Chemical Properties of Hexane, 2-methyl- (CAS 591-76-4)

InChI

InChI=1S/C7H16/c1-4-5-6-7(2)3/h7H,4-6H2,1-3H3

InChI Key

GXDHCNNESPLIKD-UHFFFAOYSA-N

Formula

C7H16

SMILES

CCCCC(C)C

Molecular Weight¹

100.20

CAS

591-76-4

Other Names

• 2-methylhexane
• Isoheptane

• ω : Acentric Factor.
• 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).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (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_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3260		Relay (1.0) Calculated Property
ΔcH°liquid	[-4811.50; -4810.00]	kJ/mol
ΔcH°liquid	-4811.50 ± 1.20	kJ/mol	NIST
ΔcH°liquid	-4810.00 ± 1.00	kJ/mol	NIST
ΔfG°	5.62	kJ/mol	Joback Calculated Property
ΔfH°gas	[-196.20; -195.00]	kJ/mol
ΔfH°gas	-195.00 ± 1.30	kJ/mol	NIST
ΔfH°gas	-196.20	kJ/mol	NIST
ΔfH°liquid	[-231.00; -229.80]	kJ/mol
ΔfH°liquid	-229.80 ± 1.30	kJ/mol	NIST
ΔfH°liquid	-231.00 ± 1.00	kJ/mol	NIST
ΔfusH°	10.36	kJ/mol	Joback Calculated Property
ΔvapH°	[34.80; 34.98]	kJ/mol
ΔvapH°	34.98	kJ/mol	NIST
ΔvapH°	34.90 ± 0.10	kJ/mol	NIST
ΔvapH°	34.80	kJ/mol	NIST
ΔvapH°	34.80	kJ/mol	NIST
IE	9.90	eV	Relay (1.0) Calculated Property
log10WS	-4.52		Relay (1.0) Calculated Property
logPoct/wat	2.833		Crippen Calculated Property
McVol	109.490	ml/mol	McGowan Calculated Property
Pc	[2732.80; 2756.04]	kPa
Pc	2740.00 ± 20.00	kPa	NIST
Pc	2750.00 ± 25.00	kPa	NIST
Pc	2732.80 ± 40.53	kPa	NIST
Pc	2756.04 ± 50.66	kPa	NIST
ρc	[238.48; 238.48]	kg/m3
ρc	238.48 ± 2.00	kg/m3	NIST
ρc	238.48 ± 5.01	kg/m3	NIST
Inp	[654.00; 676.00]
Inp	666.90		NIST
Inp	667.30		NIST
Inp	667.00		NIST
Inp	665.00		NIST
Inp	667.00		NIST
Inp	667.80		NIST
Inp	664.70		NIST
Inp	666.00		NIST
Inp	667.80		NIST
Inp	667.80		NIST
Inp	667.80		NIST
Inp	667.80		NIST
Inp	667.70		NIST
Inp	665.00		NIST
Inp	667.60		NIST
Inp	667.70		NIST
Inp	667.60		NIST
Inp	668.10		NIST
Inp	666.60		NIST
Inp	666.90		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	666.10		NIST
Inp	666.40		NIST
Inp	667.10		NIST
Inp	667.40		NIST
Inp	667.50		NIST
Inp	667.60		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.80		NIST
Inp	667.80		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	668.00		NIST
Inp	667.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	663.00		NIST
Inp	666.60		NIST
Inp	667.10		NIST
Inp	666.60		NIST
Inp	666.20		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	667.00		NIST
Inp	669.00		NIST
Inp	667.80		NIST
Inp	667.80		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	669.01		NIST
Inp	669.50		NIST
Inp	669.95		NIST
Inp	668.35		NIST
Inp	668.68		NIST
Inp	665.00		NIST
Inp	665.00		NIST
Inp	665.00		NIST
Inp	665.00		NIST
Inp	666.00		NIST
Inp	666.90		NIST
Inp	668.00		NIST
Inp	668.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	670.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	666.00		NIST
Inp	666.50		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	668.00		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	668.00		NIST
Inp	667.00		NIST
Inp	659.00		NIST
Inp	659.00		NIST
Inp	Outlier 658.00		NIST
Inp	667.60		NIST
Inp	671.00		NIST
Inp	664.80		NIST
Inp	Outlier 656.80		NIST
Inp	Outlier 657.59		NIST
Inp	663.60		NIST
Inp	662.90		NIST
Inp	Outlier 656.90		NIST
Inp	659.60		NIST
Inp	660.46		NIST
Inp	660.54		NIST
Inp	667.00		NIST
Inp	661.02		NIST
Inp	661.15		NIST
Inp	661.00		NIST
Inp	667.40		NIST
Inp	667.70		NIST
Inp	667.40		NIST
Inp	659.00		NIST
Inp	658.98		NIST
Inp	663.00		NIST
Inp	667.00		NIST
Inp	664.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	668.00		NIST
Inp	667.00		NIST
Inp	Outlier 657.00		NIST
Inp	667.00		NIST
Inp	Outlier 654.00		NIST
Inp	668.00		NIST
Inp	662.50		NIST
Inp	662.00		NIST
Inp	662.00		NIST
Inp	664.00		NIST
Inp	663.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	669.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	Outlier 658.18		NIST
Inp	663.00		NIST
Inp	666.00		NIST
Inp	666.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	662.00		NIST
Inp	662.00		NIST
Inp	667.00		NIST
Inp	Outlier 658.00		NIST
Inp	659.00		NIST
Inp	667.00		NIST
Inp	Outlier 676.00		NIST
Inp	Outlier 674.00		NIST
Inp	Outlier 676.00		NIST
Inp	Outlier 674.00		NIST
Inp	666.90		NIST
Inp	667.80		NIST
Inp	667.70		NIST
Inp	668.00		NIST
Inp	666.10		NIST
Inp	667.60		NIST
Inp	667.00		NIST
Inp	663.00		NIST
Inp	666.00		NIST
Inp	669.00		NIST
Inp	668.68		NIST
Inp	664.80		NIST
Inp	Outlier 656.90		NIST
Inp	661.02		NIST
Inp	667.40		NIST
Inp	658.98		NIST
Inp	659.00		NIST
Inp	Outlier 658.18		NIST
Inp	Outlier 658.00		NIST
Inp	Outlier 676.00		NIST
I	[650.00; 650.00]
I	650.00		NIST
I	650.00		NIST
S°gas	419.99	J/mol×K	NIST
S°liquid	[314.60; 323.34]	J/mol×K
S°liquid	323.34	J/mol×K	NIST
S°liquid	315.10	J/mol×K	NIST
S°liquid	314.60	J/mol×K	NIST
Tboil	[360.85; 364.90]	K
Tboil	363.20	K	NIST
Tboil	363.20	K	NIST
Tboil	Outlier 362.00 ± 5.00	K	NIST
Tboil	Outlier 364.90 ± 3.00	K	NIST
Tboil	364.00 ± 2.00	K	NIST
Tboil	363.20 ± 0.15	K	NIST
Tboil	363.70 ± 3.00	K	NIST
Tboil	364.15 ± 2.00	K	NIST
Tboil	363.25 ± 0.10	K	NIST
Tboil	363.15 ± 0.30	K	NIST
Tboil	363.45 ± 0.30	K	NIST
Tboil	362.85 ± 0.50	K	NIST
Tboil	363.25 ± 0.30	K	NIST
Tboil	363.20 ± 0.15	K	NIST
Tboil	363.20 ± 0.50	K	NIST
Tboil	363.30 ± 0.30	K	NIST
Tboil	363.20 ± 0.07	K	NIST
Tboil	363.25 ± 0.30	K	NIST
Tboil	363.20 ± 0.07	K	NIST
Tboil	363.18 ± 0.15	K	NIST
Tboil	363.18 ± 0.10	K	NIST
Tboil	363.30 ± 0.30	K	NIST
Tboil	363.15 ± 0.50	K	NIST
Tboil	363.15 ± 0.50	K	NIST
Tboil	363.20 ± 0.06	K	NIST
Tboil	363.30 ± 0.30	K	NIST
Tboil	363.20 ± 0.50	K	NIST
Tboil	363.23 ± 0.30	K	NIST
Tboil	363.35 ± 0.50	K	NIST
Tboil	363.25 ± 0.50	K	NIST
Tboil	362.85 ± 0.60	K	NIST
Tboil	363.25 ± 0.30	K	NIST
Tboil	363.25 ± 0.50	K	NIST
Tboil	362.90 ± 0.60	K	NIST
Tboil	363.25 ± 0.20	K	NIST
Tboil	363.45 ± 0.30	K	NIST
Tboil	363.38 ± 0.50	K	NIST
Tboil	363.25 ± 0.50	K	NIST
Tboil	Outlier 360.85 ± 0.50	K	NIST
Tboil	362.85 ± 0.30	K	NIST
Tboil	362.82 ± 0.10	K	NIST
Tboil	362.90 ± 0.30	K	NIST
Tboil	363.15 ± 0.50	K	NIST
Tboil	363.15 ± 0.50	K	NIST
Tboil	364.00 ± 2.00	K	NIST
Tboil	364.00 ± 2.00	K	NIST
Tboil	363.35 ± 1.00	K	NIST
Tboil	363.15 ± 2.00	K	NIST
Tc	[530.30; 531.05]	K
Tc	530.40 ± 0.20	K	NIST
Tc	530.43 ± 0.20	K	NIST
Tc	530.30	K	NIST
Tc	530.30 ± 0.40	K	NIST
Tc	530.33 ± 0.20	K	NIST
Tc	Outlier 531.05 ± 0.50	K	NIST
Tfus	[152.85; 154.95]	K
Tfus	154.87 ± 0.02	K	NIST
Tfus	154.86 ± 0.04	K	NIST
Tfus	154.85 ± 0.02	K	NIST
Tfus	154.86 ± 0.03	K	NIST
Tfus	154.88 ± 0.02	K	NIST
Tfus	154.39 ± 0.05	K	NIST
Tfus	154.87 ± 0.03	K	NIST
Tfus	154.95 ± 0.50	K	NIST
Tfus	154.91 ± 0.30	K	NIST
Tfus	154.89 ± 0.20	K	NIST
Tfus	154.89 ± 0.20	K	NIST
Tfus	154.82 ± 0.03	K	NIST
Tfus	154.83 ± 0.02	K	NIST
Tfus	154.88 ± 0.02	K	NIST
Tfus	154.65 ± 0.30	K	NIST
Tfus	154.65 ± 0.50	K	NIST
Tfus	154.95 ± 0.50	K	NIST
Tfus	Outlier 152.85 ± 0.30	K	NIST
Tfus	154.95 ± 0.50	K	NIST
Tfus	154.25 ± 0.20	K	NIST
Tfus	154.05 ± 0.50	K	NIST
Tfus	154.05 ± 0.50	K	NIST
Tfus	154.05 ± 0.50	K	NIST
Ttriple	[154.00; 154.90]	K
Ttriple	154.86 ± 0.09	K	NIST
Ttriple	154.90 ± 0.06	K	NIST
Ttriple	154.86 ± 0.04	K	NIST
Ttriple	154.90 ± 0.02	K	NIST
Ttriple	154.00 ± 0.20	K	NIST
Ttriple	154.00 ± 0.20	K	NIST
Vc	0.421	m3/kmol	NIST

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[194.02; 260.72]	J/mol×K	[359.12; 526.54]
Cp,gas	194.02	J/mol×K	359.12	Joback Calculated Property
Cp,gas	206.19	J/mol×K	387.02	Joback Calculated Property
Cp,gas	217.92	J/mol×K	414.93	Joback Calculated Property
Cp,gas	229.23	J/mol×K	442.83	Joback Calculated Property
Cp,gas	240.13	J/mol×K	470.73	Joback Calculated Property
Cp,gas	250.62	J/mol×K	498.63	Joback Calculated Property
Cp,gas	260.72	J/mol×K	526.54	Joback Calculated Property
Cp,liquid	[219.20; 222.92]	J/mol×K	[292.40; 298.15]
Cp,liquid	219.20	J/mol×K	292.40	NIST
Cp,liquid	222.92	J/mol×K	298.15	NIST
Csat	[180.40; 223.60]	J/mol×K	[160.00; 300.00]
Csat	180.40	J/mol×K	160.00	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
Csat	182.30	J/mol×K	170.00	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
Csat	184.40	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
Csat	186.70	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
Csat	189.10	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
Csat	191.80	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
Csat	194.60	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
Csat	197.60	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
Csat	200.80	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
Csat	204.10	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
Csat	207.70	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
Csat	211.40	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
Csat	212.60	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
Csat	215.30	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
Csat	219.40	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
Csat	222.80	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
Csat	223.60	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
η	[0.0002348; 0.0099972]	Pa×s	[153.65; 359.12]
η	0.0099972	Pa×s	153.65	Joback Calculated Property
η	0.0030264	Pa×s	187.90	Joback Calculated Property
η	0.0013243	Pa×s	222.14	Joback Calculated Property
η	0.0007226	Pa×s	256.38	Joback Calculated Property
η	0.0004548	Pa×s	290.63	Joback Calculated Property
η	0.0003156	Pa×s	324.88	Joback Calculated Property
η	0.0002348	Pa×s	359.12	Joback Calculated Property
ΔfusH	[8.87; 9.18]	kJ/mol	[154.00; 154.90]
ΔfusH	8.87	kJ/mol	154.00	NIST
ΔfusH	8.87	kJ/mol	154.00	NIST
ΔfusH	9.18	kJ/mol	154.90	NIST
ΔfusH	9.18	kJ/mol	154.90	NIST
ΔfusH	9.18	kJ/mol	154.90	NIST
ΔvapH	[30.62; 34.80]	kJ/mol	[313.00; 363.20]
ΔvapH	33.90 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	34.80	kJ/mol	327.50	NIST
ΔvapH	34.60	kJ/mol	330.50	NIST
ΔvapH	32.70 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	31.30 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	30.62	kJ/mol	363.20	NIST
ΔfusS	[57.60; 59.29]	J/mol×K	[154.00; 154.90]
ΔfusS	57.60	J/mol×K	154.00	NIST
ΔfusS	57.60	J/mol×K	154.00	NIST
ΔfusS	59.29	J/mol×K	154.90	NIST
λ	[0.10; 0.12]	W/m×K	[256.24; 338.11]
λ	0.12	W/m×K	256.24	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	256.67	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	257.02	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	275.56	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	276.00	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	276.39	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	296.46	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	296.93	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	297.40	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	317.40	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	317.92	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	318.35	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	337.10	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	337.65	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	338.11	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[263.60; 388.11]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.42374e+01
Coefficient B			-3.08596e+03
Coefficient C			-4.23820e+01
Temperature range, min.			263.60
Temperature range, max.			388.11
Pvap	1.33	kPa	263.60	Calculated Property
Pvap	3.03	kPa	277.43	Calculated Property
Pvap	6.29	kPa	291.27	Calculated Property
Pvap	12.08	kPa	305.10	Calculated Property
Pvap	21.73	kPa	318.94	Calculated Property
Pvap	36.98	kPa	332.77	Calculated Property
Pvap	59.96	kPa	346.61	Calculated Property
Pvap	93.22	kPa	360.44	Calculated Property
Pvap	139.68	kPa	374.28	Calculated Property
Pvap	202.64	kPa	388.11	Calculated Property
Pvap	[1.91e-06; 2759.35]	kPa	[154.90; 530.37]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			9.26032e+01
Coefficient B			-7.22527e+03
Coefficient C			-1.17722e+01
Coefficient D			9.94213e-06
Temperature range, min.			154.90
Temperature range, max.			530.37
Pvap	1.91e-06	kPa	154.90	Calculated Property
Pvap	2.65e-03	kPa	196.62	Calculated Property
Pvap	0.20	kPa	238.34	Calculated Property
Pvap	3.48	kPa	280.06	Calculated Property
Pvap	24.71	kPa	321.78	Calculated Property
Pvap	102.85	kPa	363.49	Calculated Property
Pvap	304.75	kPa	405.21	Calculated Property
Pvap	723.26	kPa	446.93	Calculated Property
Pvap	1482.46	kPa	488.65	Calculated Property
Pvap	2759.35	kPa	530.37	Calculated Property

Similar Compounds

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

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
• 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

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
These property values are available through the Cheméo API. A free account gives you an access key.