Chemical Properties of Nonane, 3-methyl- (CAS 5911-04-6)

InChI

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

InChI Key

PLZDDPSCZHRBOY-UHFFFAOYSA-N

Formula

C10H22

SMILES

CCCCCCC(C)CC

Molecular Weight¹

142.28

CAS

5911-04-6

Other Names

• 3-Methylnonane
• 3-Methylnonane(DL)
• 3-Methylnonane, (DL)-

• ω : Acentric Factor.
• AP : Aniline Point (K).
• 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_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	[0.4510; 0.4649]
ω	0.4649		ChemSep v8.3 pure component data Compiled value
ω	0.4510		KDB
AP	351.350	K	KDB
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	28.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δc,grossH	6775.15	kJ/mol	KDB
Δc,netH	6291.021	kJ/mol	KDB
ΔfH°gas	-254.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	18.13	kJ/mol	Joback Calculated Property
ΔvapH°	[49.72; 50.20]	kJ/mol
ΔvapH°	49.72	kJ/mol	NIST
ΔvapH°	50.20	kJ/mol	NIST
IE	9.60	eV	Relay (1.0) Calculated Property
log10WS	-5.78		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	5.65e-07	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[958.00; 980.00]
Inp	969.00		NIST
Inp	973.00		NIST
Inp	976.00		NIST
Inp	970.00		NIST
Inp	970.40		NIST
Inp	970.50		NIST
Inp	970.00		NIST
Inp	967.00		NIST
Inp	Outlier 979.00		NIST
Inp	974.00		NIST
Inp	972.00		NIST
Inp	Outlier 980.00		NIST
Inp	976.00		NIST
Inp	971.20		NIST
Inp	971.30		NIST
Inp	973.00		NIST
Inp	970.40		NIST
Inp	970.60		NIST
Inp	972.50		NIST
Inp	970.40		NIST
Inp	971.30		NIST
Inp	969.60		NIST
Inp	970.20		NIST
Inp	973.00		NIST
Inp	Outlier 958.00		NIST
Inp	970.42		NIST
Inp	970.42		NIST
Inp	970.00		NIST
Inp	970.00		NIST
Inp	977.00		NIST
Inp	971.92		NIST
Inp	970.00		NIST
Inp	970.00		NIST
Inp	971.00		NIST
Inp	977.20		NIST
Inp	Outlier 979.00		NIST
Inp	969.00		NIST
Inp	972.00		NIST
Inp	976.00		NIST
Inp	Outlier 962.00		NIST
Inp	972.80		NIST
Inp	969.00		NIST
Inp	971.20		NIST
Inp	970.50		NIST
Inp	971.70		NIST
Inp	974.20		NIST
Inp	972.00		NIST
Inp	971.00		NIST
Inp	971.80		NIST
Inp	972.15		NIST
Inp	972.23		NIST
Inp	971.40		NIST
Inp	971.74		NIST
Inp	971.85		NIST
Inp	970.00		NIST
Inp	968.00		NIST
Inp	970.00		NIST
Inp	Outlier 960.00		NIST
Inp	971.00		NIST
Inp	969.00		NIST
Inp	970.00		NIST
Inp	975.00		NIST
Inp	970.00		NIST
Inp	974.00		NIST
Inp	973.00		NIST
Inp	972.10		NIST
Inp	967.00		NIST
Inp	970.00		NIST
Inp	964.00		NIST
Inp	976.00		NIST
Inp	966.00		NIST
Inp	968.00		NIST
Inp	972.00		NIST
Inp	973.00		NIST
Inp	970.00		NIST
Inp	970.00		NIST
Inp	972.00		NIST
Inp	970.00		NIST
Inp	970.00		NIST
Inp	973.00		NIST
Inp	972.00		NIST
Inp	966.00		NIST
Inp	970.00		NIST
Inp	971.40		NIST
Inp	977.00		NIST
Inp	971.00		NIST
Inp	973.00		NIST
Inp	970.00		NIST
Inp	977.00		NIST
Inp	Outlier 960.00		NIST
Inp	977.20		NIST
Inp	972.00		NIST
Inp	966.00		NIST
Inp	971.00		NIST
Ip	[965.00; 983.00]
Ip	983.00		NIST
Ip	969.00		NIST
Ip	965.00		NIST
Ip	969.00		NIST
Ip	983.00		NIST
S°liquid	427.20	J/mol×K	NIST
Tboil	[440.65; 441.00]	K
Tboil	440.95	K	ChemSep v8.3 pure component data Compiled value
Tboil	441.00	K	KDB
Tboil	441.00	K	NIST
Tboil	Outlier 440.65 ± 1.00	K	NIST
Tboil	440.95 ± 0.30	K	NIST
Tboil	441.00 ± 0.30	K	NIST
Tboil	441.00 ± 0.30	K	NIST
Tboil	440.75 ± 0.50	K	NIST
Tboil	441.00 ± 0.30	K	NIST
Tc	[613.40; 613.70]	K
Tc	613.70	K	ChemSep v8.3 pure component data Compiled value
Tc	613.40	K	KDB
Tc	613.60	K	NIST
Tfus	[183.15; 188.49]	K
Tfus	188.25	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	188.35	K	ChemSep v8.3 pure component data Compiled value
Tfus	188.00	K	KDB
Tfus	188.49 ± 0.20	K	NIST
Tfus	Outlier 183.15 ± 0.50	K	NIST
Tfus	188.29 ± 0.20	K	NIST
Tfus	188.49 ± 0.20	K	NIST
Ttriple	[188.35; 188.50]	K
Ttriple	188.35	K	ChemSep v8.3 pure component data Compiled value
Ttriple	188.50 ± 0.20	K	NIST
Ttriple	188.50 ± 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	[0.582; 0.590]	m3/kmol
Vc	0.590	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.582	m3/kmol	KDB
Zc	[0.2442060; 0.2470000]
Zc	0.2470000		ChemSep v8.3 pure component data Compiled value
Zc	0.2442060		KDB
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[263.80; 310.60]	J/mol×K	[190.00; 300.00]
Cp,liquid	263.80	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	266.30	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	269.20	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	272.40	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	276.00	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	279.90	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	284.10	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	288.70	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	293.70	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	295.30	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	299.00	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	304.60	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	308.99	J/mol×K	298.10	NIST
Cp,liquid	309.50	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	310.60	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	[18.70; 18.70]	kJ/mol	[188.50; 188.50]
ΔfusH	18.70	kJ/mol	188.50	NIST
ΔfusH	18.70	kJ/mol	188.50	NIST
ΔfusH	18.70	kJ/mol	188.50	NIST
ΔvapH	[38.26; 47.30]	kJ/mol	[328.00; 441.00]
ΔvapH	47.30 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	46.20 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	45.10 ± 0.20	kJ/mol	358.00	NIST
ΔvapH	39.12	kJ/mol	441.00	KDB
ΔvapH	38.26	kJ/mol	441.00	NIST
n0	1.41030		298.15	KDB
ΔfusS	[99.20; 99.20]	J/mol×K	[188.50; 188.50]
ΔfusS	99.20	J/mol×K	188.50	NIST
ΔfusS	99.20	J/mol×K	188.50	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[146.83; 620.43]	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			1.33050e+02
Coefficient B			-5.99420e+02
Coefficient C			6.62224e+00
Coefficient D			-1.73530e-05
Coefficient E			-3.36300e-09
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	146.83	J/mol×K	150.00	Calculated Property
Cp,gas	234.41	J/mol×K	300.00	Calculated Property
Cp,gas	329.76	J/mol×K	450.00	Calculated Property
Cp,gas	406.63	J/mol×K	600.00	Calculated Property
Cp,gas	466.04	J/mol×K	750.00	Calculated Property
Cp,gas	512.18	J/mol×K	900.00	Calculated Property
Cp,gas	548.53	J/mol×K	1050.00	Calculated Property
Cp,gas	577.60	J/mol×K	1200.00	Calculated Property
Cp,gas	601.15	J/mol×K	1350.00	Calculated Property
Cp,gas	620.43	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[263.53; 507.54]	J/mol×K	[188.35; 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			7.85060e+01
Coefficient B			7.48920e+01
Coefficient C			4.11524e+00
Coefficient D			4.05680e-03
Coefficient E			-1.59270e-06
Temperature range, min.			188.35
Temperature range, max.			580.00
Cp,liquid	263.53	J/mol×K	188.35	Calculated Property
Cp,liquid	277.50	J/mol×K	231.87	Calculated Property
Cp,liquid	296.31	J/mol×K	275.38	Calculated Property
Cp,liquid	318.79	J/mol×K	318.90	Calculated Property
Cp,liquid	344.36	J/mol×K	362.42	Calculated Property
Cp,liquid	372.65	J/mol×K	405.93	Calculated Property
Cp,liquid	403.39	J/mol×K	449.45	Calculated Property
Cp,liquid	436.31	J/mol×K	492.97	Calculated Property
Cp,liquid	471.13	J/mol×K	536.48	Calculated Property
Cp,liquid	507.54	J/mol×K	580.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0086669; 0.0001510]	Pa×s	[188.35; 490.96]	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			-1.29220e+01
Coefficient B			1.26730e+03
Coefficient C			2.81590e-01
Coefficient D			-8.38070e-07
Coefficient E			2.00000e+00
Temperature range, min.			188.35
Temperature range, max.			490.96
η	0.0086669	Pa×s	188.35	Calculated Property
η	0.0032382	Pa×s	221.97	Calculated Property
η	0.0015687	Pa×s	255.60	Calculated Property
η	0.0008988	Pa×s	289.22	Calculated Property
η	0.0005773	Pa×s	322.84	Calculated Property
η	0.0004022	Pa×s	356.47	Calculated Property
η	0.0002973	Pa×s	390.09	Calculated Property
η	0.0002298	Pa×s	423.71	Calculated Property
η	0.0001839	Pa×s	457.34	Calculated Property
η	0.0001510	Pa×s	490.96	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[60.00; 3.50]	kJ/mol	[188.35; 613.00]	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			8.35416e+01
Coefficient B			1.02448e+00
Coefficient C			-9.08156e-02
Coefficient D			-1.22812e+00
Coefficient E			7.62381e-01
Critical temperature, Tc (K)			6.13700e+02
Temperature range, min.			188.35
Temperature range, max.			613.00
ΔvapH	60.00	kJ/mol	188.35	Calculated Property
ΔvapH	55.31	kJ/mol	235.53	Calculated Property
ΔvapH	51.09	kJ/mol	282.72	Calculated Property
ΔvapH	47.24	kJ/mol	329.90	Calculated Property
ΔvapH	43.62	kJ/mol	377.08	Calculated Property
ΔvapH	40.00	kJ/mol	424.27	Calculated Property
ΔvapH	36.01	kJ/mol	471.45	Calculated Property
ΔvapH	31.05	kJ/mol	518.63	Calculated Property
ΔvapH	23.68	kJ/mol	565.82	Calculated Property
ΔvapH	3.50	kJ/mol	613.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[323.99; 469.90]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45072e+01
Coefficient B			-3.79773e+03
Coefficient C			-5.69090e+01
Temperature range, min.			323.99
Temperature range, max.			469.90
Pvap	1.33	kPa	323.99	Calculated Property
Pvap	3.01	kPa	340.20	Calculated Property
Pvap	6.22	kPa	356.41	Calculated Property
Pvap	11.92	kPa	372.63	Calculated Property
Pvap	21.45	kPa	388.84	Calculated Property
Pvap	36.55	kPa	405.05	Calculated Property
Pvap	59.38	kPa	421.26	Calculated Property
Pvap	92.58	kPa	437.48	Calculated Property
Pvap	139.18	kPa	453.69	Calculated Property
Pvap	202.66	kPa	469.90	Calculated Property
Pvap	[1.39e-06; 2162.45]	kPa	[188.35; 613.00]	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			8.38302e+01
Coefficient B			-8.47680e+03
Coefficient C			-1.00230e+01
Coefficient D			5.34480e-06
Coefficient E			2.00000e+00
Temperature range, min.			188.35
Temperature range, max.			613.00
Pvap	1.39e-06	kPa	188.35	Calculated Property
Pvap	1.35e-03	kPa	235.53	Calculated Property
Pvap	0.10	kPa	282.72	Calculated Property
Pvap	1.81	kPa	329.90	Calculated Property
Pvap	14.14	kPa	377.08	Calculated Property
Pvap	64.69	kPa	424.27	Calculated Property
Pvap	208.14	kPa	471.45	Calculated Property
Pvap	527.24	kPa	518.63	Calculated Property
Pvap	1131.57	kPa	565.82	Calculated Property
Pvap	2162.45	kPa	613.00	Calculated Property
Pvap	[5.74e-07; 2188.73]	kPa	[188.35; 613.00]	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			1.11505e+02
Coefficient B			-9.76977e+03
Coefficient C			-1.41847e+01
Coefficient D			8.42650e-06
Coefficient E			0.00000e+00
Temperature range, min.			188.35
Temperature range, max.			613.00
Pvap	5.74e-07	kPa	188.35	Calculated Property
Pvap	9.29e-04	kPa	235.53	Calculated Property
Pvap	0.09	kPa	282.72	Calculated Property
Pvap	1.74	kPa	329.90	Calculated Property
Pvap	14.07	kPa	377.08	Calculated Property
Pvap	64.82	kPa	424.27	Calculated Property
Pvap	207.81	kPa	471.45	Calculated Property
Pvap	524.56	kPa	518.63	Calculated Property
Pvap	1129.44	kPa	565.82	Calculated Property
Pvap	2188.73	kPa	613.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[799.81; 250.54]	kg/m3	[188.35; 613.00]	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			2.70506e+01
Coefficient B			1.73190e-01
Coefficient C			6.13700e+02
Coefficient D			1.93490e-01
Temperature range, min.			188.35
Temperature range, max.			613.00
ρl	799.81	kg/m3	188.35	Calculated Property
ρl	770.96	kg/m3	235.53	Calculated Property
ρl	740.26	kg/m3	282.72	Calculated Property
ρl	707.25	kg/m3	329.90	Calculated Property
ρl	671.27	kg/m3	377.08	Calculated Property
ρl	631.28	kg/m3	424.27	Calculated Property
ρl	585.49	kg/m3	471.45	Calculated Property
ρl	530.24	kg/m3	518.63	Calculated Property
ρl	455.52	kg/m3	565.82	Calculated Property
ρl	250.54	kg/m3	613.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 1.91e-05]	N/m	[188.35; 608.75]	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			-1.11700e-02
Coefficient B			4.56770e+01
Coefficient C			-3.25660e+00
Coefficient D			3.04030e-04
Coefficient E			-4.03780e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 613 K.
Temperature range, min.			188.35
Temperature range, max.			608.75
γ	0.03	N/m	188.35	Calculated Property
γ	0.03	N/m	235.06	Calculated Property
γ	0.02	N/m	281.77	Calculated Property
γ	0.02	N/m	328.48	Calculated Property
γ	0.02	N/m	375.20	Calculated Property
γ	0.01	N/m	421.91	Calculated Property
γ	0.01	N/m	468.62	Calculated Property
γ	0.01	N/m	515.33	Calculated Property
γ	0.00	N/m	562.04	Calculated Property
γ	1.91e-05	N/m	608.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[188.35; 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			3.34070e-05
Coefficient B			1.13380e+00
Coefficient C			-1.62760e+02
Coefficient D			1.71650e+05
Temperature range, min.			188.35
Temperature range, max.			1000.00
λgas	0.00	W/m×K	188.35	Calculated Property
λgas	0.01	W/m×K	278.53	Calculated Property
λgas	0.01	W/m×K	368.72	Calculated Property
λgas	0.02	W/m×K	458.90	Calculated Property
λgas	0.03	W/m×K	549.08	Calculated Property
λgas	0.04	W/m×K	639.27	Calculated Property
λgas	0.05	W/m×K	729.45	Calculated Property
λgas	0.06	W/m×K	819.63	Calculated Property
λgas	0.07	W/m×K	909.82	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	[188.35; 490.00]	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			-1.78100e-01
Coefficient B			1.05570e+01
Coefficient C			-1.07800e+00
Coefficient D			-2.31480e-04
Coefficient E			-6.82210e-07
Temperature range, min.			188.35
Temperature range, max.			490.00
λliquid	0.16	W/m×K	188.35	Calculated Property
λliquid	0.15	W/m×K	221.87	Calculated Property
λliquid	0.14	W/m×K	255.38	Calculated Property
λliquid	0.13	W/m×K	288.90	Calculated Property
λliquid	0.13	W/m×K	322.42	Calculated Property
λliquid	0.12	W/m×K	355.93	Calculated Property
λliquid	0.11	W/m×K	389.45	Calculated Property
λliquid	0.10	W/m×K	422.97	Calculated Property
λliquid	0.09	W/m×K	456.48	Calculated Property
λliquid	0.09	W/m×K	490.00	Calculated Property

Similar Compounds

Find more compounds similar to Nonane, 3-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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