Chemical Properties of Nonane, 4-methyl- (CAS 17301-94-9)

InChI

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

InChI Key

IALRSQMWHFKJJA-UHFFFAOYSA-N

Formula

C10H22

SMILES

CCCCCC(C)CCC

Molecular Weight¹

142.29

CAS

17301-94-9

Other Names

• 4-Methylnonane, (DL)-
• 4-methylnonane
• n-C3H7CH(CH3)(CH2)4CH3

• 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.
• 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; 0.4651]
ω	0.4651		ChemSep v8.3 pure component data Compiled value
ω	0.4510		KDB
AP	351.450	K	KDB
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	28.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δc,grossH	6775.57	kJ/mol	KDB
Δc,netH	6291.439	kJ/mol	KDB
ΔfH°gas	-254.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	18.13	kJ/mol	Joback Calculated Property
ΔvapH°	49.50	kJ/mol	NIST
IE	9.57	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	1.08e-07	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[955.00; 972.00]
Inp	960.00		NIST
Inp	Outlier 972.00		NIST
Inp	965.00		NIST
Inp	960.00		NIST
Inp	964.00		NIST
Inp	Outlier 970.00		NIST
Inp	Outlier 970.00		NIST
Inp	962.50		NIST
Inp	962.40		NIST
Inp	960.00		NIST
Inp	959.30		NIST
Inp	960.00		NIST
Inp	960.80		NIST
Inp	965.00		NIST
Inp	964.00		NIST
Inp	966.00		NIST
Inp	968.00		NIST
Inp	963.00		NIST
Inp	958.00		NIST
Inp	960.63		NIST
Inp	960.63		NIST
Inp	961.00		NIST
Inp	960.00		NIST
Inp	961.00		NIST
Inp	962.40		NIST
Inp	962.00		NIST
Inp	Outlier 955.00		NIST
Inp	961.00		NIST
Inp	967.00		NIST
Inp	960.00		NIST
Inp	963.80		NIST
Inp	962.10		NIST
Inp	961.60		NIST
Inp	962.00		NIST
Inp	963.54		NIST
Inp	963.12		NIST
Inp	963.33		NIST
Inp	963.34		NIST
Inp	962.48		NIST
Inp	962.63		NIST
Inp	962.67		NIST
Inp	Outlier 955.00		NIST
Inp	958.00		NIST
Inp	962.00		NIST
Inp	963.00		NIST
Inp	961.00		NIST
Inp	964.00		NIST
Inp	961.00		NIST
Inp	958.00		NIST
Inp	962.00		NIST
Inp	964.00		NIST
Inp	966.00		NIST
Inp	964.00		NIST
Inp	962.80		NIST
Inp	963.00		NIST
Inp	960.00		NIST
Inp	963.00		NIST
Inp	964.00		NIST
Inp	960.00		NIST
Inp	960.00		NIST
Inp	962.00		NIST
Inp	962.00		NIST
Inp	961.00		NIST
Inp	963.00		NIST
Inp	962.00		NIST
S°liquid	425.50	J/mol×K	NIST
Tboil	[438.85; 442.15]	K
Tboil	438.85	K	ChemSep v8.3 pure component data Compiled value
Tboil	438.90	K	KDB
Tboil	441.15 ± 2.00	K	NIST
Tboil	438.85 ± 0.50	K	NIST
Tboil	438.90 ± 0.50	K	NIST
Tboil	Outlier 442.15 ± 2.00	K	NIST
Tboil	438.90 ± 0.50	K	NIST
Tboil	438.90 ± 0.30	K	NIST
Tc	[610.50; 613.70]	K
Tc	613.70	K	ChemSep v8.3 pure component data Compiled value
Tc	610.50	K	KDB
Tfus	[171.53; 174.69]	K
Tfus	174.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	174.45	K	ChemSep v8.3 pure component data Compiled value
Tfus	174.00	K	KDB
Tfus	174.69 ± 0.20	K	NIST
Tfus	Outlier 171.53 ± 0.15	K	NIST
Tfus	174.69 ± 0.20	K	NIST
Ttriple	[174.45; 174.70]	K
Ttriple	174.45	K	ChemSep v8.3 pure component data Compiled value
Ttriple	174.70 ± 0.20	K	NIST
Ttriple	174.70 ± 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	[0.575; 0.590]	m3/kmol
Vc	0.590	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.575	m3/kmol	KDB
Zc	[0.2424150; 0.2480000]
Zc	0.2480000		ChemSep v8.3 pure component data Compiled value
Zc	0.2424150		KDB
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[263.70; 318.80]	J/mol×K	[180.00; 300.00]
Cp,liquid	263.70	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
Cp,liquid	265.90	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	268.60	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
Cp,liquid	271.70	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	275.30	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	279.20	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	283.60	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	288.40	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	293.60	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	299.30	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
Cp,liquid	301.20	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	305.40	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	311.90	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	317.36	J/mol×K	298.10	NIST
Cp,liquid	317.50	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	318.80	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	[15.19; 15.19]	kJ/mol	[174.70; 174.70]
ΔfusH	15.19	kJ/mol	174.70	NIST
ΔfusH	15.19	kJ/mol	174.70	NIST
ΔfusH	15.19	kJ/mol	174.70	NIST
ΔvapH	38.79	kJ/mol	438.90	KDB
n0	1.40950		298.15	KDB
ρl	[626.00; 739.36]	kg/m3	[283.15; 423.15]
ρl	739.36	kg/m3	283.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	735.55	kg/m3	288.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	731.74	kg/m3	293.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	728.35	kg/m3	298.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	727.93	kg/m3	298.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	724.10	kg/m3	303.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	720.25	kg/m3	308.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	716.40	kg/m3	313.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	712.53	kg/m3	318.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	708.63	kg/m3	323.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	708.82	kg/m3	323.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	704.73	kg/m3	328.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	700.81	kg/m3	333.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	696.87	kg/m3	338.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	692.92	kg/m3	343.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	688.94	kg/m3	348.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	689.00	kg/m3	348.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	684.94	kg/m3	353.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	680.92	kg/m3	358.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	676.88	kg/m3	363.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	668.81	kg/m3	373.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	647.86	kg/m3	398.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ρl	626.00	kg/m3	423.15	Viscosity and Surface Tension of Branched Alkanes 2-Methylnonane and 4-Methylnonane
ΔfusS	[86.94; 86.94]	J/mol×K	[174.70; 174.70]
ΔfusS	86.94	J/mol×K	174.70	NIST
ΔfusS	86.94	J/mol×K	174.70	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[145.41; 620.22]	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			1.30820e+02
Coefficient B			-5.89610e+02
Coefficient C			6.61124e+00
Coefficient D			-1.38110e-06
Coefficient E			-1.01820e-08
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	145.41	J/mol×K	150.00	Calculated Property
Cp,gas	234.84	J/mol×K	300.00	Calculated Property
Cp,gas	330.82	J/mol×K	450.00	Calculated Property
Cp,gas	407.83	J/mol×K	600.00	Calculated Property
Cp,gas	467.23	J/mol×K	750.00	Calculated Property
Cp,gas	513.28	J/mol×K	900.00	Calculated Property
Cp,gas	549.47	J/mol×K	1050.00	Calculated Property
Cp,gas	578.28	J/mol×K	1200.00	Calculated Property
Cp,gas	601.45	J/mol×K	1350.00	Calculated Property
Cp,gas	620.22	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[262.63; 535.64]	J/mol×K	[120.00; 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			4.19530e+01
Coefficient B			5.65000e+01
Coefficient C			4.57624e+00
Coefficient D			2.98610e-03
Coefficient E			-6.05500e-07
Temperature range, min.			120.00
Temperature range, max.			580.00
Cp,liquid	262.63	J/mol×K	120.00	Calculated Property
Cp,liquid	263.29	J/mol×K	171.11	Calculated Property
Cp,liquid	278.03	J/mol×K	222.22	Calculated Property
Cp,liquid	300.20	J/mol×K	273.33	Calculated Property
Cp,liquid	327.81	J/mol×K	324.44	Calculated Property
Cp,liquid	360.17	J/mol×K	375.56	Calculated Property
Cp,liquid	397.09	J/mol×K	426.67	Calculated Property
Cp,liquid	438.57	J/mol×K	477.78	Calculated Property
Cp,liquid	484.71	J/mol×K	528.89	Calculated Property
Cp,liquid	535.64	J/mol×K	580.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0136886; 0.0001506]	Pa×s	[174.45; 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			-8.71740e+00
Coefficient B			1.14850e+03
Coefficient C			-4.22780e-01
Coefficient D			8.18000e-07
Coefficient E			2.00000e+00
Temperature range, min.			174.45
Temperature range, max.			491.00
η	0.0136886	Pa×s	174.45	Calculated Property
η	0.0042432	Pa×s	209.62	Calculated Property
η	0.0018323	Pa×s	244.79	Calculated Property
η	0.0009748	Pa×s	279.97	Calculated Property
η	0.0005968	Pa×s	315.14	Calculated Property
η	0.0004034	Pa×s	350.31	Calculated Property
η	0.0002934	Pa×s	385.48	Calculated Property
η	0.0002256	Pa×s	420.66	Calculated Property
η	0.0001812	Pa×s	455.83	Calculated Property
η	0.0001506	Pa×s	491.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[55.27; 8.92]	kJ/mol	[174.45; 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			6.28730e+01
Coefficient B			3.94960e-01
Coefficient C			-5.41150e-02
Coefficient D			8.17790e-02
Coefficient E			-4.07010e-02
Critical temperature, Tc (K)			6.13700e+02
Temperature range, min.			174.45
Temperature range, max.			610.00
ΔvapH	55.27	kJ/mol	174.45	Calculated Property
ΔvapH	52.87	kJ/mol	222.84	Calculated Property
ΔvapH	50.27	kJ/mol	271.24	Calculated Property
ΔvapH	47.43	kJ/mol	319.63	Calculated Property
ΔvapH	44.27	kJ/mol	368.03	Calculated Property
ΔvapH	40.70	kJ/mol	416.42	Calculated Property
ΔvapH	36.54	kJ/mol	464.82	Calculated Property
ΔvapH	31.44	kJ/mol	513.21	Calculated Property
ΔvapH	24.46	kJ/mol	561.61	Calculated Property
ΔvapH	8.92	kJ/mol	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[320.68; 467.87]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47150e+01
Coefficient B			-3.97462e+03
Coefficient C			-4.51930e+01
Temperature range, min.			320.68
Temperature range, max.			467.87
Pvap	1.33	kPa	320.68	Calculated Property
Pvap	2.99	kPa	337.03	Calculated Property
Pvap	6.16	kPa	353.39	Calculated Property
Pvap	11.80	kPa	369.74	Calculated Property
Pvap	21.24	kPa	386.10	Calculated Property
Pvap	36.22	kPa	402.45	Calculated Property
Pvap	58.95	kPa	418.81	Calculated Property
Pvap	92.10	kPa	435.16	Calculated Property
Pvap	138.80	kPa	451.52	Calculated Property
Pvap	202.66	kPa	467.87	Calculated Property
Pvap	[2.35e-08; 2690.05]	kPa	[174.45; 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			1.36779e+02
Coefficient B			-1.06321e+04
Coefficient C			-1.81755e+01
Coefficient D			1.37486e-05
Coefficient E			2.00000e+00
Temperature range, min.			174.45
Temperature range, max.			610.00
Pvap	2.35e-08	kPa	174.45	Calculated Property
Pvap	2.01e-04	kPa	222.84	Calculated Property
Pvap	0.04	kPa	271.24	Calculated Property
Pvap	1.10	kPa	319.63	Calculated Property
Pvap	10.68	kPa	368.03	Calculated Property
Pvap	54.70	kPa	416.42	Calculated Property
Pvap	190.22	kPa	464.82	Calculated Property
Pvap	520.97	kPa	513.21	Calculated Property
Pvap	1234.23	kPa	561.61	Calculated Property
Pvap	2690.05	kPa	610.00	Calculated Property
Pvap	[1.05e-07; 2093.44]	kPa	[174.45; 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			7.38814e+01
Coefficient B			-8.08283e+03
Coefficient C			-8.47077e+00
Coefficient D			3.60829e-06
Coefficient E			0.00000e+00
Temperature range, min.			174.45
Temperature range, max.			610.00
Pvap	1.05e-07	kPa	174.45	Calculated Property
Pvap	3.33e-04	kPa	222.84	Calculated Property
Pvap	0.04	kPa	271.24	Calculated Property
Pvap	1.12	kPa	319.63	Calculated Property
Pvap	10.60	kPa	368.03	Calculated Property
Pvap	54.80	kPa	416.42	Calculated Property
Pvap	190.04	kPa	464.82	Calculated Property
Pvap	502.11	kPa	513.21	Calculated Property
Pvap	1097.01	kPa	561.61	Calculated Property
Pvap	2093.44	kPa	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[810.27; 259.53]	kg/m3	[174.45; 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			6.65210e+00
Coefficient B			8.56870e-02
Coefficient C			6.13700e+02
Coefficient D			1.39090e-01
Temperature range, min.			174.45
Temperature range, max.			610.00
ρl	810.27	kg/m3	174.45	Calculated Property
ρl	780.23	kg/m3	222.84	Calculated Property
ρl	748.11	kg/m3	271.24	Calculated Property
ρl	713.41	kg/m3	319.63	Calculated Property
ρl	675.37	kg/m3	368.03	Calculated Property
ρl	632.86	kg/m3	416.42	Calculated Property
ρl	583.88	kg/m3	464.82	Calculated Property
ρl	524.44	kg/m3	513.21	Calculated Property
ρl	443.86	kg/m3	561.61	Calculated Property
ρl	259.53	kg/m3	610.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 4.57e-06]	N/m	[174.45; 606.95]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-9.19150e-03
Coefficient B			4.16480e+01
Coefficient C			-3.21960e+00
Coefficient D			1.21500e-04
Coefficient E			-4.37510e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 610 K.
Temperature range, min.			174.45
Temperature range, max.			606.95
γ	0.04	N/m	174.45	Calculated Property
γ	0.03	N/m	222.51	Calculated Property
γ	0.03	N/m	270.56	Calculated Property
γ	0.02	N/m	318.62	Calculated Property
γ	0.02	N/m	366.67	Calculated Property
γ	0.01	N/m	414.73	Calculated Property
γ	0.01	N/m	462.78	Calculated Property
γ	0.01	N/m	510.84	Calculated Property
γ	0.00	N/m	558.90	Calculated Property
γ	4.57e-06	N/m	606.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[174.45; 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			3.93320e-05
Coefficient B			1.11310e+00
Coefficient C			-1.52110e+02
Coefficient D			1.74490e+05
Temperature range, min.			174.45
Temperature range, max.			1000.00
λgas	0.00	W/m×K	174.45	Calculated Property
λgas	0.01	W/m×K	266.18	Calculated Property
λgas	0.01	W/m×K	357.91	Calculated Property
λgas	0.02	W/m×K	449.63	Calculated Property
λgas	0.03	W/m×K	541.36	Calculated Property
λgas	0.04	W/m×K	633.09	Calculated Property
λgas	0.05	W/m×K	724.82	Calculated Property
λgas	0.06	W/m×K	816.54	Calculated Property
λgas	0.07	W/m×K	908.27	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	[174.45; 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			-1.61980e-01
Coefficient B			1.25310e+01
Coefficient C			-1.14390e+00
Coefficient D			-1.90060e-04
Coefficient E			-7.90790e-07
Temperature range, min.			174.45
Temperature range, max.			488.00
λliquid	0.16	W/m×K	174.45	Calculated Property
λliquid	0.15	W/m×K	209.29	Calculated Property
λliquid	0.14	W/m×K	244.13	Calculated Property
λliquid	0.14	W/m×K	278.97	Calculated Property
λliquid	0.13	W/m×K	313.81	Calculated Property
λliquid	0.12	W/m×K	348.64	Calculated Property
λliquid	0.11	W/m×K	383.48	Calculated Property
λliquid	0.10	W/m×K	418.32	Calculated Property
λliquid	0.09	W/m×K	453.16	Calculated Property
λliquid	0.08	W/m×K	488.00	Calculated Property

Similar Compounds

Find more compounds similar to Nonane, 4-methyl-.

Mixtures

• Nonane, 4-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
• 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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