Chemical Properties of Cyclopentane, methyl- (CAS 96-37-7)

InChI

InChI=1S/C6H12/c1-6-4-2-3-5-6/h6H,2-5H2,1H3

InChI Key

GDOPTJXRTPNYNR-UHFFFAOYSA-N

Formula

C6H12

SMILES

CC1CCCC1

Molecular Weight¹

84.16

CAS

96-37-7

Other Names

• Methylcyclopentane
• UN 2298

• 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_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).
• γ : Surface Tension (N/m).
• 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.

Physical Properties

Property	Value	Unit	Source
ω	[0.2270; 0.2395]
ω	0.2390		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2395		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2270		ChemSep v8.3 pure component data Compiled value
ω	0.2310		KDB
Tig	602.04	K	KDB
AP	306.150	K	KDB
ΔcH°liquid	[-3956.00; -3936.20]	kJ/mol
ΔcH°liquid	-3938.30 ± 0.59	kJ/mol	NIST
ΔcH°liquid	-3937.70 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-3936.20 ± 1.70	kJ/mol	NIST
ΔcH°liquid	-3956.00	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	255.37	K	KDB
ΔfG°	[35.80; 36.30]	kJ/mol
ΔfG°	36.30	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	35.80	kJ/mol	KDB
Rg	3.1670		KDB
Δc,grossH	3938.32	kJ/mol	KDB
Δc,netH	3674.263	kJ/mol	KDB
ΔfH°gas	[-108.10; -106.00]	kJ/mol
ΔfH°gas	-106.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-106.80	kJ/mol	KDB
ΔfH°gas	-106.00	kJ/mol	NIST
ΔfH°gas	-106.70 ± 0.84	kJ/mol	NIST
ΔfH°gas	-108.10	kJ/mol	NIST
ΔfH°liquid	[-139.80; -137.70]	kJ/mol
ΔfH°liquid	-137.70 ± 0.71	kJ/mol	NIST
ΔfH°liquid	-138.40 ± 0.84	kJ/mol	NIST
ΔfH°liquid	-139.80 ± 1.70	kJ/mol	NIST
ΔfusH°	5.23	kJ/mol	Joback Calculated Property
ΔvapH°	[31.60; 31.78]	kJ/mol
ΔvapH°	31.78	kJ/mol	NIST
ΔvapH°	31.60	kJ/mol	NIST
ΔvapH°	31.70	kJ/mol	NIST
ΔvapH°	31.60 ± 0.10	kJ/mol	NIST
ΔvapH°	31.63	kJ/mol	NIST
ΔvapH°	31.70	kJ/mol	NIST
IE	[9.62; 10.45]	eV
IE	9.70 ± 0.10	eV	NIST
IE	9.62 ± 0.05	eV	NIST
IE	9.85	eV	NIST
IE	10.42	eV	NIST
IE	10.34 ± 0.04	eV	NIST
IE	10.45	eV	NIST
log10WS	[-3.30; -3.30]
log10WS	-3.30		Aq. Solubility Prediction
log10WS	-3.30		Estimated Solubility
logPoct/wat	2.196		Crippen Calculated Property
McVol	84.540	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	[3784.00; 3790.00]	kPa
Pc	3790.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Pc	3789.56	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3784.53	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3784.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3790.00	kPa	KDB
Pc	3790.00 ± 40.00	kPa	NIST
Pc	3784.00 ± 40.53	kPa	NIST
Pc	3785.91 ± 5.06	kPa	NIST
Ptriple	2.25e-07	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[264.01; 264.26]	kg/m3
ρc	264.26 ± 3.37	kg/m3	NIST
ρc	264.01 ± 4.21	kg/m3	NIST
ρc	264.26 ± 1.68	kg/m3	NIST
Inp	[600.00; 658.00]
Inp	Outlier 648.00		NIST
Inp	625.40		NIST
Inp	629.10		NIST
Inp	619.00		NIST
Inp	620.00		NIST
Inp	635.10		NIST
Inp	Outlier 648.40		NIST
Inp	Outlier 656.30		NIST
Inp	625.00		NIST
Inp	630.40		NIST
Inp	630.50		NIST
Inp	630.60		NIST
Inp	630.80		NIST
Inp	630.70		NIST
Inp	619.00		NIST
Inp	628.20		NIST
Inp	631.30		NIST
Inp	628.20		NIST
Inp	631.10		NIST
Inp	627.90		NIST
Inp	630.90		NIST
Inp	632.30		NIST
Inp	635.80		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	626.00		NIST
Inp	629.00		NIST
Inp	632.00		NIST
Inp	627.40		NIST
Inp	631.00		NIST
Inp	Outlier 658.00		NIST
Inp	Outlier 654.00		NIST
Inp	Outlier 654.00		NIST
Inp	Outlier 654.00		NIST
Inp	626.60		NIST
Inp	628.40		NIST
Inp	630.10		NIST
Inp	631.50		NIST
Inp	638.10		NIST
Inp	624.00		NIST
Inp	626.00		NIST
Inp	627.00		NIST
Inp	629.00		NIST
Inp	631.00		NIST
Inp	633.00		NIST
Inp	630.40		NIST
Inp	630.80		NIST
Inp	628.00		NIST
Inp	634.00		NIST
Inp	628.00		NIST
Inp	628.00		NIST
Inp	628.00		NIST
Inp	626.00		NIST
Inp	631.00		NIST
Inp	627.80		NIST
Inp	634.10		NIST
Inp	636.00		NIST
Inp	629.00		NIST
Inp	635.50		NIST
Inp	635.50		NIST
Inp	636.00		NIST
Inp	629.00		NIST
Inp	633.00		NIST
Inp	628.00		NIST
Inp	631.00		NIST
Inp	Outlier 651.00		NIST
Inp	647.00		NIST
Inp	629.00		NIST
Inp	631.00		NIST
Inp	632.00		NIST
Inp	633.00		NIST
Inp	635.00		NIST
Inp	629.00		NIST
Inp	628.60		NIST
Inp	633.00		NIST
Inp	635.00		NIST
Inp	629.00		NIST
Inp	631.00		NIST
Inp	631.00		NIST
Inp	631.00		NIST
Inp	634.00		NIST
Inp	624.00		NIST
Inp	629.00		NIST
Inp	632.00		NIST
Inp	635.00		NIST
Inp	623.00		NIST
Inp	624.00		NIST
Inp	626.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	633.00		NIST
Inp	635.00		NIST
Inp	630.00		NIST
Inp	Outlier 651.00		NIST
Inp	635.00		NIST
Inp	620.00		NIST
Inp	634.00		NIST
Inp	625.60		NIST
Inp	625.00		NIST
Inp	629.00		NIST
Inp	623.80		NIST
Inp	618.00		NIST
Inp	618.70		NIST
Inp	627.30		NIST
Inp	623.00		NIST
Inp	620.72		NIST
Inp	620.72		NIST
Inp	621.00		NIST
Inp	620.67		NIST
Inp	620.81		NIST
Inp	621.00		NIST
Inp	627.50		NIST
Inp	625.80		NIST
Inp	625.40		NIST
Inp	620.00		NIST
Inp	625.00		NIST
Inp	633.00		NIST
Inp	628.00		NIST
Inp	628.00		NIST
Inp	631.00		NIST
Inp	Outlier 600.00		NIST
Inp	Outlier 604.00		NIST
Inp	624.00		NIST
Inp	625.00		NIST
Inp	621.00		NIST
Inp	624.00		NIST
Inp	635.00		NIST
Inp	627.00		NIST
Inp	626.00		NIST
Inp	622.00		NIST
Inp	626.00		NIST
Inp	635.00		NIST
Inp	623.00		NIST
Inp	634.00		NIST
Inp	625.00		NIST
Inp	Outlier 651.00		NIST
Inp	628.00		NIST
Inp	627.00		NIST
Inp	624.00		NIST
Inp	624.00		NIST
Inp	619.20		NIST
Inp	635.00		NIST
Inp	630.00		NIST
Inp	621.00		NIST
Inp	627.00		NIST
Inp	625.00		NIST
Inp	629.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	619.00		NIST
Inp	619.00		NIST
Inp	620.00		NIST
Inp	631.00		NIST
Inp	Outlier 650.00		NIST
Inp	628.00		NIST
Inp	620.00		NIST
Inp	627.00		NIST
Inp	629.00		NIST
Inp	Outlier 650.00		NIST
Inp	640.00		NIST
Inp	623.00		NIST
Inp	640.00		NIST
Inp	635.00		NIST
Inp	Outlier 648.00		NIST
Inp	635.10		NIST
Inp	630.50		NIST
Inp	628.20		NIST
Inp	630.90		NIST
Inp	626.00		NIST
Inp	Outlier 658.00		NIST
Inp	628.40		NIST
Inp	630.40		NIST
Inp	628.00		NIST
Inp	634.10		NIST
Inp	636.00		NIST
Inp	Outlier 651.00		NIST
Inp	633.00		NIST
Inp	635.00		NIST
Inp	634.00		NIST
Inp	623.00		NIST
Inp	625.60		NIST
Inp	620.00		NIST
Ip	[675.00; 675.00]
Ip	675.00		NIST
Ip	675.00		NIST
S°liquid	[247.70; 247.78]	J/mol×K
S°liquid	247.78	J/mol×K	NIST
S°liquid	247.70	J/mol×K	NIST
Tboil	[343.00; 353.25]	K
Tboil	344.96	K	Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
Tboil	344.98	K	ChemSep v8.3 pure component data Compiled value
Tboil	344.90	K	KDB
Tboil	345.00	K	NIST
Tboil	345.00	K	NIST
Tboil	344.97 ± 0.15	K	NIST
Tboil	344.95 ± 0.30	K	NIST
Tboil	344.97 ± 0.30	K	NIST
Tboil	344.95 ± 0.50	K	NIST
Tboil	344.96 ± 0.10	K	NIST
Tboil	343.00 ± 2.00	K	NIST
Tboil	344.93 ± 0.20	K	NIST
Tboil	344.95 ± 0.20	K	NIST
Tboil	345.00 ± 0.30	K	NIST
Tboil	345.00 ± 0.20	K	NIST
Tboil	Outlier 353.25 ± 0.30	K	NIST
Tboil	344.97 ± 0.05	K	NIST
Tboil	345.20 ± 0.40	K	NIST
Tboil	344.94 ± 0.30	K	NIST
Tboil	344.96 ± 0.01	K	NIST
Tboil	344.80 ± 0.50	K	NIST
Tboil	345.20 ± 0.50	K	NIST
Tboil	344.96 ± 0.05	K	NIST
Tboil	345.00 ± 0.20	K	NIST
Tboil	344.96 ± 0.20	K	NIST
Tboil	344.95 ± 0.30	K	NIST
Tboil	344.95 ± 0.30	K	NIST
Tboil	344.96 ± 0.20	K	NIST
Tboil	344.97 ± 0.30	K	NIST
Tboil	345.00 ± 0.20	K	NIST
Tboil	345.10 ± 0.40	K	NIST
Tboil	345.05 ± 0.20	K	NIST
Tboil	345.15 ± 0.20	K	NIST
Tboil	344.95 ± 0.50	K	NIST
Tboil	345.05 ± 0.50	K	NIST
Tboil	346.65 ± 0.70	K	NIST
Tboil	346.15 ± 1.50	K	NIST
Tboil	345.05 ± 1.00	K	NIST
Tboil	345.15 ± 0.50	K	NIST
Tboil	345.00 ± 2.00	K	NIST
Tboil	345.15 ± 1.00	K	NIST
Tboil	345.00 ± 3.00	K	NIST
Tboil	343.65 ± 2.00	K	NIST
Tboil	344.00 ± 5.00	K	NIST
Tc	[532.70; 532.79]	K
Tc	532.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc	532.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	532.79	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	532.79	K	ChemSep v8.3 pure component data Compiled value
Tc	532.70	K	KDB
Tc	532.70 ± 0.20	K	NIST
Tc	532.70	K	NIST
Tc	532.73 ± 0.30	K	NIST
Tc	532.70 ± 0.20	K	NIST
Tc	532.76 ± 0.05	K	NIST
Tfus	[129.00; 279.65]	K
Tfus	130.65	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	130.73	K	ChemSep v8.3 pure component data Compiled value
Tfus	130.60	K	KDB
Tfus	130.65	K	Aq. Solubility Prediction
Tfus	Outlier 279.65 ± 0.40	K	NIST
Tfus	130.20 ± 0.20	K	NIST
Tfus	130.70 ± 0.08	K	NIST
Tfus	130.70 ± 0.08	K	NIST
Tfus	130.69 ± 0.30	K	NIST
Tfus	133.40 ± 0.40	K	NIST
Tfus	130.71 ± 0.08	K	NIST
Tfus	130.71 ± 0.05	K	NIST
Tfus	130.71 ± 0.40	K	NIST
Tfus	130.71 ± 0.20	K	NIST
Tfus	130.69 ± 0.08	K	NIST
Tfus	130.69 ± 0.05	K	NIST
Tfus	130.20 ± 0.20	K	NIST
Tfus	130.71 ± 0.20	K	NIST
Tfus	130.68 ± 0.40	K	NIST
Tfus	130.69 ± 0.20	K	NIST
Tfus	130.68 ± 0.01	K	NIST
Tfus	130.68 ± 0.08	K	NIST
Tfus	130.67 ± 0.06	K	NIST
Tfus	130.69 ± 0.04	K	NIST
Tfus	130.72 ± 0.10	K	NIST
Tfus	130.62 ± 0.20	K	NIST
Tfus	130.45 ± 0.30	K	NIST
Tfus	130.45 ± 0.30	K	NIST
Tfus	130.45 ± 0.40	K	NIST
Tfus	130.75 ± 0.40	K	NIST
Tfus	130.45 ± 0.30	K	NIST
Tfus	132.15 ± 2.00	K	NIST
Tfus	133.95 ± 0.40	K	NIST
Tfus	129.00 ± 2.00	K	NIST
Tfus	130.20 ± 1.00	K	NIST
Tfus	Outlier 273.14 ± 2.00	K	NIST
Tfus	132.00 ± 2.00	K	NIST
Tfus	133.00 ± 0.30	K	NIST
Tfus	132.15 ± 0.50	K	NIST
Ttriple	[130.10; 130.74]	K
Ttriple	130.74	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	130.73	K	ChemSep v8.3 pure component data Compiled value
Ttriple	130.71 ± 0.00	K	NIST
Ttriple	130.69 ± 0.05	K	NIST
Ttriple	130.71 ± 0.03	K	NIST
Ttriple	130.71 ± 0.10	K	NIST
Ttriple	130.10 ± 0.20	K	NIST
Ttriple	130.10 ± 0.20	K	NIST
UQi	3.01		ChemSep v8.3 pure component data Compiled value
URi	3.97		ChemSep v8.3 pure component data Compiled value
Vc	[0.318; 0.319]	m3/kmol
Vc	0.318	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Vc	0.318	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.319	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.318	m3/kmol	KDB
Vc	0.318	m3/kmol	NIST
VCOSTALD	0.32	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.23		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2720000; 0.2721120]
Zc	0.2720000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Zc	0.2720000		ChemSep v8.3 pure component data Compiled value
Zc	0.2721120		KDB
Zra	[0.27; 0.27]
Zra	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[124.24; 178.17]	J/mol×K	[333.20; 471.05]
Cp,gas	124.24 ± 0.25	J/mol×K	333.20	NIST
Cp,gas	136.21 ± 0.27	J/mol×K	362.55	NIST
Cp,gas	152.15 ± 0.30	J/mol×K	402.35	NIST
Cp,gas	165.21 ± 0.33	J/mol×K	436.25	NIST
Cp,gas	178.17 ± 0.36	J/mol×K	471.05	NIST
Cp,liquid	[125.10; 188.70]	J/mol×K	[140.00; 370.00]
Cp,liquid	125.10	J/mol×K	140.00	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	125.40	J/mol×K	150.00	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	126.00	J/mol×K	160.00	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	126.90	J/mol×K	170.00	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	128.10	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	129.50	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	131.10	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	133.00	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	135.10	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	137.50	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	140.00	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	142.80	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	145.80	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	148.90	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	149.90	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	152.20	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	155.70	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	157.66	J/mol×K	293.15	NIST
Cp,liquid	157.30	J/mol×K	295.70	NIST
Cp,liquid	158.70	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	158.70	J/mol×K	298.15	NIST
Cp,liquid	159.12	J/mol×K	299.80	NIST
Cp,liquid	159.40	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	163.20	J/mol×K	310.00	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	167.10	J/mol×K	320.00	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	171.20	J/mol×K	330.00	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	175.40	J/mol×K	340.00	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	179.70	J/mol×K	350.00	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	184.20	J/mol×K	360.00	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	188.70	J/mol×K	370.00	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
η	[0.0004500; 0.0005040]	Pa×s	[293.15; 303.15]
η	0.0005040	Pa×s	293.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0005040	Pa×s	293.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0004760	Pa×s	298.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0004760	Pa×s	298.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0004500	Pa×s	303.15	Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η	0.0004500	Pa×s	303.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
ΔfusH	[6.88; 6.93]	kJ/mol	[130.10; 130.73]
ΔfusH	6.88	kJ/mol	130.10	NIST
ΔfusH	6.93	kJ/mol	130.70	NIST
ΔfusH	6.93	kJ/mol	130.70	NIST
ΔfusH	6.93	kJ/mol	130.73	NIST
ΔvapH	[29.08; 31.90]	kJ/mol	[304.00; 345.00]
ΔvapH	31.33 ± 0.02	kJ/mol	304.00	NIST
ΔvapH	31.30 ± 0.10	kJ/mol	304.00	NIST
ΔvapH	31.90	kJ/mol	317.00	NIST
ΔvapH	31.40	kJ/mol	322.50	NIST
ΔvapH	30.20 ± 0.10	kJ/mol	326.00	NIST
ΔvapH	29.08	kJ/mol	345.00	KDB
ΔvapH	29.08	kJ/mol	345.00	NIST
ΔvapH	29.10 ± 0.10	kJ/mol	345.00	NIST
Pvap	101.30	kPa	344.96	Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
n0	[1.40670; 1.40700]		[298.15; 298.15]
n0	1.40670		298.15	Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
n0	1.40700		298.15	KDB
ρl	754.00	kg/m3	289.00	KDB
ΔfusS	[52.90; 53.00]	J/mol×K	[130.10; 130.73]
ΔfusS	52.90	J/mol×K	130.10	NIST
ΔfusS	53.00	J/mol×K	130.73	NIST
γ	0.02	N/m	293.20	KDB
λliquid	[0.11; 0.13]	W/m×K	[258.71; 312.99]
λliquid	0.13	W/m×K	258.71	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	258.96	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	259.11	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	277.00	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	277.24	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	277.41	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	294.90	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	295.15	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	295.32	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	312.57	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	312.82	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	312.99	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[73.64; 355.43]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			5.56240e+01
Coefficient B			-6.76340e+02
Coefficient C			6.29924e+00
Coefficient D			-1.36300e-04
Coefficient E			2.63210e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	73.64	J/mol×K	200.00	Calculated Property
Cp,gas	128.73	J/mol×K	344.44	Calculated Property
Cp,gas	184.07	J/mol×K	488.89	Calculated Property
Cp,gas	229.02	J/mol×K	633.33	Calculated Property
Cp,gas	264.05	J/mol×K	777.78	Calculated Property
Cp,gas	291.32	J/mol×K	922.22	Calculated Property
Cp,gas	312.79	J/mol×K	1066.67	Calculated Property
Cp,gas	329.95	J/mol×K	1211.11	Calculated Property
Cp,gas	343.90	J/mol×K	1355.56	Calculated Property
Cp,gas	355.43	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[125.16; 186.67]	J/mol×K	[126.58; 366.48]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.02830e+02
Coefficient B			3.17530e+02
Coefficient C			-1.90876e+00
Coefficient D			2.23680e-02
Coefficient E			-2.02980e-05
Temperature range, min.			126.58
Temperature range, max.			366.48
Cp,liquid	125.16	J/mol×K	126.58	Calculated Property
Cp,liquid	125.35	J/mol×K	153.24	Calculated Property
Cp,liquid	127.94	J/mol×K	179.89	Calculated Property
Cp,liquid	132.28	J/mol×K	206.55	Calculated Property
Cp,liquid	138.18	J/mol×K	233.20	Calculated Property
Cp,liquid	145.57	J/mol×K	259.86	Calculated Property
Cp,liquid	154.35	J/mol×K	286.51	Calculated Property
Cp,liquid	164.35	J/mol×K	313.17	Calculated Property
Cp,liquid	175.27	J/mol×K	339.82	Calculated Property
Cp,liquid	186.67	J/mol×K	366.48	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0009293; 0.0001544]	Pa×s	[248.15; 426.23]	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			-9.22880e+00
Coefficient B			8.46650e+02
Coefficient C			-1.86120e-01
Coefficient D			-2.23830e-06
Coefficient E			2.00000e+00
Temperature range, min.			248.15
Temperature range, max.			426.23
η	0.0009293	Pa×s	248.15	Calculated Property
η	0.0006960	Pa×s	267.94	Calculated Property
η	0.0005393	Pa×s	287.72	Calculated Property
η	0.0004293	Pa×s	307.51	Calculated Property
η	0.0003493	Pa×s	327.30	Calculated Property
η	0.0002894	Pa×s	347.08	Calculated Property
η	0.0002433	Pa×s	366.87	Calculated Property
η	0.0002070	Pa×s	386.66	Calculated Property
η	0.0001780	Pa×s	406.45	Calculated Property
η	0.0001544	Pa×s	426.23	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[41.14; 1.28]	kJ/mol	[130.72; 532.70]	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			4.98643e+01
Coefficient B			7.54250e-01
Coefficient C			-1.86227e-01
Coefficient D			-5.06210e-01
Coefficient E			3.59990e-01
Critical temperature, Tc (K)			5.32790e+02
Temperature range, min.			130.72
Temperature range, max.			532.70
ΔvapH	41.14	kJ/mol	130.72	Calculated Property
ΔvapH	38.45	kJ/mol	175.38	Calculated Property
ΔvapH	35.91	kJ/mol	220.05	Calculated Property
ΔvapH	33.46	kJ/mol	264.71	Calculated Property
ΔvapH	31.03	kJ/mol	309.38	Calculated Property
ΔvapH	28.49	kJ/mol	354.04	Calculated Property
ΔvapH	25.63	kJ/mol	398.71	Calculated Property
ΔvapH	22.09	kJ/mol	443.37	Calculated Property
ΔvapH	16.95	kJ/mol	488.04	Calculated Property
ΔvapH	1.28	kJ/mol	532.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[248.23; 369.20]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42458e+01
Coefficient B			-3.00275e+03
Coefficient C			-3.31070e+01
Temperature range, min.			248.23
Temperature range, max.			369.20
Pvap	1.33	kPa	248.23	Calculated Property
Pvap	3.03	kPa	261.67	Calculated Property
Pvap	6.28	kPa	275.11	Calculated Property
Pvap	12.07	kPa	288.55	Calculated Property
Pvap	21.73	kPa	301.99	Calculated Property
Pvap	36.97	kPa	315.44	Calculated Property
Pvap	59.95	kPa	328.88	Calculated Property
Pvap	93.21	kPa	342.32	Calculated Property
Pvap	139.68	kPa	355.76	Calculated Property
Pvap	202.66	kPa	369.20	Calculated Property
Pvap	[1.40e-07; 3755.79]	kPa	[130.73; 532.70]	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			5.62743e+01
Coefficient B			-5.47037e+03
Coefficient C			-6.21513e+00
Coefficient D			4.38474e-06
Coefficient E			2.00000e+00
Temperature range, min.			130.73
Temperature range, max.			532.70
Pvap	1.40e-07	kPa	130.73	Calculated Property
Pvap	1.01e-03	kPa	175.39	Calculated Property
Pvap	0.15	kPa	220.06	Calculated Property
Pvap	3.47	kPa	264.72	Calculated Property
Pvap	29.12	kPa	309.38	Calculated Property
Pvap	133.44	kPa	354.05	Calculated Property
Pvap	417.16	kPa	398.71	Calculated Property
Pvap	1012.91	kPa	443.37	Calculated Property
Pvap	2070.63	kPa	488.04	Calculated Property
Pvap	3755.79	kPa	532.70	Calculated Property
Pvap	[6.70e-08; 3779.90]	kPa	[130.73; 532.79]	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			7.27581e+01
Coefficient B			-6.08643e+03
Coefficient C			-8.79214e+00
Coefficient D			7.40207e-06
Coefficient E			0.00000e+00
Temperature range, min.			130.73
Temperature range, max.			532.79
Pvap	6.70e-08	kPa	130.73	Calculated Property
Pvap	7.90e-04	kPa	175.40	Calculated Property
Pvap	0.14	kPa	220.08	Calculated Property
Pvap	3.45	kPa	264.75	Calculated Property
Pvap	29.26	kPa	309.42	Calculated Property
Pvap	133.16	kPa	354.10	Calculated Property
Pvap	412.18	kPa	398.77	Calculated Property
Pvap	996.24	kPa	443.44	Calculated Property
Pvap	2047.35	kPa	488.12	Calculated Property
Pvap	3779.90	kPa	532.79	Calculated Property
Pvap	[11.69; 103.90]	kPa	[288.18; 345.78]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37873e+01
Coefficient B			-2.73100e+03
Coefficient C			-4.71080e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			288.18
Temperature range, max.			345.78
Pvap	11.69	kPa	288.18	Calculated Property
Pvap	15.67	kPa	294.58	Calculated Property
Pvap	20.69	kPa	300.98	Calculated Property
Pvap	26.96	kPa	307.38	Calculated Property
Pvap	34.68	kPa	313.78	Calculated Property
Pvap	44.09	kPa	320.18	Calculated Property
Pvap	55.44	kPa	326.58	Calculated Property
Pvap	68.99	kPa	332.98	Calculated Property
Pvap	85.05	kPa	339.38	Calculated Property
Pvap	103.90	kPa	345.78	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[880.06; 270.74]	kg/m3	[130.73; 532.70]	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			5.34034e+01
Coefficient B			2.34770e-01
Coefficient C			5.32790e+02
Coefficient D			2.43940e-01
Temperature range, min.			130.73
Temperature range, max.			532.70
ρl	880.06	kg/m3	130.73	Calculated Property
ρl	846.98	kg/m3	175.39	Calculated Property
ρl	812.05	kg/m3	220.06	Calculated Property
ρl	774.80	kg/m3	264.72	Calculated Property
ρl	734.59	kg/m3	309.38	Calculated Property
ρl	690.38	kg/m3	354.05	Calculated Property
ρl	640.36	kg/m3	398.71	Calculated Property
ρl	580.94	kg/m3	443.37	Calculated Property
ρl	502.19	kg/m3	488.04	Calculated Property
ρl	270.74	kg/m3	532.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[130.95; 344.95]	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			5.63973e-02
Coefficient B			-1.16300e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			130.95
Temperature range, max.			344.95
γ	0.04	N/m	130.95	Calculated Property
γ	0.04	N/m	154.73	Calculated Property
γ	0.04	N/m	178.51	Calculated Property
γ	0.03	N/m	202.28	Calculated Property
γ	0.03	N/m	226.06	Calculated Property
γ	0.03	N/m	249.84	Calculated Property
γ	0.02	N/m	273.62	Calculated Property
γ	0.02	N/m	297.39	Calculated Property
γ	0.02	N/m	321.17	Calculated Property
γ	0.02	N/m	344.95	Calculated Property
γ	[0.04; 1.81e-05]	N/m	[130.73; 528.68]	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			-9.31680e-03
Coefficient B			2.64030e+01
Coefficient C			-3.08840e+00
Coefficient D			3.62460e-04
Coefficient E			-6.53720e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 532.7 K.
Temperature range, min.			130.73
Temperature range, max.			528.68
γ	0.04	N/m	130.73	Calculated Property
γ	0.04	N/m	174.95	Calculated Property
γ	0.03	N/m	219.16	Calculated Property
γ	0.03	N/m	263.38	Calculated Property
γ	0.02	N/m	307.60	Calculated Property
γ	0.02	N/m	351.81	Calculated Property
γ	0.01	N/m	396.03	Calculated Property
γ	0.01	N/m	440.25	Calculated Property
γ	0.00	N/m	484.46	Calculated Property
γ	1.81e-05	N/m	528.68	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.10]	W/m×K	[130.73; 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			7.66530e-03
Coefficient B			4.85210e-01
Coefficient C			4.79720e+02
Coefficient D			6.58190e+05
Temperature range, min.			130.73
Temperature range, max.			1000.00
λgas	0.00	W/m×K	130.73	Calculated Property
λgas	0.01	W/m×K	227.32	Calculated Property
λgas	0.01	W/m×K	323.90	Calculated Property
λgas	0.02	W/m×K	420.49	Calculated Property
λgas	0.04	W/m×K	517.07	Calculated Property
λgas	0.05	W/m×K	613.66	Calculated Property
λgas	0.06	W/m×K	710.24	Calculated Property
λgas	0.08	W/m×K	806.83	Calculated Property
λgas	0.09	W/m×K	903.41	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.11]	W/m×K	[130.73; 344.95]	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			-4.08150e-02
Coefficient B			4.48080e+00
Coefficient C			-1.54340e+00
Coefficient D			-5.04940e-04
Coefficient E			-1.76710e-06
Temperature range, min.			130.73
Temperature range, max.			344.95
λliquid	0.16	W/m×K	130.73	Calculated Property
λliquid	0.15	W/m×K	154.53	Calculated Property
λliquid	0.15	W/m×K	178.33	Calculated Property
λliquid	0.14	W/m×K	202.14	Calculated Property
λliquid	0.14	W/m×K	225.94	Calculated Property
λliquid	0.13	W/m×K	249.74	Calculated Property
λliquid	0.12	W/m×K	273.54	Calculated Property
λliquid	0.12	W/m×K	297.35	Calculated Property
λliquid	0.11	W/m×K	321.15	Calculated Property
λliquid	0.11	W/m×K	344.95	Calculated Property

Similar Compounds

Find more compounds similar to Cyclopentane, methyl-.

Mixtures

• Thiophene, 3-methyl- + Cyclopentane, methyl-
• Cyclopentane, methyl- + Thiophene, tetrahydro-, 1,1-dioxide
• Cyclopentane, methyl- + Dimethyl Sulfoxide
• Cyclopentane, methyl- + Acetone
• Cyclopentane, methyl- + 2-Butanone
• Cyclopentane, methyl- + 2-Pentanone
• Cyclopentane, methyl- + 1-Butanethiol
• Cyclopentane, methyl- + Ethanol
• Cyclopentane, methyl- + 1-Propanol
• Cyclopentane, methyl- + 1-Butanol
• Cyclopentane, methyl- + 2-Propanol
• Cyclopentane, methyl- + 2-Pentanol
• Cyclopentane, methyl- + Ethanol, 2-methoxy-
• Cyclopentane, methyl- + N-Formylmorpholine
• Cyclopentane, methyl- + Ethane, 1,2-dimethoxy-
• Cyclopentane, methyl- + 2-Butanol

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
• Liquid liquid equilibria for the binary systems of sulfolane with branched cycloalkanes
• Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
• Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
• Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
• Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Isobaric Vapor-Liquid Equilibrium Data for Two Binary Systems n-Hexane + 1,2-Dimethoxyethane and Methylcyclopentane + 1,2-Dimethoxyethane at 101.3 kPa
• Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
• Liquid-Liquid Equilibria for the Binary Systems of N-Formylmorpholine with Branched Cycloalkanes
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• 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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