Chemical Properties of Nonane, 5-methyl- (CAS 15869-85-9)

InChI

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

InChI Key

TYSIILFJZXHVPU-UHFFFAOYSA-N

Formula

C10H22

SMILES

CCCCC(C)CCCC

Molecular Weight¹

142.28

CAS

15869-85-9

Other Names

• 5-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.
• 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).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4520; 0.4562]
ω	0.4562		ChemSep v8.3 pure component data Compiled value
ω	0.4520		KDB
AP	351.050	K	KDB
ΔcH°liquid	-6771.40 ± 1.60	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	30.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δc,grossH	6775.74	kJ/mol	KDB
Δc,netH	6291.606	kJ/mol	KDB
ΔfH°gas	[-258.60; -254.72]	kJ/mol
ΔfH°gas	-254.72	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-258.60	kJ/mol	NIST
ΔfH°liquid	-307.90 ± 1.60	kJ/mol	NIST
ΔfusH°	18.13	kJ/mol	Joback Calculated Property
ΔvapH°	[49.35; 49.80]	kJ/mol
ΔvapH°	49.35	kJ/mol	NIST
ΔvapH°	49.80	kJ/mol	NIST
IE	9.59	eV	Relay (1.0) Calculated Property
log10WS	-5.77		Relay (1.0) Calculated Property
logPoct/wat	4.003		Crippen Calculated Property
McVol	151.760	ml/mol	McGowan Calculated Property
Pc	[2140.00; 2140.00]	kPa
Pc	2140.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2140.00	kPa	KDB
Ptriple	4.38e-07	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[954.00; 968.00]
Inp	961.00		NIST
Inp	958.00		NIST
Inp	957.00		NIST
Inp	961.00		NIST
Inp	966.00		NIST
Inp	965.00		NIST
Inp	960.00		NIST
Inp	964.00		NIST
Inp	960.80		NIST
Inp	960.80		NIST
Inp	956.00		NIST
Inp	957.40		NIST
Inp	958.60		NIST
Inp	Outlier 954.00		NIST
Inp	957.00		NIST
Inp	958.00		NIST
Inp	962.00		NIST
Inp	960.00		NIST
Inp	960.00		NIST
Inp	957.00		NIST
Inp	Outlier 967.80		NIST
Inp	957.00		NIST
Inp	962.10		NIST
Inp	958.10		NIST
Inp	959.80		NIST
Inp	963.00		NIST
Inp	961.00		NIST
Inp	961.48		NIST
Inp	961.76		NIST
Inp	961.62		NIST
Inp	960.91		NIST
Inp	961.01		NIST
Inp	960.97		NIST
Inp	960.00		NIST
Inp	960.00		NIST
Inp	959.00		NIST
Inp	966.00		NIST
Inp	962.00		NIST
Inp	961.10		NIST
Inp	961.00		NIST
Inp	957.00		NIST
Inp	957.00		NIST
Inp	960.00		NIST
Inp	Outlier 968.00		NIST
Inp	958.00		NIST
Inp	960.00		NIST
Inp	957.00		NIST
Inp	960.00		NIST
Inp	960.80		NIST
Inp	959.00		NIST
Inp	962.10		NIST
Inp	961.48		NIST
Inp	960.97		NIST
Ip	[960.00; 960.00]
Ip	960.00		NIST
Ip	960.00		NIST
Ip	960.00		NIST
S°liquid	423.80	J/mol×K	NIST
Tboil	[435.65; 438.30]	K
Tboil	438.25	K	ChemSep v8.3 pure component data Compiled value
Tboil	438.30	K	KDB
Tboil	438.30	K	NIST
Tboil	438.30	K	NIST
Tboil	438.30 ± 0.30	K	NIST
Tboil	Outlier 435.65 ± 2.00	K	NIST
Tboil	438.15 ± 2.00	K	NIST
Tc	[609.60; 609.80]	K
Tc	609.60	K	ChemSep v8.3 pure component data Compiled value
Tc	609.60	K	KDB
Tc	609.80	K	NIST
Tfus	[185.00; 186.70]	K
Tfus	185.30	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	186.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	185.00	K	KDB
Tfus	186.70 ± 0.20	K	NIST
Tfus	186.35 ± 0.15	K	NIST
Tfus	186.70 ± 0.20	K	NIST
Ttriple	[185.45; 186.70]	K
Ttriple	185.45	K	ChemSep v8.3 pure component data Compiled value
Ttriple	186.70 ± 0.01	K	NIST
Ttriple	186.70 ± 0.01	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	[0.573; 0.590]	m3/kmol
Vc	0.590	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.573	m3/kmol	KDB
Zc	[0.2419280; 0.2480000]
Zc	0.2480000		ChemSep v8.3 pure component data Compiled value
Zc	0.2419280		KDB
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[264.70; 315.70]	J/mol×K	[190.00; 300.00]
Cp,liquid	264.70	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	267.40	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	270.50	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	273.90	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	277.80	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	282.00	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	286.60	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	291.70	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	297.10	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	298.90	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	302.90	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	309.10	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	314.43	J/mol×K	298.10	NIST
Cp,liquid	314.50	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	315.70	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	[16.64; 16.65]	kJ/mol	[186.70; 186.70]
ΔfusH	16.65	kJ/mol	186.70	NIST
ΔfusH	16.65	kJ/mol	186.70	NIST
ΔfusH	16.64	kJ/mol	186.70	NIST
ΔfusH	16.64	kJ/mol	186.70	NIST
ΔvapH	[38.14; 47.00]	kJ/mol	[328.00; 438.30]
ΔvapH	47.00 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	45.90 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	44.60 ± 0.20	kJ/mol	358.00	NIST
ΔvapH	38.70	kJ/mol	438.30	KDB
ΔvapH	38.14	kJ/mol	438.30	NIST
n0	1.41000		298.15	KDB
ΔfusS	[89.13; 89.13]	J/mol×K	[186.70; 186.70]
ΔfusS	89.13	J/mol×K	186.70	NIST
ΔfusS	89.13	J/mol×K	186.70	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[145.89; 620.41]	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			1.31700e+02
Coefficient B			-5.94980e+02
Coefficient C			6.62124e+00
Coefficient D			-1.42340e-05
Coefficient E			-5.09870e-09
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	145.89	J/mol×K	150.00	Calculated Property
Cp,gas	234.55	J/mol×K	300.00	Calculated Property
Cp,gas	330.37	J/mol×K	450.00	Calculated Property
Cp,gas	407.38	J/mol×K	600.00	Calculated Property
Cp,gas	466.79	J/mol×K	750.00	Calculated Property
Cp,gas	512.86	J/mol×K	900.00	Calculated Property
Cp,gas	549.09	J/mol×K	1050.00	Calculated Property
Cp,gas	578.01	J/mol×K	1200.00	Calculated Property
Cp,gas	601.36	J/mol×K	1350.00	Calculated Property
Cp,gas	620.41	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[263.26; 500.24]	J/mol×K	[185.45; 550.00]	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			2.30160e+02
Coefficient B			-6.19770e+01
Coefficient C			2.25254e+00
Coefficient D			9.66450e-03
Coefficient E			-6.13760e-06
Temperature range, min.			185.45
Temperature range, max.			550.00
Cp,liquid	263.26	J/mol×K	185.45	Calculated Property
Cp,liquid	277.09	J/mol×K	225.96	Calculated Property
Cp,liquid	294.19	J/mol×K	266.46	Calculated Property
Cp,liquid	314.85	J/mol×K	306.97	Calculated Property
Cp,liquid	339.15	J/mol×K	347.47	Calculated Property
Cp,liquid	366.96	J/mol×K	387.98	Calculated Property
Cp,liquid	397.85	J/mol×K	428.48	Calculated Property
Cp,liquid	431.09	J/mol×K	468.99	Calculated Property
Cp,liquid	465.65	J/mol×K	509.49	Calculated Property
Cp,liquid	500.24	J/mol×K	550.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0095311; 0.0001503]	Pa×s	[185.45; 491.00]	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			-1.38380e+01
Coefficient B			1.30380e+03
Coefficient C			4.18280e-01
Coefficient D			-8.79420e-07
Coefficient E			2.00000e+00
Temperature range, min.			185.45
Temperature range, max.			491.00
η	0.0095311	Pa×s	185.45	Calculated Property
η	0.0034038	Pa×s	219.40	Calculated Property
η	0.0016074	Pa×s	253.35	Calculated Property
η	0.0009075	Pa×s	287.30	Calculated Property
η	0.0005781	Pa×s	321.25	Calculated Property
η	0.0004009	Pa×s	355.20	Calculated Property
η	0.0002957	Pa×s	389.15	Calculated Property
η	0.0002284	Pa×s	423.10	Calculated Property
η	0.0001828	Pa×s	457.05	Calculated Property
η	0.0001503	Pa×s	491.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[57.73; 17.33]	kJ/mol	[185.45; 587.66]	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			6.55880e+01
Coefficient B			2.97620e-02
Coefficient C			1.60610e+00
Coefficient D			-2.04170e+00
Coefficient E			8.03240e-01
Critical temperature, Tc (K)			6.09600e+02
Temperature range, min.			185.45
Temperature range, max.			587.66
ΔvapH	57.73	kJ/mol	185.45	Calculated Property
ΔvapH	54.56	kJ/mol	230.14	Calculated Property
ΔvapH	51.22	kJ/mol	274.83	Calculated Property
ΔvapH	47.79	kJ/mol	319.52	Calculated Property
ΔvapH	44.28	kJ/mol	364.21	Calculated Property
ΔvapH	40.64	kJ/mol	408.90	Calculated Property
ΔvapH	36.73	kJ/mol	453.59	Calculated Property
ΔvapH	32.27	kJ/mol	498.28	Calculated Property
ΔvapH	26.57	kJ/mol	542.97	Calculated Property
ΔvapH	17.33	kJ/mol	587.66	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[321.68; 467.18]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44953e+01
Coefficient B			-3.77885e+03
Coefficient C			-5.57070e+01
Temperature range, min.			321.68
Temperature range, max.			467.18
Pvap	1.33	kPa	321.68	Calculated Property
Pvap	3.01	kPa	337.85	Calculated Property
Pvap	6.22	kPa	354.01	Calculated Property
Pvap	11.93	kPa	370.18	Calculated Property
Pvap	21.46	kPa	386.35	Calculated Property
Pvap	36.57	kPa	402.51	Calculated Property
Pvap	59.41	kPa	418.68	Calculated Property
Pvap	92.61	kPa	434.85	Calculated Property
Pvap	139.21	kPa	451.01	Calculated Property
Pvap	202.67	kPa	467.18	Calculated Property
Pvap	[5.67e-08; 3095.66]	kPa	[185.45; 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			2.08731e+02
Coefficient B			-1.37123e+04
Coefficient C			-2.91586e+01
Coefficient D			2.36309e-05
Coefficient E			2.00000e+00
Temperature range, min.			185.45
Temperature range, max.			610.00
Pvap	5.67e-08	kPa	185.45	Calculated Property
Pvap	3.96e-04	kPa	232.62	Calculated Property
Pvap	0.07	kPa	279.79	Calculated Property
Pvap	1.64	kPa	326.97	Calculated Property
Pvap	13.94	kPa	374.14	Calculated Property
Pvap	64.26	kPa	421.31	Calculated Property
Pvap	207.97	kPa	468.48	Calculated Property
Pvap	552.58	kPa	515.66	Calculated Property
Pvap	1330.32	kPa	562.83	Calculated Property
Pvap	3095.66	kPa	610.00	Calculated Property
Pvap	[4.23e-07; 2063.01]	kPa	[185.45; 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			1.03449e+02
Coefficient B			-9.43079e+03
Coefficient C			-1.29252e+01
Coefficient D			6.82316e-06
Coefficient E			0.00000e+00
Temperature range, min.			185.45
Temperature range, max.			610.00
Pvap	4.23e-07	kPa	185.45	Calculated Property
Pvap	7.78e-04	kPa	232.62	Calculated Property
Pvap	0.08	kPa	279.79	Calculated Property
Pvap	1.65	kPa	326.97	Calculated Property
Pvap	13.74	kPa	374.14	Calculated Property
Pvap	64.30	kPa	421.31	Calculated Property
Pvap	206.87	kPa	468.48	Calculated Property
Pvap	518.21	kPa	515.66	Calculated Property
Pvap	1095.48	kPa	562.83	Calculated Property
Pvap	2063.01	kPa	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[807.60; 248.32]	kg/m3	[185.45; 610.00]	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			5.89943e+01
Coefficient B			2.52900e-01
Coefficient C			6.10010e+02
Coefficient D			2.80510e-01
Temperature range, min.			185.45
Temperature range, max.			610.00
ρl	807.60	kg/m3	185.45	Calculated Property
ρl	775.66	kg/m3	232.62	Calculated Property
ρl	742.14	kg/m3	279.79	Calculated Property
ρl	706.67	kg/m3	326.97	Calculated Property
ρl	668.68	kg/m3	374.14	Calculated Property
ρl	627.29	kg/m3	421.31	Calculated Property
ρl	580.98	kg/m3	468.48	Calculated Property
ρl	526.70	kg/m3	515.66	Calculated Property
ρl	456.11	kg/m3	562.83	Calculated Property
ρl	248.32	kg/m3	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 7.71e-04]	N/m	[185.45; 587.66]	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			-1.55520e-02
Coefficient B			2.22800e+01
Coefficient C			-2.89610e+00
Coefficient D			-7.50590e-04
Coefficient E			-2.36260e-06
Temperature range, min.			185.45
Temperature range, max.			587.66
γ	0.03	N/m	185.45	Calculated Property
γ	0.03	N/m	230.14	Calculated Property
γ	0.03	N/m	274.83	Calculated Property
γ	0.02	N/m	319.52	Calculated Property
γ	0.02	N/m	364.21	Calculated Property
γ	0.01	N/m	408.90	Calculated Property
γ	0.01	N/m	453.59	Calculated Property
γ	0.01	N/m	498.28	Calculated Property
γ	0.00	N/m	542.97	Calculated Property
γ	7.71e-04	N/m	587.66	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[185.45; 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			3.61400e-05
Coefficient B			1.12390e+00
Coefficient C			-1.59130e+02
Coefficient D			1.72680e+05
Temperature range, min.			185.45
Temperature range, max.			1000.00
λgas	0.00	W/m×K	185.45	Calculated Property
λgas	0.01	W/m×K	275.96	Calculated Property
λgas	0.01	W/m×K	366.46	Calculated Property
λgas	0.02	W/m×K	456.97	Calculated Property
λgas	0.03	W/m×K	547.47	Calculated Property
λgas	0.04	W/m×K	637.98	Calculated Property
λgas	0.05	W/m×K	728.48	Calculated Property
λgas	0.06	W/m×K	818.99	Calculated Property
λgas	0.07	W/m×K	909.49	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.08]	W/m×K	[185.45; 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			-1.83000e-01
Coefficient B			1.04900e+01
Coefficient C			-1.06980e+00
Coefficient D			-2.16160e-04
Coefficient E			-6.89130e-07
Temperature range, min.			185.45
Temperature range, max.			488.00
λliquid	0.16	W/m×K	185.45	Calculated Property
λliquid	0.15	W/m×K	219.07	Calculated Property
λliquid	0.14	W/m×K	252.68	Calculated Property
λliquid	0.13	W/m×K	286.30	Calculated Property
λliquid	0.13	W/m×K	319.92	Calculated Property
λliquid	0.12	W/m×K	353.53	Calculated Property
λliquid	0.11	W/m×K	387.15	Calculated Property
λliquid	0.10	W/m×K	420.77	Calculated Property
λliquid	0.09	W/m×K	454.38	Calculated Property
λliquid	0.08	W/m×K	488.00	Calculated Property

Similar Compounds

Find more compounds similar to Nonane, 5-methyl-.

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
• 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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