Chemical Properties of Pentane, 2,4-dimethyl- (CAS 108-08-7)

InChI

InChI=1S/C7H16/c1-6(2)5-7(3)4/h6-7H,5H2,1-4H3

InChI Key

BZHMBWZPUJHVEE-UHFFFAOYSA-N

Formula

C7H16

SMILES

CC(C)CC(C)C

Molecular Weight¹

100.20

CAS

108-08-7

Other Names

• 2,4-dimethylpentane

• ω : Acentric Factor.
• 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).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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.
• 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°_gas : Molar entropy at standard conditions (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	[0.3020; 0.3060]
ω	0.3060		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3059		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.3040		ChemSep v8.3 pure component data Compiled value
ω	0.3020		KDB
AP	351.950	K	KDB
ΔcH°liquid	[-4806.29; -4802.00]	kJ/mol
ΔcH°liquid	-4806.29 ± 0.84	kJ/mol	NIST
ΔcH°liquid	-4802.00 ± 1.00	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
ΔfG°	[3.10; 3.31]	kJ/mol
ΔfG°	3.31	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	3.10	kJ/mol	KDB
Δc,grossH	4806.29	kJ/mol	KDB
Δc,netH	4454.161	kJ/mol	KDB
ΔfH°gas	[-205.10; -201.67]	kJ/mol
ΔfH°gas	-201.67	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-202.10	kJ/mol	KDB
ΔfH°gas	-202.10 ± 0.96	kJ/mol	NIST
ΔfH°gas	-205.10	kJ/mol	NIST
ΔfH°liquid	[-238.00; -235.00]	kJ/mol
ΔfH°liquid	-235.00 ± 0.96	kJ/mol	NIST
ΔfH°liquid	-238.00 ± 1.00	kJ/mol	NIST
ΔfusH°	6.84	kJ/mol	Joback Calculated Property
ΔvapH°	[32.70; 33.02]	kJ/mol
ΔvapH°	33.02	kJ/mol	NIST
ΔvapH°	32.70 ± 0.10	kJ/mol	NIST
ΔvapH°	32.90 ± 0.10	kJ/mol	NIST
ΔvapH°	32.88	kJ/mol	NIST
IE	9.92	eV	Relay (1.0) Calculated Property
log10WS	[-4.26; -4.26]
log10WS	-4.26		Aq. Solubility Prediction
log10WS	-4.26		Estimated Solubility
logPoct/wat	2.688		Crippen Calculated Property
McVol	109.490	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[2736.53; 2776.30]	kPa
Pc	2740.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Pc	2739.83	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2736.53	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2740.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2740.00	kPa	KDB
Pc	2740.00 ± 50.00	kPa	NIST
Pc	2736.70 ± 40.53	kPa	NIST
Pc	Outlier 2776.30 ± 50.66	kPa	NIST
Ptriple	6.70e-06	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[240.48; 240.48]	kg/m3
ρc	240.48 ± 5.01	kg/m3	NIST
ρc	240.48 ± 5.01	kg/m3	NIST
Inp	[620.30; 641.00]
Inp	628.90		NIST
Inp	630.00		NIST
Inp	628.00		NIST
Inp	628.00		NIST
Inp	632.00		NIST
Inp	626.30		NIST
Inp	630.30		NIST
Inp	634.90		NIST
Inp	631.00		NIST
Inp	630.80		NIST
Inp	631.00		NIST
Inp	630.90		NIST
Inp	630.70		NIST
Inp	629.30		NIST
Inp	628.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	630.40		NIST
Inp	630.50		NIST
Inp	631.30		NIST
Inp	629.80		NIST
Inp	630.50		NIST
Inp	629.30		NIST
Inp	629.80		NIST
Inp	631.00		NIST
Inp	632.00		NIST
Inp	633.00		NIST
Inp	630.00		NIST
Inp	630.20		NIST
Inp	629.90		NIST
Inp	630.40		NIST
Inp	630.90		NIST
Inp	631.50		NIST
Inp	631.00		NIST
Inp	631.00		NIST
Inp	632.00		NIST
Inp	632.00		NIST
Inp	632.00		NIST
Inp	633.00		NIST
Inp	628.70		NIST
Inp	629.00		NIST
Inp	629.30		NIST
Inp	629.60		NIST
Inp	630.00		NIST
Inp	630.30		NIST
Inp	631.00		NIST
Inp	630.90		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	632.00		NIST
Inp	632.00		NIST
Inp	630.00		NIST
Inp	630.50		NIST
Inp	631.20		NIST
Inp	631.90		NIST
Inp	632.60		NIST
Inp	633.40		NIST
Inp	634.20		NIST
Inp	633.70		NIST
Inp	633.10		NIST
Inp	632.20		NIST
Inp	631.50		NIST
Inp	630.60		NIST
Inp	629.60		NIST
Inp	627.00		NIST
Inp	631.00		NIST
Inp	629.00		NIST
Inp	629.00		NIST
Inp	632.00		NIST
Inp	631.00		NIST
Inp	632.00		NIST
Inp	632.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	631.00		NIST
Inp	626.90		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	633.19		NIST
Inp	633.65		NIST
Inp	633.57		NIST
Inp	632.42		NIST
Inp	632.98		NIST
Inp	631.00		NIST
Inp	631.00		NIST
Inp	626.00		NIST
Inp	627.00		NIST
Inp	627.00		NIST
Inp	628.00		NIST
Inp	628.00		NIST
Inp	629.80		NIST
Inp	628.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	629.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	629.00		NIST
Inp	630.00		NIST
Inp	629.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	629.00		NIST
Inp	629.00		NIST
Inp	632.00		NIST
Inp	631.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	633.00		NIST
Inp	631.00		NIST
Inp	627.00		NIST
Inp	630.00		NIST
Inp	Outlier 623.00		NIST
Inp	Outlier 621.00		NIST
Inp	630.60		NIST
Inp	633.00		NIST
Inp	627.10		NIST
Inp	Outlier 620.63		NIST
Inp	Outlier 621.45		NIST
Inp	Outlier 621.20		NIST
Inp	625.80		NIST
Inp	Outlier 620.30		NIST
Inp	Outlier 623.10		NIST
Inp	623.73		NIST
Inp	623.75		NIST
Inp	630.00		NIST
Inp	624.00		NIST
Inp	624.00		NIST
Inp	Outlier 623.00		NIST
Inp	626.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	632.00		NIST
Inp	630.00		NIST
Inp	Outlier 621.00		NIST
Inp	629.00		NIST
Inp	627.00		NIST
Inp	631.00		NIST
Inp	625.00		NIST
Inp	630.00		NIST
Inp	634.00		NIST
Inp	631.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	630.00		NIST
Inp	630.00		NIST
Inp	626.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	629.00		NIST
Inp	629.00		NIST
Inp	630.00		NIST
Inp	626.00		NIST
Inp	628.00		NIST
Inp	624.00		NIST
Inp	632.00		NIST
Inp	630.00		NIST
Inp	Outlier 640.00		NIST
Inp	Outlier 641.00		NIST
Inp	631.00		NIST
Inp	627.10		NIST
Inp	Outlier 620.30		NIST
Inp	624.00		NIST
Ip	[609.00; 611.00]
Ip	609.00		NIST
Ip	611.00		NIST
Ip	611.00		NIST
S°gas	396.73	J/mol×K	NIST
S°liquid	[291.60; 303.17]	J/mol×K
S°liquid	303.17	J/mol×K	NIST
S°liquid	291.60	J/mol×K	NIST
Tboil	[352.10; 354.25]	K
Tboil	353.62	K	ChemSep v8.3 pure component data Compiled value
Tboil	353.64	K	KDB
Tboil	353.70	K	NIST
Tboil	353.70	K	NIST
Tboil	353.65 ± 0.30	K	NIST
Tboil	353.65 ± 0.20	K	NIST
Tboil	353.65 ± 0.20	K	NIST
Tboil	353.65 ± 0.30	K	NIST
Tboil	353.75 ± 0.60	K	NIST
Tboil	353.75 ± 0.50	K	NIST
Tboil	353.62 ± 0.20	K	NIST
Tboil	353.62 ± 0.30	K	NIST
Tboil	353.45 ± 0.50	K	NIST
Tboil	353.70 ± 0.20	K	NIST
Tboil	354.00 ± 0.50	K	NIST
Tboil	353.25 ± 0.50	K	NIST
Tboil	Outlier 352.65 ± 2.00	K	NIST
Tboil	354.25 ± 0.20	K	NIST
Tboil	353.75 ± 0.30	K	NIST
Tboil	353.60 ± 0.50	K	NIST
Tboil	353.70 ± 0.50	K	NIST
Tboil	353.70 ± 0.30	K	NIST
Tboil	353.80 ± 0.50	K	NIST
Tboil	353.65 ± 0.10	K	NIST
Tboil	353.66 ± 0.10	K	NIST
Tboil	353.95 ± 0.50	K	NIST
Tboil	353.55 ± 0.30	K	NIST
Tboil	353.65 ± 0.05	K	NIST
Tboil	353.85 ± 0.30	K	NIST
Tboil	353.95 ± 0.50	K	NIST
Tboil	353.80 ± 0.30	K	NIST
Tboil	352.95 ± 0.60	K	NIST
Tboil	353.66 ± 0.05	K	NIST
Tboil	353.80 ± 0.20	K	NIST
Tboil	353.65 ± 0.50	K	NIST
Tboil	353.65 ± 0.30	K	NIST
Tboil	353.64 ± 0.10	K	NIST
Tboil	353.75 ± 0.50	K	NIST
Tboil	354.00 ± 0.60	K	NIST
Tboil	353.75 ± 0.20	K	NIST
Tboil	353.75 ± 0.50	K	NIST
Tboil	353.75 ± 0.20	K	NIST
Tboil	353.56 ± 0.40	K	NIST
Tboil	Outlier 352.10 ± 0.20	K	NIST
Tboil	353.65 ± 0.50	K	NIST
Tboil	Outlier 352.60 ± 1.00	K	NIST
Tboil	353.95 ± 0.50	K	NIST
Tboil	353.95 ± 0.50	K	NIST
Tboil	353.95 ± 0.50	K	NIST
Tboil	353.95 ± 0.30	K	NIST
Tc	[519.70; 521.70]	K
Tc	519.80	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc	519.80	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	519.79	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	519.70	K	ChemSep v8.3 pure component data Compiled value
Tc	519.80	K	KDB
Tc	519.80 ± 0.50	K	NIST
Tc	519.73 ± 0.40	K	NIST
Tc	Outlier 521.70 ± 2.00	K	NIST
Tc	520.25 ± 0.50	K	NIST
Tfus	[148.33; 154.15]	K
Tfus	153.25	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	153.91	K	ChemSep v8.3 pure component data Compiled value
Tfus	153.20	K	KDB
Tfus	152.52	K	Aq. Solubility Prediction
Tfus	153.90 ± 0.04	K	NIST
Tfus	153.90 ± 0.03	K	NIST
Tfus	153.92 ± 0.02	K	NIST
Tfus	153.83 ± 0.07	K	NIST
Tfus	153.87 ± 0.05	K	NIST
Tfus	153.83 ± 0.15	K	NIST
Tfus	153.58 ± 0.30	K	NIST
Tfus	153.29 ± 0.10	K	NIST
Tfus	153.88 ± 0.30	K	NIST
Tfus	153.87 ± 0.04	K	NIST
Tfus	153.88 ± 0.03	K	NIST
Tfus	153.92 ± 0.02	K	NIST
Tfus	153.85 ± 0.60	K	NIST
Tfus	152.75 ± 0.50	K	NIST
Tfus	153.65 ± 0.20	K	NIST
Tfus	154.05 ± 0.30	K	NIST
Tfus	154.05 ± 0.20	K	NIST
Tfus	Outlier 148.33 ± 0.50	K	NIST
Tfus	154.15 ± 2.00	K	NIST
Tfus	153.95 ± 0.50	K	NIST
Tfus	153.75 ± 1.00	K	NIST
Tfus	152.55 ± 0.50	K	NIST
Tfus	Outlier 149.75 ± 0.50	K	NIST
Tfus	Outlier 149.75 ± 0.50	K	NIST
Tfus	Outlier 149.75 ± 2.00	K	NIST
Tfus	153.75 ± 0.50	K	NIST
Tfus	152.55 ± 0.50	K	NIST
Ttriple	[152.50; 153.98]	K
Ttriple	153.98	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	153.91	K	ChemSep v8.3 pure component data Compiled value
Ttriple	153.94 ± 0.08	K	NIST
Ttriple	153.96 ± 0.06	K	NIST
Ttriple	153.94 ± 0.04	K	NIST
Ttriple	153.96 ± 0.03	K	NIST
Ttriple	153.95 ± 0.06	K	NIST
Ttriple	153.97 ± 0.03	K	NIST
Ttriple	Outlier 152.50 ± 0.20	K	NIST
UQi	4.39		ChemSep v8.3 pure component data Compiled value
URi	5.17		ChemSep v8.3 pure component data Compiled value
Vc	[0.417; 0.418]	m3/kmol
Vc	0.418	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Vc	0.418	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	Outlier 0.417	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.418	m3/kmol	KDB
Vc	0.418	m3/kmol	NIST
VCOSTALD	0.43	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.30		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2650000; 0.2650050]
Zc	0.2650000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Zc	0.2650000		ChemSep v8.3 pure component data Compiled value
Zc	0.2650050		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,liquid	[220.90; 224.22]	J/mol×K	[294.40; 298.15]
Cp,liquid	220.90	J/mol×K	294.40	NIST
Cp,liquid	224.22	J/mol×K	298.15	NIST
Csat	[169.50; 229.90]	J/mol×K	[160.00; 310.00]
Csat	169.50	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
Csat	172.50	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
Csat	175.70	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
Csat	179.10	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
Csat	182.60	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
Csat	186.30	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
Csat	190.20	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
Csat	194.10	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
Csat	198.30	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
Csat	202.50	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
Csat	206.80	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
Csat	211.30	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
Csat	212.70	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
Csat	215.80	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
Csat	220.50	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
Csat	224.30	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
Csat	225.20	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
Csat	229.90	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
ΔfusH	[6.69; 6.85]	kJ/mol	[152.50; 154.00]
ΔfusH	6.69	kJ/mol	152.50	NIST
ΔfusH	6.84	kJ/mol	153.97	NIST
ΔfusH	6.85	kJ/mol	154.00	NIST
ΔvapH	[29.50; 33.30]	kJ/mol	[308.00; 353.80]
ΔvapH	32.30 ± 0.10	kJ/mol	308.00	NIST
ΔvapH	31.90 ± 0.10	kJ/mol	315.00	NIST
ΔvapH	33.30	kJ/mol	319.50	NIST
ΔvapH	33.20	kJ/mol	320.50	NIST
ΔvapH	31.50 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	31.00 ± 0.10	kJ/mol	330.00	NIST
ΔvapH	30.60 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	30.00 ± 0.10	kJ/mol	348.00	NIST
ΔvapH	29.55	kJ/mol	353.70	NIST
ΔvapH	29.50	kJ/mol	353.80	KDB
n0	1.37882		298.15	KDB
ρl	673.00	kg/m3	293.00	KDB
ΔfusS	[43.90; 44.46]	J/mol×K	[152.50; 153.97]
ΔfusS	43.90	J/mol×K	152.50	NIST
ΔfusS	44.46	J/mol×K	153.97	NIST
γ	0.02	N/m	298.20	KDB
λliquid	[0.09; 0.11]	W/m×K	[256.59; 334.81]
λliquid	0.11	W/m×K	256.59	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	256.99	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	257.30	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	276.30	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	276.69	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	277.04	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	296.19	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	296.63	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	296.97	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	316.55	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	317.01	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	317.37	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.09	W/m×K	333.96	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.09	W/m×K	334.43	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.09	W/m×K	334.81	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	95.00	681.7
283.15	4961.00	686.3
283.15	9969.00	690.9
283.15	14980.00	695.1
283.15	19985.00	699.1
283.15	25039.00	702.9
283.15	30016.00	706.5
283.15	35089.00	710.0
283.15	40016.00	713.3
283.15	45012.00	716.4
283.15	49972.00	719.5
283.15	54980.00	722.4
283.15	59931.00	725.3
283.15	65047.00	728.1
288.15	127.00	677.3
288.15	4984.00	682.2
288.15	9987.00	686.8
288.15	14976.00	691.2
288.15	19996.00	695.3
288.15	24895.00	699.2
288.15	30002.00	703.0
288.15	34983.00	706.5
288.15	40000.00	709.9
288.15	44974.00	713.1
288.15	49950.00	716.2
288.15	55010.00	719.3
288.15	60065.00	722.2
288.15	64958.00	725.0
293.15	83.00	672.8
293.15	4982.00	677.9
293.15	9969.00	682.7
293.15	15059.00	687.3
293.15	19914.00	691.5
293.15	25056.00	695.6
293.15	29936.00	699.3
293.15	34976.00	703.0
293.15	39994.00	706.4
293.15	44992.00	709.8
293.15	50030.00	713.0
293.15	54953.00	716.0
293.15	59933.00	719.0
293.15	65045.00	721.9
298.15	92.00	668.3
298.15	4941.00	673.6
298.15	9982.00	678.6
298.15	14991.00	683.3
298.15	19963.00	687.6
298.15	25048.00	691.8
298.15	29972.00	695.7
298.15	34945.00	699.4
298.15	39958.00	702.9
298.15	45007.00	706.4
298.15	49963.00	709.6
298.15	55008.00	712.8
298.15	60003.00	715.8
298.15	65017.00	718.8
303.15	72.00	663.8
303.15	4969.00	669.3
303.15	9974.00	674.5
303.15	14963.00	679.3
303.15	19981.00	683.9
303.15	25047.00	688.2
303.15	29954.00	692.1
303.15	34987.00	695.9
303.15	39964.00	699.6
303.15	45006.00	703.1
303.15	49991.00	706.4
303.15	55060.00	709.7
303.15	59991.00	712.8
303.15	65054.00	715.8
308.15	100.00	659.4
308.15	4987.00	665.1
308.15	9965.00	670.4
308.15	15040.00	675.5
308.15	19960.00	680.1
308.15	24964.00	684.4
308.15	30076.00	688.7
308.15	34985.00	692.5
308.15	39972.00	696.2
308.15	44972.00	699.8
308.15	49955.00	703.2
308.15	54996.00	706.5
308.15	60063.00	709.7
308.15	65021.00	712.7
313.15	108.00	654.9
313.15	5004.00	660.8
313.15	10013.00	666.4
313.15	15049.00	671.6
313.15	19963.00	676.3
313.15	25062.00	680.9
313.15	29960.00	685.0
313.15	34942.00	689.0
313.15	40039.00	692.9
313.15	45017.00	696.6
313.15	50065.00	700.1
313.15	54977.00	703.4
313.15	59923.00	706.6
313.15	64996.00	709.7
318.15	110.00	650.2
318.15	5061.00	656.5
318.15	9957.00	662.2
318.15	15002.00	667.6
318.15	19980.00	672.5
318.15	25013.00	677.1
318.15	30045.00	681.5
318.15	34965.00	685.6
318.15	39938.00	689.5
318.15	44971.00	693.2
318.15	49989.00	696.8
318.15	55009.00	700.2
318.15	59952.00	703.5
318.15	65056.00	706.7
323.15	121.00	645.6
323.15	5001.00	652.1
323.15	10007.00	658.1
323.15	15037.00	663.6
323.15	19969.00	668.7
323.15	25018.00	673.5
323.15	29938.00	677.9
323.15	35006.00	682.2
323.15	39965.00	686.1
323.15	45012.00	690.0
323.15	49970.00	693.6
323.15	54953.00	697.1
323.15	59965.00	700.4
323.15	65022.00	703.7
328.15	98.00	641.0
328.15	5010.00	647.8
328.15	9934.00	653.9
328.15	14950.00	659.6
328.15	19968.00	664.9
328.15	25011.00	669.8
328.15	30040.00	674.5
328.15	34952.00	678.7
328.15	39959.00	682.8
328.15	45017.00	686.8
328.15	49935.00	690.4
328.15	54941.00	694.0
328.15	59962.00	697.4
328.15	65006.00	700.8
333.15	92.00	636.3
333.15	4968.00	643.3
333.15	9977.00	649.8
333.15	15014.00	655.7
333.15	19986.00	661.1
333.15	25001.00	666.2
333.15	29959.00	670.9
333.15	34922.00	675.3
333.15	39972.00	679.5
333.15	45064.00	683.6
333.15	50006.00	687.3
333.15	54975.00	691.0
333.15	59984.00	694.5
333.15	64995.00	697.8
338.15	107.00	631.7
338.15	5007.00	639.1
338.15	9978.00	645.7
338.15	14968.00	651.8
338.15	19968.00	657.4
338.15	25042.00	662.7
338.15	30018.00	667.5
338.15	35052.00	672.1
338.15	39990.00	676.3
338.15	45087.00	680.5
338.15	49968.00	684.3
338.15	55044.00	688.1
338.15	60031.00	691.6
338.15	64997.00	695.0
343.15	98.00	626.8
343.15	4944.00	634.4
343.15	10008.00	641.5
343.15	14958.00	647.7
343.15	19959.00	653.5
343.15	25045.00	658.9
343.15	30012.00	663.9
343.15	34980.00	668.5
343.15	40024.00	672.9
343.15	44956.00	677.1
343.15	50037.00	681.1
343.15	55010.00	684.9
343.15	59979.00	688.5
343.15	65088.00	692.1
348.15	103.00	622.0
348.15	4998.00	630.0
348.15	9948.00	637.2
348.15	15016.00	643.8
348.15	19991.00	649.7
348.15	25051.00	655.3
348.15	29994.00	660.3
348.15	34970.00	665.1
348.15	39979.00	669.6
348.15	45063.00	673.9
348.15	50024.00	678.0
348.15	54974.00	681.8
348.15	59994.00	685.5
353.15	1014.00	618.8
353.15	5010.00	625.6
353.15	9950.00	633.0
353.15	15037.00	639.9
353.15	19996.00	646.0
353.15	25024.00	651.7
353.15	29983.00	656.9
353.15	34950.00	661.8
353.15	40060.00	666.5
353.15	45017.00	670.8
353.15	49987.00	674.9
353.15	54976.00	678.9
353.15	59989.00	682.7
358.15	5026.00	621.0
358.15	9954.00	628.7
358.15	15017.00	635.8
358.15	19926.00	642.0
358.15	25014.00	647.9
358.15	30045.00	653.4
358.15	35004.00	658.3
358.15	40013.00	663.1
358.15	44988.00	667.5
358.15	49996.00	671.7
358.15	55037.00	675.8
358.15	60020.00	679.6
358.15	65016.00	683.3
363.15	4947.00	616.2
363.15	10031.00	624.5
363.15	15019.00	631.7
363.15	19970.00	638.2
363.15	25122.00	644.3
363.15	30059.00	649.8
363.15	35064.00	654.9
363.15	40055.00	659.8
363.15	45078.00	664.3
363.15	49933.00	668.5
363.15	54989.00	672.7
363.15	59992.00	676.6
363.15	65058.00	680.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[115.43; 461.16]	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			6.61000e+01
Coefficient B			-4.27670e+02
Coefficient C			5.96824e+00
Coefficient D			3.65940e-04
Coefficient E			-1.12450e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	115.43	J/mol×K	200.00	Calculated Property
Cp,gas	192.48	J/mol×K	344.44	Calculated Property
Cp,gas	255.81	J/mol×K	488.89	Calculated Property
Cp,gas	305.86	J/mol×K	633.33	Calculated Property
Cp,gas	346.15	J/mol×K	777.78	Calculated Property
Cp,gas	379.14	J/mol×K	922.22	Calculated Property
Cp,gas	406.36	J/mol×K	1066.67	Calculated Property
Cp,gas	428.73	J/mol×K	1211.11	Calculated Property
Cp,gas	446.86	J/mol×K	1355.56	Calculated Property
Cp,gas	461.16	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[167.43; 252.56]	J/mol×K	[153.91; 353.64]	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			9.02830e+01
Coefficient B			2.21170e+01
Coefficient C			3.38524e+00
Coefficient D			5.81920e-03
Coefficient E			-3.32960e-06
Temperature range, min.			153.91
Temperature range, max.			353.64
Cp,liquid	167.43	J/mol×K	153.91	Calculated Property
Cp,liquid	174.41	J/mol×K	176.10	Calculated Property
Cp,liquid	182.10	J/mol×K	198.29	Calculated Property
Cp,liquid	190.44	J/mol×K	220.49	Calculated Property
Cp,liquid	199.41	J/mol×K	242.68	Calculated Property
Cp,liquid	208.97	J/mol×K	264.87	Calculated Property
Cp,liquid	219.10	J/mol×K	287.06	Calculated Property
Cp,liquid	229.77	J/mol×K	309.26	Calculated Property
Cp,liquid	240.93	J/mol×K	331.45	Calculated Property
Cp,liquid	252.56	J/mol×K	353.64	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0107046; 0.0001270]	Pa×s	[153.91; 400.00]	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			-1.58490e+01
Coefficient B			1.20450e+03
Coefficient C			7.02160e-01
Coefficient D			-2.12840e-06
Coefficient E			2.00000e+00
Temperature range, min.			153.91
Temperature range, max.			400.00
η	0.0107046	Pa×s	153.91	Calculated Property
η	0.0036161	Pa×s	181.25	Calculated Property
η	0.0016327	Pa×s	208.60	Calculated Property
η	0.0008884	Pa×s	235.94	Calculated Property
η	0.0005485	Pa×s	263.28	Calculated Property
η	0.0003702	Pa×s	290.63	Calculated Property
η	0.0002665	Pa×s	317.97	Calculated Property
η	0.0002013	Pa×s	345.31	Calculated Property
η	0.0001577	Pa×s	372.66	Calculated Property
η	0.0001270	Pa×s	400.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[42.15; 12.67]	kJ/mol	[153.91; 500.54]	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			5.63692e+01
Coefficient B			1.08368e+00
Coefficient C			-9.19235e-01
Coefficient D			1.42800e-01
Coefficient E			1.36050e-01
Critical temperature, Tc (K)			5.19700e+02
Temperature range, min.			153.91
Temperature range, max.			500.54
ΔvapH	42.15	kJ/mol	153.91	Calculated Property
ΔvapH	39.49	kJ/mol	192.42	Calculated Property
ΔvapH	37.02	kJ/mol	230.94	Calculated Property
ΔvapH	34.69	kJ/mol	269.45	Calculated Property
ΔvapH	32.38	kJ/mol	307.97	Calculated Property
ΔvapH	29.98	kJ/mol	346.48	Calculated Property
ΔvapH	27.32	kJ/mol	385.00	Calculated Property
ΔvapH	24.13	kJ/mol	423.51	Calculated Property
ΔvapH	19.84	kJ/mol	462.03	Calculated Property
ΔvapH	12.67	kJ/mol	500.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[255.40; 378.30]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41563e+01
Coefficient B			-3.00079e+03
Coefficient C			-3.90250e+01
Temperature range, min.			255.40
Temperature range, max.			378.30
Pvap	1.33	kPa	255.40	Calculated Property
Pvap	3.04	kPa	269.06	Calculated Property
Pvap	6.31	kPa	282.71	Calculated Property
Pvap	12.13	kPa	296.37	Calculated Property
Pvap	21.83	kPa	310.02	Calculated Property
Pvap	37.13	kPa	323.68	Calculated Property
Pvap	60.16	kPa	337.33	Calculated Property
Pvap	93.44	kPa	350.99	Calculated Property
Pvap	139.87	kPa	364.64	Calculated Property
Pvap	202.67	kPa	378.30	Calculated Property
Pvap	[6.65e-06; 2720.79]	kPa	[153.91; 519.70]	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			7.93266e+01
Coefficient B			-6.49829e+03
Coefficient C			-9.77263e+00
Coefficient D			8.13336e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 519.8 K.
Temperature range, min.			153.91
Temperature range, max.			519.70
Pvap	6.65e-06	kPa	153.91	Calculated Property
Pvap	5.12e-03	kPa	194.55	Calculated Property
Pvap	0.30	kPa	235.20	Calculated Property
Pvap	4.34	kPa	275.84	Calculated Property
Pvap	28.35	kPa	316.48	Calculated Property
Pvap	112.56	kPa	357.13	Calculated Property
Pvap	323.41	kPa	397.77	Calculated Property
Pvap	749.27	kPa	438.41	Calculated Property
Pvap	1500.41	kPa	479.06	Calculated Property
Pvap	2720.79	kPa	519.70	Calculated Property
Pvap	[6.38e-06; 2725.86]	kPa	[153.91; 519.79]	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			8.06735e+01
Coefficient B			-6.55171e+03
Coefficient C			-9.98037e+00
Coefficient D			8.33917e-06
Coefficient E			0.00000e+00
Temperature range, min.			153.91
Temperature range, max.			519.79
Pvap	6.38e-06	kPa	153.91	Calculated Property
Pvap	5.05e-03	kPa	194.56	Calculated Property
Pvap	0.30	kPa	235.22	Calculated Property
Pvap	4.35	kPa	275.87	Calculated Property
Pvap	28.47	kPa	316.52	Calculated Property
Pvap	113.00	kPa	357.18	Calculated Property
Pvap	324.39	kPa	397.83	Calculated Property
Pvap	750.90	kPa	438.48	Calculated Property
Pvap	1503.01	kPa	479.14	Calculated Property
Pvap	2725.86	kPa	519.79	Calculated Property
Pvap	[7.70; 104.01]	kPa	[286.86; 354.52]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37262e+01
Coefficient B			-2.75759e+03
Coefficient C			-5.08770e+01
Reference			Forziati, Norris, et al., 1949
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			286.86
Temperature range, max.			354.52
Pvap	7.70	kPa	286.86	Calculated Property
Pvap	11.04	kPa	294.38	Calculated Property
Pvap	15.50	kPa	301.90	Calculated Property
Pvap	21.33	kPa	309.41	Calculated Property
Pvap	28.83	kPa	316.93	Calculated Property
Pvap	38.33	kPa	324.45	Calculated Property
Pvap	50.19	kPa	331.97	Calculated Property
Pvap	64.80	kPa	339.48	Calculated Property
Pvap	82.59	kPa	347.00	Calculated Property
Pvap	104.01	kPa	354.52	Calculated Property
Pvap	[7.70; 104.01]	kPa	[286.86; 354.52]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37262e+01
Coefficient B			-2.75759e+03
Coefficient C			-5.08770e+01
Reference			Forziati, Norris, et al., 1949, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			286.86
Temperature range, max.			354.52
Pvap	7.70	kPa	286.86	Calculated Property
Pvap	11.04	kPa	294.38	Calculated Property
Pvap	15.50	kPa	301.90	Calculated Property
Pvap	21.33	kPa	309.41	Calculated Property
Pvap	28.83	kPa	316.93	Calculated Property
Pvap	38.33	kPa	324.45	Calculated Property
Pvap	50.19	kPa	331.97	Calculated Property
Pvap	64.80	kPa	339.48	Calculated Property
Pvap	82.59	kPa	347.00	Calculated Property
Pvap	104.01	kPa	354.52	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[771.22; 254.07]	kg/m3	[153.91; 519.70]	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			5.00449e+01
Coefficient B			2.41010e-01
Coefficient C			5.19810e+02
Coefficient D			2.30860e-01
Comment			Range stopped at Tc; ChemSep gives it to 519.8 K.
Temperature range, min.			153.91
Temperature range, max.			519.70
ρl	771.22	kg/m3	153.91	Calculated Property
ρl	744.55	kg/m3	194.55	Calculated Property
ρl	716.25	kg/m3	235.20	Calculated Property
ρl	685.92	kg/m3	275.84	Calculated Property
ρl	652.97	kg/m3	316.48	Calculated Property
ρl	616.49	kg/m3	357.13	Calculated Property
ρl	574.88	kg/m3	397.77	Calculated Property
ρl	524.93	kg/m3	438.41	Calculated Property
ρl	457.77	kg/m3	479.06	Calculated Property
ρl	254.07	kg/m3	519.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[153.15; 353.55]	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			4.66402e-02
Coefficient B			-9.72000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			153.15
Temperature range, max.			353.55
γ	0.03	N/m	153.15	Calculated Property
γ	0.03	N/m	175.42	Calculated Property
γ	0.03	N/m	197.68	Calculated Property
γ	0.03	N/m	219.95	Calculated Property
γ	0.02	N/m	242.22	Calculated Property
γ	0.02	N/m	264.48	Calculated Property
γ	0.02	N/m	286.75	Calculated Property
γ	0.02	N/m	309.02	Calculated Property
γ	0.01	N/m	331.28	Calculated Property
γ	0.01	N/m	353.55	Calculated Property
γ	[0.03; 8.86e-04]	N/m	[153.91; 500.54]	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			-1.26250e-02
Coefficient B			1.96420e+01
Coefficient C			-3.08720e+00
Coefficient D			-2.52990e-04
Coefficient E			-4.50890e-06
Temperature range, min.			153.91
Temperature range, max.			500.54
γ	0.03	N/m	153.91	Calculated Property
γ	0.03	N/m	192.42	Calculated Property
γ	0.02	N/m	230.94	Calculated Property
γ	0.02	N/m	269.45	Calculated Property
γ	0.02	N/m	307.97	Calculated Property
γ	0.01	N/m	346.48	Calculated Property
γ	0.01	N/m	385.00	Calculated Property
γ	0.01	N/m	423.51	Calculated Property
γ	0.00	N/m	462.03	Calculated Property
γ	8.86e-04	N/m	500.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.10]	W/m×K	[153.91; 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			2.56900e-04
Coefficient B			9.03300e-01
Coefficient C			1.47330e+02
Coefficient D			1.82490e+05
Temperature range, min.			153.91
Temperature range, max.			1000.00
λgas	0.00	W/m×K	153.91	Calculated Property
λgas	0.01	W/m×K	247.92	Calculated Property
λgas	0.02	W/m×K	341.93	Calculated Property
λgas	0.03	W/m×K	435.94	Calculated Property
λgas	0.04	W/m×K	529.95	Calculated Property
λgas	0.05	W/m×K	623.96	Calculated Property
λgas	0.06	W/m×K	717.97	Calculated Property
λgas	0.07	W/m×K	811.98	Calculated Property
λgas	0.09	W/m×K	905.99	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.13; 0.09]	W/m×K	[153.91; 353.64]	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			-1.00480e-01
Coefficient B			3.79800e+00
Coefficient C			-1.38240e+00
Coefficient D			-4.04130e-04
Coefficient E			-1.17830e-06
Temperature range, min.			153.91
Temperature range, max.			353.64
λliquid	0.13	W/m×K	153.91	Calculated Property
λliquid	0.13	W/m×K	176.10	Calculated Property
λliquid	0.12	W/m×K	198.29	Calculated Property
λliquid	0.12	W/m×K	220.49	Calculated Property
λliquid	0.12	W/m×K	242.68	Calculated Property
λliquid	0.11	W/m×K	264.87	Calculated Property
λliquid	0.11	W/m×K	287.06	Calculated Property
λliquid	0.10	W/m×K	309.26	Calculated Property
λliquid	0.09	W/m×K	331.45	Calculated Property
λliquid	0.09	W/m×K	353.64	Calculated Property

Similar Compounds

Find more compounds similar to Pentane, 2,4-dimethyl-.

Mixtures

• 1,2-Ethanediol + Pentane, 2,4-dimethyl- + Water

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.
• Cheméo Relay (1.0)
• 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
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• P-r-T Data and Derivative Properties of 3-Methylpentane, 2,4-Dimethylpentane, and 2,3,4-Trimethylpentane from 283.15 to 363.15 K at Pressures up to 65 MPa
• Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• 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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