Chemical Properties of Octane, 4-methyl- (CAS 2216-34-4)

InChI

InChI=1S/C9H20/c1-4-6-8-9(3)7-5-2/h9H,4-8H2,1-3H3

InChI Key

DOGIHOCMZJUJNR-UHFFFAOYSA-N

Formula

C9H20

SMILES

CCCCC(C)CCC

Molecular Weight¹

128.26

CAS

2216-34-4

Other Names

• 1,3-Dimethylheptane
• 4-methyloctane

• 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_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.
• 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	[0.4129; 0.4160]
ω	0.4129		ChemSep v8.3 pure component data Compiled value
ω	0.4160		KDB
AP	347.650	K	KDB
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	21.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δc,grossH	6121.78	kJ/mol	KDB
Δc,netH	5681.663	kJ/mol	KDB
ΔfH°gas	-233.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	15.54	kJ/mol	Joback Calculated Property
ΔvapH°	44.50	kJ/mol	NIST
IE	9.65	eV	Relay (1.0) Calculated Property
log10WS	-5.43		Relay (1.0) Calculated Property
logPoct/wat	3.613		Crippen Calculated Property
McVol	137.670	ml/mol	McGowan Calculated Property
Pc	[2330.00; 2340.00]	kPa
Pc	2340.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2330.00	kPa	KDB
Ptriple	3.18e-08	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[856.30; 881.00]
Inp	863.00		NIST
Inp	863.00		NIST
Inp	862.00		NIST
Inp	862.50		NIST
Inp	862.70		NIST
Inp	864.60		NIST
Inp	864.70		NIST
Inp	861.00		NIST
Inp	863.30		NIST
Inp	863.00		NIST
Inp	863.10		NIST
Inp	868.00		NIST
Inp	861.00		NIST
Inp	862.00		NIST
Inp	860.00		NIST
Inp	859.00		NIST
Inp	863.00		NIST
Inp	863.00		NIST
Inp	863.00		NIST
Inp	862.00		NIST
Inp	863.00		NIST
Inp	864.00		NIST
Inp	866.00		NIST
Inp	862.85		NIST
Inp	863.00		NIST
Inp	861.00		NIST
Inp	861.00		NIST
Inp	Outlier 874.40		NIST
Inp	868.00		NIST
Inp	863.00		NIST
Inp	864.00		NIST
Inp	865.90		NIST
Inp	863.50		NIST
Inp	Outlier 856.30		NIST
Inp	863.70		NIST
Inp	862.91		NIST
Inp	863.09		NIST
Inp	866.00		NIST
Inp	865.16		NIST
Inp	865.34		NIST
Inp	865.43		NIST
Inp	864.58		NIST
Inp	864.75		NIST
Inp	864.91		NIST
Inp	861.00		NIST
Inp	858.00		NIST
Inp	864.00		NIST
Inp	863.00		NIST
Inp	864.00		NIST
Inp	865.00		NIST
Inp	864.00		NIST
Inp	865.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	864.10		NIST
Inp	865.00		NIST
Inp	864.00		NIST
Inp	863.00		NIST
Inp	863.00		NIST
Inp	864.00		NIST
Inp	Outlier 873.00		NIST
Inp	868.00		NIST
Inp	861.00		NIST
Inp	861.00		NIST
Inp	Outlier 881.00		NIST
Inp	Outlier 875.00		NIST
Inp	865.90		NIST
Inp	863.09		NIST
Inp	864.58		NIST
Ip	[823.00; 823.00]
Ip	823.00		NIST
Ip	823.00		NIST
Ip	823.00		NIST
Tboil	[414.10; 416.00]	K
Tboil	415.59	K	ChemSep v8.3 pure component data Compiled value
Tboil	415.60	K	KDB
Tboil	416.00 ± 2.00	K	NIST
Tboil	416.00 ± 3.00	K	NIST
Tboil	Outlier 414.15 ± 2.00	K	NIST
Tboil	Outlier 414.10 ± 2.00	K	NIST
Tboil	415.57 ± 0.20	K	NIST
Tboil	415.45 ± 0.40	K	NIST
Tboil	415.61 ± 0.30	K	NIST
Tboil	415.60 ± 0.30	K	NIST
Tboil	415.60 ± 0.30	K	NIST
Tboil	415.64 ± 0.20	K	NIST
Tboil	415.64 ± 0.20	K	NIST
Tboil	415.58 ± 0.15	K	NIST
Tboil	415.63 ± 0.10	K	NIST
Tboil	414.75 ± 0.70	K	NIST
Tboil	414.75 ± 0.30	K	NIST
Tboil	414.75 ± 0.30	K	NIST
Tc	[586.70; 587.65]	K
Tc	587.65	K	ChemSep v8.3 pure component data Compiled value
Tc	586.70	K	KDB
Tfus	[154.02; 219.62]	K
Tfus	160.00	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	159.95	K	ChemSep v8.3 pure component data Compiled value
Tfus	160.00	K	KDB
Tfus	Outlier 219.62 ± 0.20	K	NIST
Tfus	159.95 ± 0.50	K	NIST
Tfus	154.02 ± 0.15	K	NIST
Tfus	159.85 ± 0.15	K	NIST
Ttriple	159.95	K	ChemSep v8.3 pure component data Compiled value
UQi	5.47		ChemSep v8.3 pure component data Compiled value
URi	6.52		ChemSep v8.3 pure component data Compiled value
Vc	[0.523; 0.533]	m3/kmol
Vc	0.523	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.533	m3/kmol	KDB
Zc	[0.2500000; 0.2548220]
Zc	0.2500000		ChemSep v8.3 pure component data Compiled value
Zc	0.2548220		KDB
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔvapH	36.61	kJ/mol	415.60	KDB
n0	1.40390		298.15	KDB
ρl	[653.90; 727.60]	kg/m3	[283.15; 373.15]
ρl	727.50	kg/m3	283.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	727.60	kg/m3	283.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	719.80	kg/m3	293.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	719.70	kg/m3	293.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	711.70	kg/m3	303.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	711.90	kg/m3	303.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	703.70	kg/m3	313.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	703.90	kg/m3	313.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	695.70	kg/m3	323.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	695.90	kg/m3	323.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	687.50	kg/m3	333.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	679.30	kg/m3	343.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	671.00	kg/m3	353.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	662.50	kg/m3	363.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
ρl	653.90	kg/m3	373.15	Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[130.04; 563.57]	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			1.16790e+02
Coefficient B			-5.88340e+02
Coefficient C			6.50424e+00
Coefficient D			1.52010e-05
Coefficient E			-1.45610e-08
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	130.04	J/mol×K	150.00	Calculated Property
Cp,gas	211.08	J/mol×K	300.00	Calculated Property
Cp,gas	298.19	J/mol×K	450.00	Calculated Property
Cp,gas	368.32	J/mol×K	600.00	Calculated Property
Cp,gas	422.61	J/mol×K	750.00	Calculated Property
Cp,gas	464.87	J/mol×K	900.00	Calculated Property
Cp,gas	498.18	J/mol×K	1050.00	Calculated Property
Cp,gas	524.78	J/mol×K	1200.00	Calculated Property
Cp,gas	546.20	J/mol×K	1350.00	Calculated Property
Cp,gas	563.57	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[232.61; 409.20]	J/mol×K	[159.95; 500.00]	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			7.15820e+01
Coefficient B			1.00570e+02
Coefficient C			3.70424e+00
Coefficient D			5.07830e-03
Coefficient E			-2.49050e-06
Temperature range, min.			159.95
Temperature range, max.			500.00
Cp,liquid	232.61	J/mol×K	159.95	Calculated Property
Cp,liquid	238.86	J/mol×K	197.73	Calculated Property
Cp,liquid	250.90	J/mol×K	235.52	Calculated Property
Cp,liquid	266.80	J/mol×K	273.30	Calculated Property
Cp,liquid	285.65	J/mol×K	311.08	Calculated Property
Cp,liquid	306.93	J/mol×K	348.87	Calculated Property
Cp,liquid	330.25	J/mol×K	386.65	Calculated Property
Cp,liquid	355.29	J/mol×K	424.43	Calculated Property
Cp,liquid	381.72	J/mol×K	462.22	Calculated Property
Cp,liquid	409.20	J/mol×K	500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0151918; 0.0001300]	Pa×s	[159.95; 470.12]	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			-1.18370e+01
Coefficient B			1.16200e+03
Coefficient C			7.72370e-02
Coefficient D			-2.63360e-07
Coefficient E			2.00000e+00
Temperature range, min.			159.95
Temperature range, max.			470.12
η	0.0151918	Pa×s	159.95	Calculated Property
η	0.0042410	Pa×s	194.41	Calculated Property
η	0.0017395	Pa×s	228.88	Calculated Property
η	0.0009008	Pa×s	263.34	Calculated Property
η	0.0005430	Pa×s	297.80	Calculated Property
η	0.0003632	Pa×s	332.27	Calculated Property
η	0.0002618	Pa×s	366.73	Calculated Property
η	0.0001994	Pa×s	401.19	Calculated Property
η	0.0001584	Pa×s	435.66	Calculated Property
η	0.0001300	Pa×s	470.12	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[52.38; 0.00]	kJ/mol	[159.95; 587.65]	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			6.29160e+01
Coefficient B			7.44600e-01
Coefficient C			-8.08820e-01
Coefficient D			8.02280e-01
Coefficient E			-3.38950e-01
Critical temperature, Tc (K)			5.87650e+02
Temperature range, min.			159.95
Temperature range, max.			587.65
ΔvapH	52.38	kJ/mol	159.95	Calculated Property
ΔvapH	49.64	kJ/mol	207.47	Calculated Property
ΔvapH	46.88	kJ/mol	254.99	Calculated Property
ΔvapH	44.00	kJ/mol	302.52	Calculated Property
ΔvapH	40.89	kJ/mol	350.04	Calculated Property
ΔvapH	37.45	kJ/mol	397.56	Calculated Property
ΔvapH	33.50	kJ/mol	445.08	Calculated Property
ΔvapH	28.71	kJ/mol	492.61	Calculated Property
ΔvapH	22.11	kJ/mol	540.13	Calculated Property
ΔvapH	0.00	kJ/mol	587.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[302.68; 443.50]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45395e+01
Coefficient B			-3.68657e+03
Coefficient C			-4.40050e+01
Temperature range, min.			302.68
Temperature range, max.			443.50
Pvap	1.33	kPa	302.68	Calculated Property
Pvap	3.01	kPa	318.33	Calculated Property
Pvap	6.21	kPa	333.97	Calculated Property
Pvap	11.90	kPa	349.62	Calculated Property
Pvap	21.42	kPa	365.27	Calculated Property
Pvap	36.50	kPa	380.91	Calculated Property
Pvap	59.31	kPa	396.56	Calculated Property
Pvap	92.50	kPa	412.21	Calculated Property
Pvap	139.12	kPa	427.85	Calculated Property
Pvap	202.65	kPa	443.50	Calculated Property
Pvap	[2.27e-09; 2340.00]	kPa	[159.95; 573.23]	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			1.61583e+02
Coefficient B			-1.11386e+04
Coefficient C			-2.21349e+01
Coefficient D			1.88399e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 587.65 K.
Temperature range, min.			159.95
Temperature range, max.			573.23
Pvap	2.27e-09	kPa	159.95	Calculated Property
Pvap	6.50e-05	kPa	205.87	Calculated Property
Pvap	0.02	kPa	251.79	Calculated Property
Pvap	0.78	kPa	297.71	Calculated Property
Pvap	8.46	kPa	343.63	Calculated Property
Pvap	45.36	kPa	389.55	Calculated Property
Pvap	160.27	kPa	435.47	Calculated Property
Pvap	441.85	kPa	481.39	Calculated Property
Pvap	1055.61	kPa	527.31	Calculated Property
Pvap	2340.00	kPa	573.23	Calculated Property
Pvap	[3.07e-08; 2243.54]	kPa	[159.95; 587.65]	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			7.99304e+01
Coefficient B			-7.86955e+03
Coefficient C			-9.48846e+00
Coefficient D			4.85511e-06
Coefficient E			0.00000e+00
Temperature range, min.			159.95
Temperature range, max.			587.65
Pvap	3.07e-08	kPa	159.95	Calculated Property
Pvap	2.22e-04	kPa	207.47	Calculated Property
Pvap	0.04	kPa	254.99	Calculated Property
Pvap	1.18	kPa	302.52	Calculated Property
Pvap	11.70	kPa	350.04	Calculated Property
Pvap	61.04	kPa	397.56	Calculated Property
Pvap	210.19	kPa	445.08	Calculated Property
Pvap	548.67	kPa	492.61	Calculated Property
Pvap	1184.99	kPa	540.13	Calculated Property
Pvap	2243.54	kPa	587.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[814.75; 245.46]	kg/m3	[159.95; 587.65]	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			6.58410e+01
Coefficient B			2.68240e-01
Coefficient C			5.87650e+02
Coefficient D			2.90750e-01
Temperature range, min.			159.95
Temperature range, max.			587.65
ρl	814.75	kg/m3	159.95	Calculated Property
ρl	782.50	kg/m3	207.47	Calculated Property
ρl	748.70	kg/m3	254.99	Calculated Property
ρl	712.99	kg/m3	302.52	Calculated Property
ρl	674.79	kg/m3	350.04	Calculated Property
ρl	633.26	kg/m3	397.56	Calculated Property
ρl	586.89	kg/m3	445.08	Calculated Property
ρl	532.66	kg/m3	492.61	Calculated Property
ρl	462.42	kg/m3	540.13	Calculated Property
ρl	245.46	kg/m3	587.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[160.15; 415.15]	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			4.98961e-02
Coefficient B			-9.40000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			160.15
Temperature range, max.			415.15
γ	0.03	N/m	160.15	Calculated Property
γ	0.03	N/m	188.48	Calculated Property
γ	0.03	N/m	216.82	Calculated Property
γ	0.03	N/m	245.15	Calculated Property
γ	0.02	N/m	273.48	Calculated Property
γ	0.02	N/m	301.82	Calculated Property
γ	0.02	N/m	330.15	Calculated Property
γ	0.02	N/m	358.48	Calculated Property
γ	0.01	N/m	386.82	Calculated Property
γ	0.01	N/m	415.15	Calculated Property
γ	[0.04; 1.16e-05]	N/m	[159.95; 583.37]	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			-9.01330e-03
Coefficient B			2.79890e+01
Coefficient C			-3.17720e+00
Coefficient D			1.38170e-04
Coefficient E			-4.87520e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 587.65 K.
Temperature range, min.			159.95
Temperature range, max.			583.37
γ	0.04	N/m	159.95	Calculated Property
γ	0.03	N/m	207.00	Calculated Property
γ	0.03	N/m	254.04	Calculated Property
γ	0.02	N/m	301.09	Calculated Property
γ	0.02	N/m	348.14	Calculated Property
γ	0.01	N/m	395.18	Calculated Property
γ	0.01	N/m	442.23	Calculated Property
γ	0.01	N/m	489.28	Calculated Property
γ	0.00	N/m	536.33	Calculated Property
γ	1.16e-05	N/m	583.37	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.09]	W/m×K	[159.95; 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			3.87840e-05
Coefficient B			1.11700e+00
Coefficient C			-1.85060e+02
Coefficient D			1.77130e+05
Temperature range, min.			159.95
Temperature range, max.			1000.00
λgas	0.00	W/m×K	159.95	Calculated Property
λgas	0.01	W/m×K	253.29	Calculated Property
λgas	0.01	W/m×K	346.63	Calculated Property
λgas	0.02	W/m×K	439.97	Calculated Property
λgas	0.03	W/m×K	533.31	Calculated Property
λgas	0.04	W/m×K	626.64	Calculated Property
λgas	0.06	W/m×K	719.98	Calculated Property
λgas	0.07	W/m×K	813.32	Calculated Property
λgas	0.08	W/m×K	906.66	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.08]	W/m×K	[159.95; 470.00]	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			-1.66300e-01
Coefficient B			9.28480e+00
Coefficient C			-1.10680e+00
Coefficient D			-2.84050e-04
Coefficient E			-7.40800e-07
Temperature range, min.			159.95
Temperature range, max.			470.00
λliquid	0.16	W/m×K	159.95	Calculated Property
λliquid	0.15	W/m×K	194.40	Calculated Property
λliquid	0.14	W/m×K	228.85	Calculated Property
λliquid	0.14	W/m×K	263.30	Calculated Property
λliquid	0.13	W/m×K	297.75	Calculated Property
λliquid	0.12	W/m×K	332.20	Calculated Property
λliquid	0.11	W/m×K	366.65	Calculated Property
λliquid	0.10	W/m×K	401.10	Calculated Property
λliquid	0.09	W/m×K	435.55	Calculated Property
λliquid	0.08	W/m×K	470.00	Calculated Property

Similar Compounds

Find more compounds similar to Octane, 4-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).
• 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).
• 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
• 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

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