Chemical Properties of Nonane, 2-methyl- (CAS 871-83-0)

InChI

InChI=1S/C10H22/c1-4-5-6-7-8-9-10(2)3/h10H,4-9H2,1-3H3

InChI Key

SGVYKUFIHHTIFL-UHFFFAOYSA-N

Formula

C10H22

SMILES

CCCCCCCC(C)C

Molecular Weight¹

142.28

CAS

871-83-0

Other Names

• 2-methylnonane

• 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).
• 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).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-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).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4590; 0.4723]
ω	0.4723		ChemSep v8.3 pure component data Compiled value
ω	0.4590		KDB
AP	353.450	K	KDB
ΔcH°liquid	-6769.50 ± 2.30	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	28.41	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δc,grossH	6772.98	kJ/mol	KDB
Δc,netH	6288.845	kJ/mol	KDB
ΔfH°gas	[-260.20; -256.52]	kJ/mol
ΔfH°gas	-256.52	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-260.20	kJ/mol	NIST
ΔfH°liquid	-309.80 ± 2.40	kJ/mol	NIST
ΔfusH°	18.13	kJ/mol	Joback Calculated Property
ΔvapH°	[49.64; 51.00]	kJ/mol
ΔvapH°	49.64	kJ/mol	NIST
ΔvapH°	51.00	kJ/mol	NIST
IE	9.69	eV	Relay (1.0) Calculated Property
log10WS	-5.83		Relay (1.0) Calculated Property
logPoct/wat	4.003		Crippen Calculated Property
McVol	151.760	ml/mol	McGowan Calculated Property
Pc	[2050.00; 2100.00]	kPa
Pc	2050.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2100.00	kPa	KDB
Ptriple	2.49e-06	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[962.00; 987.00]
Inp	964.00		NIST
Inp	962.00		NIST
Inp	962.00		NIST
Inp	962.00		NIST
Inp	Outlier 976.00		NIST
Inp	966.00		NIST
Inp	964.00		NIST
Inp	964.00		NIST
Inp	972.00		NIST
Inp	972.00		NIST
Inp	965.20		NIST
Inp	965.10		NIST
Inp	962.00		NIST
Inp	963.90		NIST
Inp	964.70		NIST
Inp	965.00		NIST
Inp	964.00		NIST
Inp	966.00		NIST
Inp	968.00		NIST
Inp	964.00		NIST
Inp	966.00		NIST
Inp	965.00		NIST
Inp	967.00		NIST
Inp	968.00		NIST
Inp	963.00		NIST
Inp	964.43		NIST
Inp	964.43		NIST
Inp	963.80		NIST
Inp	964.00		NIST
Inp	964.00		NIST
Inp	964.00		NIST
Inp	964.00		NIST
Inp	964.00		NIST
Inp	971.70		NIST
Inp	974.00		NIST
Inp	964.00		NIST
Inp	965.00		NIST
Inp	966.20		NIST
Inp	962.60		NIST
Inp	964.00		NIST
Inp	964.80		NIST
Inp	968.60		NIST
Inp	965.00		NIST
Inp	964.00		NIST
Inp	965.96		NIST
Inp	966.07		NIST
Inp	966.05		NIST
Inp	965.23		NIST
Inp	965.28		NIST
Inp	965.28		NIST
Inp	964.00		NIST
Inp	962.00		NIST
Inp	Outlier 980.70		NIST
Inp	964.00		NIST
Inp	965.00		NIST
Inp	966.00		NIST
Inp	969.00		NIST
Inp	964.00		NIST
Inp	968.00		NIST
Inp	966.00		NIST
Inp	965.40		NIST
Inp	965.00		NIST
Inp	970.00		NIST
Inp	966.00		NIST
Inp	963.00		NIST
Inp	965.00		NIST
Inp	Outlier 987.00		NIST
Inp	966.00		NIST
Inp	964.00		NIST
Inp	966.00		NIST
Inp	964.00		NIST
Inp	964.00		NIST
Inp	973.00		NIST
Inp	972.00		NIST
Inp	964.00		NIST
Inp	964.00		NIST
Inp	966.00		NIST
Inp	965.20		NIST
Inp	965.00		NIST
Inp	964.43		NIST
Inp	971.70		NIST
S°liquid	420.10	J/mol×K	NIST
Tboil	[440.00; 440.20]	K
Tboil	440.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	440.20	K	KDB
Tboil	440.00	K	NIST
Tboil	440.20	K	NIST
Tboil	440.15 ± 0.15	K	NIST
Tboil	440.00 ± 0.30	K	NIST
Tc	[610.30; 621.00]	K
Tc	621.00	K	ChemSep v8.3 pure component data Compiled value
Tc	610.30	K	KDB
Tc	610.70	K	NIST
Tfus	[198.35; 201.50]	K
Tfus	198.35	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	198.50	K	ChemSep v8.3 pure component data Compiled value
Tfus	199.00	K	KDB
Tfus	Outlier 201.50 ± 0.15	K	NIST
Tfus	198.79 ± 0.20	K	NIST
Tfus	198.79 ± 0.20	K	NIST
Ttriple	[198.50; 198.80]	K
Ttriple	198.50	K	ChemSep v8.3 pure component data Compiled value
Ttriple	198.80 ± 0.20	K	NIST
Ttriple	198.80 ± 0.20	K	NIST
UQi	6.01		ChemSep v8.3 pure component data Compiled value
URi	7.20		ChemSep v8.3 pure component data Compiled value
Vc	[0.596; 0.601]	m3/kmol
Vc	0.601	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.596	m3/kmol	KDB
Zc	[0.2440000; 0.2466530]
Zc	0.2440000		ChemSep v8.3 pure component data Compiled value
Zc	0.2466530		KDB
Zra	0.24		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[278.80; 314.60]	J/mol×K	[200.00; 300.00]
Cp,liquid	278.80	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	278.90	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	280.00	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	282.10	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
Cp,liquid	285.00	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	288.70	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	293.00	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	297.80	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	299.50	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	303.10	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	308.70	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	313.30	J/mol×K	298.10	NIST
Cp,liquid	313.50	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	314.60	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
ΔfusH	[17.49; 17.49]	kJ/mol	[198.80; 198.80]
ΔfusH	17.49	kJ/mol	198.80	NIST
ΔfusH	17.49	kJ/mol	198.80	NIST
ΔfusH	17.49	kJ/mol	198.80	NIST
ΔfusH	17.49	kJ/mol	198.80	NIST
ΔvapH	[38.23; 47.30]	kJ/mol	[328.00; 440.20]
ΔvapH	47.30 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	46.20 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	45.00 ± 0.20	kJ/mol	358.00	NIST
ΔvapH	46.40 ± 0.20	kJ/mol	382.50	NIST
ΔvapH	39.20	kJ/mol	440.20	KDB
ΔvapH	38.23	kJ/mol	440.20	NIST
n0	1.40750		298.15	KDB
ρl	[621.59; 735.13]	kg/m3	[283.15; 423.15]
ρl	734.70	kg/m3	283.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	735.13	kg/m3	283.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	734.50	kg/m3	283.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	731.33	kg/m3	288.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	726.90	kg/m3	293.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	727.47	kg/m3	293.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	727.10	kg/m3	293.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	723.63	kg/m3	298.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	723.54	kg/m3	298.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	719.96	kg/m3	303.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	719.30	kg/m3	303.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	719.40	kg/m3	303.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	716.11	kg/m3	308.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	711.60	kg/m3	313.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	711.70	kg/m3	313.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	712.27	kg/m3	313.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	708.49	kg/m3	318.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	703.90	kg/m3	323.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	703.90	kg/m3	323.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	704.63	kg/m3	323.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	704.14	kg/m3	323.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	700.72	kg/m3	328.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	696.00	kg/m3	333.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	696.79	kg/m3	333.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	692.85	kg/m3	338.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	688.88	kg/m3	343.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	688.10	kg/m3	343.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	684.45	kg/m3	348.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	684.90	kg/m3	348.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	680.20	kg/m3	353.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	680.89	kg/m3	353.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	676.83	kg/m3	358.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	672.10	kg/m3	363.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	672.81	kg/m3	363.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	664.34	kg/m3	373.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	664.00	kg/m3	373.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	643.46	kg/m3	398.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	621.59	kg/m3	423.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ΔfusS	[87.97; 87.97]	J/mol×K	[198.80; 198.80]
ΔfusS	87.97	J/mol×K	198.80	NIST
ΔfusS	87.97	J/mol×K	198.80	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[150.58; 620.14]	J/mol×K	[150.00; 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			1.37030e+02
Coefficient B			-5.99280e+02
Coefficient C			6.60124e+00
Coefficient D			1.85630e-06
Coefficient E			-1.07810e-08
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	150.58	J/mol×K	150.00	Calculated Property
Cp,gas	236.84	J/mol×K	300.00	Calculated Property
Cp,gas	331.09	J/mol×K	450.00	Calculated Property
Cp,gas	407.37	J/mol×K	600.00	Calculated Property
Cp,gas	466.52	J/mol×K	750.00	Calculated Property
Cp,gas	512.55	J/mol×K	900.00	Calculated Property
Cp,gas	548.84	J/mol×K	1050.00	Calculated Property
Cp,gas	577.81	J/mol×K	1200.00	Calculated Property
Cp,gas	601.17	J/mol×K	1350.00	Calculated Property
Cp,gas	620.14	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[276.04; 531.87]	J/mol×K	[198.50; 580.00]	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			-5.26060e+01
Coefficient B			8.09810e+01
Coefficient C			4.87824e+00
Coefficient D			2.68310e-03
Coefficient E			-6.04480e-07
Temperature range, min.			198.50
Temperature range, max.			580.00
Cp,liquid	276.04	J/mol×K	198.50	Calculated Property
Cp,liquid	286.28	J/mol×K	240.89	Calculated Property
Cp,liquid	303.66	J/mol×K	283.28	Calculated Property
Cp,liquid	326.04	J/mol×K	325.67	Calculated Property
Cp,liquid	352.40	J/mol×K	368.06	Calculated Property
Cp,liquid	382.23	J/mol×K	410.44	Calculated Property
Cp,liquid	415.23	J/mol×K	452.83	Calculated Property
Cp,liquid	451.23	J/mol×K	495.22	Calculated Property
Cp,liquid	490.13	J/mol×K	537.61	Calculated Property
Cp,liquid	531.87	J/mol×K	580.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0064114; 0.0000909]	Pa×s	[198.50; 621.00]	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			-3.15190e+00
Coefficient B			9.49540e+02
Coefficient C			-1.27250e+00
Coefficient D			1.29860e-06
Coefficient E			2.00000e+00
Temperature range, min.			198.50
Temperature range, max.			621.00
η	0.0064114	Pa×s	198.50	Calculated Property
η	0.0020139	Pa×s	245.44	Calculated Property
η	0.0008950	Pa×s	292.39	Calculated Property
η	0.0004911	Pa×s	339.33	Calculated Property
η	0.0003098	Pa×s	386.28	Calculated Property
η	0.0002156	Pa×s	433.22	Calculated Property
η	0.0001614	Pa×s	480.17	Calculated Property
η	0.0001278	Pa×s	527.11	Calculated Property
η	0.0001058	Pa×s	574.06	Calculated Property
η	0.0000909	Pa×s	621.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[61.60; 9.62]	kJ/mol	[198.50; 610.00]	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			7.02399e+01
Coefficient B			-8.79246e-01
Coefficient C			6.37127e+00
Coefficient D			-9.40458e+00
Coefficient E			4.41870e+00
Critical temperature, Tc (K)			6.21000e+02
Temperature range, min.			198.50
Temperature range, max.			610.00
ΔvapH	61.60	kJ/mol	198.50	Calculated Property
ΔvapH	56.36	kJ/mol	244.22	Calculated Property
ΔvapH	51.44	kJ/mol	289.94	Calculated Property
ΔvapH	47.07	kJ/mol	335.67	Calculated Property
ΔvapH	43.22	kJ/mol	381.39	Calculated Property
ΔvapH	39.63	kJ/mol	427.11	Calculated Property
ΔvapH	35.81	kJ/mol	472.83	Calculated Property
ΔvapH	30.87	kJ/mol	518.56	Calculated Property
ΔvapH	23.35	kJ/mol	564.28	Calculated Property
ΔvapH	9.62	kJ/mol	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[324.60; 468.87]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44006e+01
Coefficient B			-3.68356e+03
Coefficient C			-6.35970e+01
Temperature range, min.			324.60
Temperature range, max.			468.87
Pvap	1.33	kPa	324.60	Calculated Property
Pvap	3.02	kPa	340.63	Calculated Property
Pvap	6.24	kPa	356.66	Calculated Property
Pvap	11.98	kPa	372.69	Calculated Property
Pvap	21.56	kPa	388.72	Calculated Property
Pvap	36.72	kPa	404.75	Calculated Property
Pvap	59.61	kPa	420.78	Calculated Property
Pvap	92.83	kPa	436.81	Calculated Property
Pvap	139.39	kPa	452.84	Calculated Property
Pvap	202.66	kPa	468.87	Calculated Property
Pvap	[2.77e-06; 2126.28]	kPa	[198.50; 610.00]	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			1.26222e+02
Coefficient B			-1.04620e+04
Coefficient C			-1.63880e+01
Coefficient D			9.92870e-06
Coefficient E			2.00000e+00
Temperature range, min.			198.50
Temperature range, max.			610.00
Pvap	2.77e-06	kPa	198.50	Calculated Property
Pvap	2.19e-03	kPa	244.22	Calculated Property
Pvap	0.14	kPa	289.94	Calculated Property
Pvap	2.36	kPa	335.67	Calculated Property
Pvap	16.91	kPa	381.39	Calculated Property
Pvap	71.94	kPa	427.11	Calculated Property
Pvap	218.40	kPa	472.83	Calculated Property
Pvap	530.93	kPa	518.56	Calculated Property
Pvap	1114.53	kPa	564.28	Calculated Property
Pvap	2126.28	kPa	610.00	Calculated Property
Pvap	[2.49e-06; 2121.01]	kPa	[198.50; 610.00]	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			1.28452e+02
Coefficient B			-1.05839e+04
Coefficient C			-1.67146e+01
Coefficient D			1.00957e-05
Coefficient E			0.00000e+00
Temperature range, min.			198.50
Temperature range, max.			610.00
Pvap	2.49e-06	kPa	198.50	Calculated Property
Pvap	2.07e-03	kPa	244.22	Calculated Property
Pvap	0.14	kPa	289.94	Calculated Property
Pvap	2.33	kPa	335.67	Calculated Property
Pvap	16.80	kPa	381.39	Calculated Property
Pvap	71.70	kPa	427.11	Calculated Property
Pvap	217.96	kPa	472.83	Calculated Property
Pvap	529.93	kPa	518.56	Calculated Property
Pvap	1112.09	kPa	564.28	Calculated Property
Pvap	2121.01	kPa	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[793.67; 398.61]	kg/m3	[198.50; 588.34]	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			3.19138e+01
Coefficient B			1.86610e-01
Coefficient C			6.21000e+02
Coefficient D			2.32590e-01
Temperature range, min.			198.50
Temperature range, max.			588.34
ρl	793.67	kg/m3	198.50	Calculated Property
ρl	763.97	kg/m3	241.82	Calculated Property
ρl	732.81	kg/m3	285.13	Calculated Property
ρl	699.88	kg/m3	328.45	Calculated Property
ρl	664.71	kg/m3	371.76	Calculated Property
ρl	626.65	kg/m3	415.08	Calculated Property
ρl	584.63	kg/m3	458.39	Calculated Property
ρl	536.75	kg/m3	501.71	Calculated Property
ρl	478.95	kg/m3	545.02	Calculated Property
ρl	398.61	kg/m3	588.34	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 2.42e-04]	N/m	[198.50; 610.00]	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			-1.32660e-02
Coefficient B			8.69720e+00
Coefficient C			-2.80180e+00
Coefficient D			-1.27790e-03
Coefficient E			-1.98180e-06
Temperature range, min.			198.50
Temperature range, max.			610.00
γ	0.03	N/m	198.50	Calculated Property
γ	0.03	N/m	244.22	Calculated Property
γ	0.02	N/m	289.94	Calculated Property
γ	0.02	N/m	335.67	Calculated Property
γ	0.02	N/m	381.39	Calculated Property
γ	0.01	N/m	427.11	Calculated Property
γ	0.01	N/m	472.83	Calculated Property
γ	0.01	N/m	518.56	Calculated Property
γ	0.00	N/m	564.28	Calculated Property
γ	2.42e-04	N/m	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[198.50; 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			3.06410e-05
Coefficient B			1.14370e+00
Coefficient C			-1.71780e+02
Coefficient D			1.68770e+05
Temperature range, min.			198.50
Temperature range, max.			1000.00
λgas	0.00	W/m×K	198.50	Calculated Property
λgas	0.01	W/m×K	287.56	Calculated Property
λgas	0.02	W/m×K	376.61	Calculated Property
λgas	0.02	W/m×K	465.67	Calculated Property
λgas	0.03	W/m×K	554.72	Calculated Property
λgas	0.04	W/m×K	643.78	Calculated Property
λgas	0.05	W/m×K	732.83	Calculated Property
λgas	0.06	W/m×K	821.89	Calculated Property
λgas	0.07	W/m×K	910.94	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.09]	W/m×K	[198.50; 488.00]	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			-1.65130e-01
Coefficient B			1.51210e+01
Coefficient C			-1.15820e+00
Coefficient D			-1.12520e-04
Coefficient E			-8.53400e-07
Temperature range, min.			198.50
Temperature range, max.			488.00
λliquid	0.16	W/m×K	198.50	Calculated Property
λliquid	0.15	W/m×K	230.67	Calculated Property
λliquid	0.14	W/m×K	262.83	Calculated Property
λliquid	0.13	W/m×K	295.00	Calculated Property
λliquid	0.12	W/m×K	327.17	Calculated Property
λliquid	0.12	W/m×K	359.33	Calculated Property
λliquid	0.11	W/m×K	391.50	Calculated Property
λliquid	0.10	W/m×K	423.67	Calculated Property
λliquid	0.09	W/m×K	455.83	Calculated Property
λliquid	0.09	W/m×K	488.00	Calculated Property

Similar Compounds

Find more compounds similar to Nonane, 2-methyl-.

Mixtures

• Nonane, 2-methyl- + Octacosane

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).
• 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
• Crippen Method
• Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
• Liquid Viscosity and Interfacial Tension of Binary and Ternary Mixtures Containing n-Octacosane by Surface Light Scattering
• Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
• Joback Method
• KDB
• 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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