Hexane, 3-methyl- (CAS 589-34-4)

InChI

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

InChI Key

VLJXXKKOSFGPHI-UHFFFAOYSA-N

Formula

C7H16

SMILES

CCCC(C)CC

Molecular Weight¹

100.20

CAS

589-34-4

Other Names

2-Ethylpentane
3-methylhexane

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_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).
n₀ : Refractive Index.
ρ_c : Critical density (kg/m³).
ρ_l : Liquid Density (kg/m³).
I_np : Non-polar retention indices.
I : Polar retention indices.
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 : Liquid thermal conductivity (W/m×K).
T_fus : Normal melting (fusion) point (K).
V_c : Critical Volume (m³/kmol).
Z_c : Critical Compressibility.
Z_ra : Rackett Parameter.
¹: Molecular weight from the IUPAC atomic weights tables.

Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Please note that you need to enable javascript to get access to all the properties. Here is how to do it for Internet Explorer and for Firefox.

Physical Properties

Property	Value	Unit	Source
ω	0.3230		KDB
AP	343.650	K	KDB
Δ_cH°_liquid	[-4813.90; -4813.00]	kJ/mol
Δ_cH°_liquid	-4813.90 ± 1.20	kJ/mol	NIST
Δ_cH°_liquid	-4813.00 ± 1.00	kJ/mol	NIST
μ	0.00	debye	KDB
Δ_fG°	4.60	kJ/mol	KDB
Δ_c,grossH	4813.90	kJ/mol	KDB
Δ_c,netH	4461.776	kJ/mol	KDB
Δ_fH°_gas	[-192.90; -192.30]	kJ/mol
Δ_fH°_gas	-192.40	kJ/mol	KDB
Δ_fH°_gas	-192.30 ± 1.30	kJ/mol	NIST
Δ_fH°_gas	-192.90	kJ/mol	NIST
Δ_fH°_liquid	[-228.00; -227.40]	kJ/mol
Δ_fH°_liquid	-227.40 ± 1.30	kJ/mol	NIST
Δ_fH°_liquid	-228.00 ± 1.00	kJ/mol	NIST
Δ_fusH°	10.36	kJ/mol	Joback Calculated Property
Δ_vapH°	[35.10; 35.16]	kJ/mol
Δ_vapH°	35.16	kJ/mol	NIST
Δ_vapH°	35.10 ± 0.10	kJ/mol	NIST
Δ_vapH°	35.10	kJ/mol	NIST
IE	9.87	eV	Relay (1.0) Calculated Property
log₁₀WS	-4.44		Relay (1.0) Calculated Property
logP_oct/wat	2.833		Crippen Calculated Property
McVol	109.490	ml/mol	McGowan Calculated Property
P_c	[2810.00; 2850.00]	kPa
P_c	2810.00	kPa	KDB
P_c	2810.00 ± 40.00	kPa	NIST
P_c	2813.50 ± 40.53	kPa	NIST
P_c	2850.00 ± 5133.40	kPa	NIST
ρ_c	[247.50; 248.50]	kg/m³
ρ_c	247.50 ± 4.01	kg/m³	NIST
ρ_c	248.50 ± 5.01	kg/m³	NIST
I_np	[664.00; 689.20]
I_np	675.90		NIST
I_np	676.60		NIST
I_np	676.00		NIST
I_np	674.00		NIST
I_np	677.00		NIST
I_np	678.20		NIST
I_np	Outlier 689.20		NIST
I_np	675.50		NIST
I_np	679.30		NIST
I_np	Outlier 682.30		NIST
I_np	675.00		NIST
I_np	677.00		NIST
I_np	678.00		NIST
I_np	678.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	675.80		NIST
I_np	676.80		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	675.70		NIST
I_np	676.10		NIST
I_np	676.40		NIST
I_np	676.90		NIST
I_np	674.00		NIST
I_np	675.00		NIST
I_np	675.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.80		NIST
I_np	676.80		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	672.00		NIST
I_np	675.50		NIST
I_np	676.10		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	676.00		NIST
I_np	678.50		NIST
I_np	671.10		NIST
I_np	673.20		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	678.51		NIST
I_np	679.09		NIST
I_np	679.75		NIST
I_np	677.32		NIST
I_np	677.95		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	674.00		NIST
I_np	674.00		NIST
I_np	675.00		NIST
I_np	675.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.40		NIST
I_np	677.00		NIST
I_np	678.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	678.00		NIST
I_np	675.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	Outlier 683.00		NIST
I_np	678.00		NIST
I_np	675.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	679.00		NIST
I_np	Outlier 667.00		NIST
I_np	669.00		NIST
I_np	672.00		NIST
I_np	675.80		NIST
I_np	678.00		NIST
I_np	671.00		NIST
I_np	673.90		NIST
I_np	Outlier 666.92		NIST
I_np	Outlier 667.66		NIST
I_np	672.70		NIST
I_np	672.20		NIST
I_np	670.16		NIST
I_np	670.26		NIST
I_np	676.00		NIST
I_np	670.56		NIST
I_np	670.60		NIST
I_np	671.00		NIST
I_np	676.90		NIST
I_np	676.50		NIST
I_np	675.80		NIST
I_np	669.00		NIST
I_np	671.00		NIST
I_np	669.20		NIST
I_np	672.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	678.00		NIST
I_np	677.00		NIST
I_np	669.00		NIST
I_np	676.00		NIST
I_np	Outlier 664.00		NIST
I_np	676.00		NIST
I_np	672.00		NIST
I_np	674.00		NIST
I_np	672.20		NIST
I_np	670.00		NIST
I_np	674.00		NIST
I_np	677.00		NIST
I_np	672.00		NIST
I_np	676.00		NIST
I_np	675.00		NIST
I_np	673.00		NIST
I_np	678.00		NIST
I_np	677.00		NIST
I_np	677.00		NIST
I_np	676.00		NIST
I_np	671.00		NIST
I_np	Outlier 668.04		NIST
I_np	672.00		NIST
I_np	676.00		NIST
I_np	675.00		NIST
I_np	676.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	676.00		NIST
I_np	677.00		NIST
I_np	Outlier 665.00		NIST
I_np	672.00		NIST
I_np	674.00		NIST
I_np	672.00		NIST
I_np	673.00		NIST
I_np	675.00		NIST
I_np	Outlier 683.00		NIST
I_np	Outlier 685.00		NIST
I_np	Outlier 683.00		NIST
I_np	Outlier 685.00		NIST
I_np	671.00		NIST
I_np	672.20		NIST
I_np	670.60		NIST
I_np	669.00		NIST
I_np	675.80		NIST
I	700.00		NIST
S°_liquid	309.60	J/mol×K	NIST
T_boil	364.99	K	KDB
T_c	[535.19; 535.55]	K
T_c	535.20	K	KDB
T_c	535.20 ± 0.40	K	NIST
T_c	535.20	K	NIST
T_c	535.19 ± 0.40	K	NIST
T_c	535.55 ± 0.50	K	NIST
T_fus	[153.70; 153.75]	K
T_fus	153.70	K	KDB
T_fus	153.75 ± 0.50	K	NIST
V_c	[0.404; 0.404]	m³/kmol
V_c	0.404	m³/kmol	KDB
V_c	0.404	m³/kmol	NIST
Z_c	0.2551140		KDB
Z_ra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[194.02; 260.72]	J/mol×K	[359.12; 526.54]

C_p,gas	194.02	J/mol×K	359.12	Joback Calculated Property
C_p,gas	206.19	J/mol×K	387.02	Joback Calculated Property
C_p,gas	217.92	J/mol×K	414.93	Joback Calculated Property
C_p,gas	229.23	J/mol×K	442.83	Joback Calculated Property
C_p,gas	240.13	J/mol×K	470.73	Joback Calculated Property
C_p,gas	250.62	J/mol×K	498.63	Joback Calculated Property
C_p,gas	260.72	J/mol×K	526.54	Joback Calculated Property
C_p,liquid	[165.90; 219.50]	J/mol×K	[90.00; 298.15]

C_p,liquid	165.90	J/mol×K	90.00	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
C_p,liquid	166.80	J/mol×K	100.00	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
C_p,liquid	167.90	J/mol×K	110.00	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
C_p,liquid	169.20	J/mol×K	120.00	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
C_p,liquid	170.60	J/mol×K	130.00	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
C_p,liquid	172.20	J/mol×K	140.00	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
C_p,liquid	174.00	J/mol×K	150.00	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
C_p,liquid	175.90	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
C_p,liquid	178.00	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
C_p,liquid	180.20	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
C_p,liquid	182.70	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
C_p,liquid	185.30	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
C_p,liquid	188.00	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
C_p,liquid	190.90	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
C_p,liquid	194.00	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
C_p,liquid	197.30	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
C_p,liquid	200.70	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
C_p,liquid	204.30	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
C_p,liquid	208.10	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
C_p,liquid	209.30	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
C_p,liquid	212.00	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
C_p,liquid	216.70	J/mol×K	289.20	NIST
C_p,liquid	214.20	J/mol×K	289.20	NIST
C_p,liquid	216.10	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
C_p,liquid	219.50	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
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
Δ_vapH	[30.79; 35.10]	kJ/mol	[313.00; 365.00]

Δ_vapH	34.20 ± 0.10	kJ/mol	313.00	NIST
Δ_vapH	35.10	kJ/mol	327.50	NIST
Δ_vapH	34.90	kJ/mol	329.50	NIST
Δ_vapH	32.90 ± 0.10	kJ/mol	333.00	NIST
Δ_vapH	31.70 ± 0.10	kJ/mol	353.00	NIST
Δ_vapH	30.79	kJ/mol	365.00	KDB
Δ_vapH	30.89	kJ/mol	365.00	NIST
n₀	1.38609		298.15	KDB
ρ_l	687.00	kg/m³	293.00	KDB
γ	0.02	N/m	298.20	KDB
λ	[0.10; 0.12]	W/m×K	[256.62; 344.30]

λ	0.12	W/m×K	256.62	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	257.00	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	257.38	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	269.72	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	270.11	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	270.44	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.12	W/m×K	284.90	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	285.32	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	285.66	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	296.55	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	296.95	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	297.35	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	311.54	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	311.97	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.11	W/m×K	312.34	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	321.52	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	321.98	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	322.34	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	322.34	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	332.24	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	332.69	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	333.09	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	343.42	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	343.89	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	344.28	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λ	0.10	W/m×K	344.30	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.67]	kPa	[264.32; 390.12]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.43045e+01
Coefficient B			-3.15633e+03
Coefficient C			-3.91420e+01
Temperature range, min.			264.32
Temperature range, max.			390.12

P_vap	1.33	kPa	264.32	Calculated Property
P_vap	3.02	kPa	278.30	Calculated Property
P_vap	6.27	kPa	292.28	Calculated Property
P_vap	12.04	kPa	306.25	Calculated Property
P_vap	21.66	kPa	320.23	Calculated Property
P_vap	36.87	kPa	334.21	Calculated Property
P_vap	59.82	kPa	348.19	Calculated Property
P_vap	93.06	kPa	362.16	Calculated Property
P_vap	139.57	kPa	376.14	Calculated Property
P_vap	202.67	kPa	390.12	Calculated Property
P_vap	[1.78e-06; 2795.09]	kPa	[153.75; 535.25]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			7.98000e+01
Coefficient B			-6.76864e+03
Coefficient C			-9.76975e+00
Coefficient D			7.54692e-06
Temperature range, min.			153.75
Temperature range, max.			535.25

P_vap	1.78e-06	kPa	153.75	Calculated Property
P_vap	2.50e-03	kPa	196.14	Calculated Property
P_vap	0.20	kPa	238.53	Calculated Property
P_vap	3.38	kPa	280.92	Calculated Property
P_vap	24.47	kPa	323.31	Calculated Property
P_vap	103.66	kPa	365.69	Calculated Property
P_vap	311.00	kPa	408.08	Calculated Property
P_vap	742.27	kPa	450.47	Calculated Property
P_vap	1518.05	kPa	492.86	Calculated Property
P_vap	2795.09	kPa	535.25	Calculated Property

Similar Compounds

Find more compounds similar to Hexane, 3-methyl-.

Sources

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.

Chemical Properties of Hexane, 3-methyl- (CAS 589-34-4)

Physical Properties

Temperature Dependent Properties

Correlations

Similar Compounds

Sources