated Property
γ	0.02	N/m	319.24	Calculated Property
γ	0.01	N/m	354.24	Calculated Property
γ	0.01	N/m	389.23	Calculated Property
γ	0.01	N/m	424.22	Calculated Property
γ	0.00	N/m	459.21	Calculated Property
γ	5.44e-04	N/m	494.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.14]	W/m×K	[179.28; 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			9.84080e-06
Coefficient B			1.46110e+00
Coefficient C			6.39530e+02
Coefficient D			7.39610e+03
Temperature range, min.			179.28
Temperature range, max.			1000.00
λgas	0.00	W/m×K	179.28	Calculated Property
λgas	0.01	W/m×K	270.47	Calculated Property
λgas	0.02	W/m×K	361.66	Calculated Property
λgas	0.03	W/m×K	452.85	Calculated Property
λgas	0.04	W/m×K	544.04	Calculated Property
λgas	0.06	W/m×K	635.24	Calculated Property
λgas	0.08	W/m×K	726.43	Calculated Property
λgas	0.10	W/m×K	817.62	Calculated Property
λgas	0.12	W/m×K	908.81	Calculated Property
λgas	0.14	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.12]	W/m×K	[179.28; 322.40]	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			1.09610e-01
Coefficient B			-5.98590e+02
Coefficient C			3.50980e+00
Coefficient D			-1.62580e-02
Coefficient E			-9.16350e-06
Temperature range, min.			179.28
Temperature range, max.			322.40
λliquid	0.16	W/m×K	179.28	Calculated Property
λliquid	0.16	W/m×K	195.18	Calculated Property
λliquid	0.15	W/m×K	211.08	Calculated Property
λliquid	0.15	W/m×K	226.99	Calculated Property
λliquid	0.14	W/m×K	242.89	Calculated Property
λliquid	0.14	W/m×K	258.79	Calculated Property
λliquid	0.13	W/m×K	274.69	Calculated Property
λliquid	0.13	W/m×K	290.60	Calculated Property
λliquid	0.12	W/m×K	306.50	Calculated Property
λliquid	0.12	W/m×K	322.40	Calculated Property

Similar Compounds

Find more compounds similar to Cyclopentane.

Mixtures

• 1H-Imidazole, 1-methyl- + Cyclopentane
• 1,2-Ethanediol + Cyclopentane + TETRAMETHYLAMMONIUM CHLORIDE
• Cyclopentane + 1,4-Dioxane
• Furfural + Cyclopentane
• Carbon dioxide + Cyclopentane
• Cyclopentane + N-Formylmorpholine
• Cyclopentane + 2-Pyrrolidinone, 1-methyl-
• Cyclopentane + TETRAMETHYLAMMONIUM CHLORIDE + Glycerin
• Cyclopentane + Ethanol
• 1-Propanol + Cyclopentane
• Cyclopentane + 1-Butanol
• 2-Furanmethanol + Cyclopentane
• 1,2-Ethanediol + Cyclopentane
• Cyclopentane + Ethanol, 2,2'-oxybis-
• Xenon + Cyclopentane
• Cyclopentane + Triethylene glycol
• Cyclopentane + Pentane, 3-methyl- + Methyl Alcohol
• Cyclopentane + Water
• 1,3-Dioxolane + Cyclopentane
• Cyclopentane + 1-Pentanol

Find more mixtures with Cyclopentane.

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).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 ChEDL chemicals 1.5.2, from Daubert, T. E. Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes. J. Chem. Eng. Data 1996, 41, 365-372.
• 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).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• 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.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
• Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• On the behaviour of solutions of xenon in liquid cycloalkanes: Solubility of xenon in cyclopentane
• Phase equilibrium relations for binary mixed hydrate systemscomposed of carbon dioxide and cyclopentane derivatives
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Thermophysical study of 1,4-dioxane with cycloalkane mixtures
• Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Development of a Henry s constant correlation and solubility measurements of n-pentane, i-pentane, cyclopentane, n-hexane, and toluene in water
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Influence of temperature on the (liquid + liquid) equilibria of {3-methyl pentane + cyclopentane + methanol} ternary system at T = (293.15, 297.15, and 299.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• 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-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• The effect of the naphthenic ring on the VLE of (carbon dioxide + alkane) mixtures
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
• Correlation of Experimental Liquid Liquid Equilibrium Data for Ternary Systems Using NRTL and GMDH-Type Neural Network
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Liquid-Liquid Equilibria for the Binary Systems of N-Formylmorpholine with Cycloalkanes
• Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
• Saturated Liquid Viscosity of Cyclopentane and Isopentane
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
• Temperature and Density Dependence of the Viscosity of Cyclopentane
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
• Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
• Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Measurement of the Viscosity of Liquid Cyclopentane Obtained with a Vibrating Wire Viscometer at Temperatures between (273 and 353) K and Pressures below 45 MPa
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Speed of Sound Measurements and a Fundamental Equation of State for Cyclopentane
• Thermodynamics of Mixing Tetrahydrofuran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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