Chemical Properties of Pentane, 3-methyl- (CAS 96-14-0)

InChI

InChI=1S/C6H14/c1-4-6(3)5-2/h6H,4-5H2,1-3H3

InChI Key

PFEOZHBOMNWTJB-UHFFFAOYSA-N

Formula

C6H14

SMILES

CCC(C)CC

Molecular Weight¹

86.18

CAS

96-14-0

Other Names

• (C2H5)2CHCH3
• 3-Methylpentane
• UN 1208
• UN 2462

• 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).
• C_p,solid : Solid 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_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).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point 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_p : Polar retention indices.
• S°_gas : Molar entropy at standard conditions (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).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.2700; 0.2750]
ω	0.2750		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2750		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2730		ChemSep v8.3 pure component data Compiled value
ω	0.2700		KDB
AP	342.450	K	KDB
ΔcH°liquid	-4159.90 ± 0.88	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[-3.42; -2.14]	kJ/mol
ΔfG°	-3.42	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-2.14	kJ/mol	KDB
Δc,grossH	4159.94	kJ/mol	KDB
Δc,netH	3851.832	kJ/mol	KDB
ΔfH°gas	[-172.00; -171.60]	kJ/mol
ΔfH°gas	-172.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-171.70	kJ/mol	KDB
ΔfH°gas	-171.60 ± 0.96	kJ/mol	NIST
ΔfH°liquid	-202.00 ± 0.96	kJ/mol	NIST
ΔfusH°	7.77	kJ/mol	Joback Calculated Property
ΔvapH°	[30.19; 30.47]	kJ/mol
ΔvapH°	30.47	kJ/mol	NIST
ΔvapH°	30.30 ± 0.10	kJ/mol	NIST
ΔvapH°	30.30	kJ/mol	NIST
ΔvapH°	30.19 ± 0.03	kJ/mol	NIST
ΔvapH°	30.30 ± 0.10	kJ/mol	NIST
ΔvapH°	30.27	kJ/mol	NIST
IE	[9.82; 10.08]	eV
IE	10.04	eV	NIST
IE	9.82	eV	NIST
IE	10.08	eV	NIST
log10WS	[-3.68; -3.68]
log10WS	-3.68		Aq. Solubility Prediction
log10WS	-3.68		Estimated Solubility
logPoct/wat	2.442		Crippen Calculated Property
McVol	95.400	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3035.00; 3128.00]	kPa
Pc	3120.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Pc	3119.80	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3124.01	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3120.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3120.00	kPa	KDB
Pc	3120.00 ± 20.00	kPa	NIST
Pc	3124.42 ± 10.00	kPa	NIST
Pc	3124.00 ± 3.00	kPa	NIST
Pc	3128.00 ± 2.00	kPa	NIST
Pc	3116.00 ± 30.40	kPa	NIST
Pc	Outlier 3035.00 ± 20.26	kPa	NIST
Ptriple	4.14e-10	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[234.40; 235.26]	kg/m3
ρc	234.40 ± 1.72	kg/m3	NIST
ρc	234.40 ± 5.17	kg/m3	NIST
ρc	235.26 ± 1.72	kg/m3	NIST
Inp	[570.00; 595.00]
Inp	582.80		NIST
Inp	583.70		NIST
Inp	585.00		NIST
Inp	581.00		NIST
Inp	581.00		NIST
Inp	586.20		NIST
Inp	583.80		NIST
Inp	588.40		NIST
Inp	590.10		NIST
Inp	583.00		NIST
Inp	584.40		NIST
Inp	584.50		NIST
Inp	584.60		NIST
Inp	584.50		NIST
Inp	584.20		NIST
Inp	583.00		NIST
Inp	581.00		NIST
Inp	Outlier 592.00		NIST
Inp	590.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	577.00		NIST
Inp	578.00		NIST
Inp	579.00		NIST
Inp	583.80		NIST
Inp	584.90		NIST
Inp	584.60		NIST
Inp	583.10		NIST
Inp	583.80		NIST
Inp	584.10		NIST
Inp	584.80		NIST
Inp	584.40		NIST
Inp	584.50		NIST
Inp	584.00		NIST
Inp	578.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	583.00		NIST
Inp	577.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	586.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	584.60		NIST
Inp	585.00		NIST
Inp	584.00		NIST
Inp	585.30		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	584.00		NIST
Inp	585.00		NIST
Inp	586.30		NIST
Inp	586.74		NIST
Inp	587.87		NIST
Inp	585.66		NIST
Inp	585.89		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	583.01		NIST
Inp	581.00		NIST
Inp	581.00		NIST
Inp	582.00		NIST
Inp	582.00		NIST
Inp	583.00		NIST
Inp	584.50		NIST
Inp	585.00		NIST
Inp	586.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	583.00		NIST
Inp	584.00		NIST
Inp	585.00		NIST
Inp	584.00		NIST
Inp	583.00		NIST
Inp	584.00		NIST
Inp	585.00		NIST
Inp	586.00		NIST
Inp	582.50		NIST
Inp	584.50		NIST
Inp	583.00		NIST
Inp	584.00		NIST
Inp	585.00		NIST
Inp	584.00		NIST
Inp	586.00		NIST
Inp	583.00		NIST
Inp	583.00		NIST
Inp	584.00		NIST
Inp	585.00		NIST
Inp	584.00		NIST
Inp	586.00		NIST
Inp	585.00		NIST
Inp	583.00		NIST
Inp	578.00		NIST
Inp	581.00		NIST
Inp	585.50		NIST
Inp	584.00		NIST
Inp	580.00		NIST
Inp	579.00		NIST
Inp	577.00		NIST
Inp	589.49		NIST
Inp	590.18		NIST
Inp	579.00		NIST
Inp	578.60		NIST
Inp	577.12		NIST
Inp	577.14		NIST
Inp	581.00		NIST
Inp	577.22		NIST
Inp	577.32		NIST
Inp	577.00		NIST
Inp	583.70		NIST
Inp	583.40		NIST
Inp	583.10		NIST
Inp	578.00		NIST
Inp	581.00		NIST
Inp	576.00		NIST
Inp	579.00		NIST
Inp	583.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	586.00		NIST
Inp	585.00		NIST
Inp	Outlier 591.00		NIST
Inp	Outlier 595.00		NIST
Inp	578.00		NIST
Inp	583.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	582.00		NIST
Inp	584.00		NIST
Inp	578.00		NIST
Inp	578.00		NIST
Inp	576.00		NIST
Inp	578.00		NIST
Inp	580.80		NIST
Inp	577.00		NIST
Inp	Outlier 595.00		NIST
Inp	579.00		NIST
Inp	577.56		NIST
Inp	583.00		NIST
Inp	578.00		NIST
Inp	580.00		NIST
Inp	575.80		NIST
Inp	576.00		NIST
Inp	586.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	577.00		NIST
Inp	577.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	579.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	585.00		NIST
Inp	581.00		NIST
Inp	Outlier 570.00		NIST
Inp	Outlier 573.00		NIST
Inp	576.00		NIST
Inp	576.00		NIST
Inp	581.00		NIST
Inp	581.00		NIST
Inp	Outlier 571.00		NIST
Inp	576.00		NIST
Inp	580.00		NIST
Inp	580.00		NIST
Inp	584.00		NIST
Inp	588.00		NIST
Inp	584.00		NIST
Inp	588.00		NIST
Inp	584.00		NIST
Inp	581.00		NIST
Inp	583.00		NIST
Inp	585.00		NIST
Inp	576.00		NIST
Inp	577.00		NIST
Inp	584.00		NIST
Inp	580.00		NIST
Inp	588.00		NIST
Inp	582.00		NIST
Inp	578.00		NIST
Inp	577.56		NIST
Ip	[577.00; 581.00]
Ip	577.00		NIST
Ip	581.00		NIST
S°gas	382.88 ± 0.67	J/mol×K	NIST
S°liquid	292.50	J/mol×K	NIST
Tboil	[333.28; 337.15]	K
Tboil	336.30	K	Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa
Tboil	336.40	K	ChemSep v8.3 pure component data Compiled value
Tboil	336.42	K	KDB
Tboil	336.50	K	NIST
Tboil	336.40	K	NIST
Tboil	337.00 ± 3.00	K	NIST
Tboil	337.00 ± 2.00	K	NIST
Tboil	335.90 ± 1.50	K	NIST
Tboil	336.43 ± 0.20	K	NIST
Tboil	336.00 ± 2.00	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.45 ± 0.10	K	NIST
Tboil	336.35 ± 0.30	K	NIST
Tboil	Outlier 335.15 ± 3.00	K	NIST
Tboil	Outlier 334.90 ± 0.50	K	NIST
Tboil	336.15 ± 1.00	K	NIST
Tboil	336.70 ± 0.30	K	NIST
Tboil	336.50 ± 0.30	K	NIST
Tboil	336.30 ± 0.30	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.50 ± 0.50	K	NIST
Tboil	336.30 ± 0.15	K	NIST
Tboil	336.41 ± 0.05	K	NIST
Tboil	336.43 ± 0.02	K	NIST
Tboil	336.10 ± 0.10	K	NIST
Tboil	Outlier 333.28 ± 0.07	K	NIST
Tboil	336.30 ± 0.30	K	NIST
Tboil	336.15 ± 0.60	K	NIST
Tboil	336.43 ± 0.05	K	NIST
Tboil	336.50 ± 0.10	K	NIST
Tboil	336.43 ± 0.02	K	NIST
Tboil	336.45 ± 0.50	K	NIST
Tboil	336.50 ± 0.50	K	NIST
Tboil	336.44 ± 0.10	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.38 ± 0.20	K	NIST
Tboil	336.55 ± 0.50	K	NIST
Tboil	336.40 ± 0.30	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.45 ± 0.30	K	NIST
Tboil	336.41 ± 0.20	K	NIST
Tboil	336.45 ± 0.20	K	NIST
Tboil	336.35 ± 0.10	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.36 ± 0.15	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.33 ± 0.15	K	NIST
Tboil	336.40 ± 0.70	K	NIST
Tboil	336.45 ± 0.50	K	NIST
Tboil	335.85 ± 0.60	K	NIST
Tboil	335.85 ± 0.50	K	NIST
Tboil	335.95 ± 0.60	K	NIST
Tboil	336.45 ± 0.50	K	NIST
Tboil	336.35 ± 0.50	K	NIST
Tboil	336.35 ± 0.40	K	NIST
Tboil	336.35 ± 0.40	K	NIST
Tboil	336.35 ± 0.30	K	NIST
Tboil	337.15 ± 1.50	K	NIST
Tboil	337.00 ± 3.00	K	NIST
Tc	[498.10; 504.70]	K
Tc	504.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc	504.60	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	504.43	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	504.40	K	ChemSep v8.3 pure component data Compiled value
Tc	504.60	K	KDB
Tc	504.60 ± 0.20	K	NIST
Tc	504.40	K	NIST
Tc	504.60 ± 0.20	K	NIST
Tc	504.59 ± 0.20	K	NIST
Tc	504.62 ± 0.15	K	NIST
Tc	504.40 ± 0.30	K	NIST
Tc	504.70 ± 0.20	K	NIST
Tc	Outlier 498.10 ± 0.20	K	NIST
Tfus	[110.20; 157.10]	K
Tfus	155.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	110.25	K	ChemSep v8.3 pure component data Compiled value
Tfus	110.20	K	KDB
Tfus	157.10	K	Aq. Solubility Prediction
Tfus	155.15 ± 2.00	K	NIST
Tfus	155.15 ± 1.00	K	NIST
Ttriple	[110.25; 110.25]	K
Ttriple	110.25	K	ChemSep v8.3 pure component data Compiled value
Ttriple	110.25	K	KDB
Ttriple	110.25 ± 0.01	K	NIST
Ttriple	110.25 ± 0.01	K	NIST
UQi	3.85		ChemSep v8.3 pure component data Compiled value
URi	4.50		ChemSep v8.3 pure component data Compiled value
Vc	[0.367; 0.368]	m3/kmol
Vc	0.368	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Vc	0.368	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.367	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.368	m3/kmol	KDB
Vc	0.368	m3/kmol	NIST
VCOSTALD	0.36	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2730000; 0.2740000]
Zc	0.2740000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Zc	0.2730000		ChemSep v8.3 pure component data Compiled value
Zc	0.2736650		KDB
Zra	[0.26; 0.27]
Zra	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[154.31; 207.32]	J/mol×K	[332.10; 471.15]
Cp,gas	154.31	J/mol×K	332.10	NIST
Cp,gas	168.41	J/mol×K	367.55	NIST
Cp,gas	181.71	J/mol×K	402.35	NIST
Cp,gas	194.64	J/mol×K	436.20	NIST
Cp,gas	207.32	J/mol×K	471.15	NIST
Cp,liquid	[146.20; 203.20]	J/mol×K	[120.00; 330.00]
Cp,liquid	146.20	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
Cp,liquid	147.50	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
Cp,liquid	149.00	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
Cp,liquid	150.60	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
Cp,liquid	152.40	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
Cp,liquid	154.20	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
Cp,liquid	156.30	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	158.40	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	160.70	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	163.20	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	165.70	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	168.50	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	171.30	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
Cp,liquid	174.30	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	177.40	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	180.70	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	181.80	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	184.10	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	187.10	J/mol×K	288.19	NIST
Cp,liquid	187.70	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	187.36	J/mol×K	298.10	NIST
Cp,liquid	190.99	J/mol×K	298.15	NIST
Cp,liquid	191.16	J/mol×K	298.15	NIST
Cp,liquid	190.86	J/mol×K	298.15	NIST
Cp,liquid	190.77	J/mol×K	298.15	NIST
Cp,liquid	190.77	J/mol×K	298.15	NIST
Cp,liquid	190.67	J/mol×K	298.15	NIST
Cp,liquid	190.70	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	186.80	J/mol×K	298.95	NIST
Cp,liquid	191.30	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
Cp,liquid	195.20	J/mol×K	310.00	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	199.10	J/mol×K	320.00	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	203.20	J/mol×K	330.00	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,solid	190.83	J/mol×K	298.15	NIST
ΔfusH	[5.31; 5.31]	kJ/mol	[110.30; 110.30]
ΔfusH	5.31	kJ/mol	110.30	NIST
ΔfusH	5.31	kJ/mol	110.30	NIST
ΔvapH	[27.00; 30.50]	kJ/mol	[303.00; 353.00]
ΔvapH	30.00 ± 0.10	kJ/mol	303.00	NIST
ΔvapH	30.00 ± 0.01	kJ/mol	303.10	NIST
ΔvapH	30.20	kJ/mol	312.50	NIST
ΔvapH	29.50 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	30.50	kJ/mol	315.50	NIST
ΔvapH	28.80 ± 0.10	kJ/mol	324.00	NIST
ΔvapH	28.30 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	28.10 ± 0.10	kJ/mol	336.00	NIST
ΔvapH	28.07	kJ/mol	336.40	KDB
ΔvapH	28.06	kJ/mol	336.40	NIST
ΔvapH	29.90	kJ/mol	338.50	NIST
ΔvapH	27.00 ± 0.10	kJ/mol	353.00	NIST
ν	[0.0000004; 0.0000005]	m2/s	[283.15; 313.15]
ν	0.0000005	m2/s	283.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000005	m2/s	283.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000004	m2/s	298.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000004	m2/s	298.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000004	m2/s	313.15	Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
ν	0.0000004	m2/s	313.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
n0	[1.37386; 1.37399]		[298.15; 298.15]
n0	1.37399		298.15	Liquid liquid equilibria of lactam containing binary systems
n0	1.37386		298.15	KDB
ρl	[659.31; 664.23]	kg/m3	[293.00; 298.60]
ρl	664.00	kg/m3	293.00	KDB
ρl	664.23	kg/m3	293.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	662.39	kg/m3	295.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	660.59	kg/m3	297.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	659.94	kg/m3	298.15	Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
ρl	659.74	kg/m3	298.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	660.30	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
ρl	659.94	kg/m3	298.15	Excess Enthalpies of the Ternary Mixtures: Diisopropyl Ether + 3-Methylpentane + (Octane or Decane) at 298.15 K
ρl	659.31	kg/m3	298.60	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
γ	0.02	N/m	298.20	KDB
λliquid	[0.10; 0.12]	W/m×K	[256.68; 329.26]
λliquid	0.12	W/m×K	256.68	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.12	W/m×K	257.00	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.12	W/m×K	257.43	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	276.71	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	277.02	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	277.46	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	296.39	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	296.74	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.11	W/m×K	297.20	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	314.22	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	314.59	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	315.08	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	328.36	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	328.75	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid	0.10	W/m×K	329.26	Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (3)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
273.14	1000.00	0.0004
273.14	5000.00	0.0004
273.14	10000.00	0.0004
273.13	15000.00	0.0004
273.14	20000.00	0.0005
273.14	25000.00	0.0005
273.14	30000.00	0.0005
273.14	35000.00	0.0005
273.14	40000.00	0.0005
283.14	1000.00	0.0003
283.14	5000.00	0.0004
283.14	10000.00	0.0004
283.15	15000.00	0.0004
283.14	20000.00	0.0004
283.14	25000.00	0.0004
283.14	30000.00	0.0004
283.15	35000.00	0.0005
283.15	40000.00	0.0005
293.17	1000.00	0.0003
293.17	5000.00	0.0003
293.17	10000.00	0.0003
293.16	15000.00	0.0004
293.16	20000.00	0.0004
293.16	25000.00	0.0004
293.17	30000.00	0.0004
293.16	35000.00	0.0004
293.16	40000.00	0.0004
303.16	1000.00	0.0003
303.16	5000.00	0.0003
303.16	10000.00	0.0003
303.16	15000.00	0.0003
303.16	20000.00	0.0003
303.16	25000.00	0.0004
303.16	30000.00	0.0004
303.15	35000.00	0.0004
303.16	40000.00	0.0004
313.16	1000.00	0.0003
313.16	5000.00	0.0003
313.17	10000.00	0.0003
313.14	15000.00	0.0003
313.16	20000.00	0.0003
313.15	25000.00	0.0003
313.16	30000.00	0.0003
313.16	35000.00	0.0004
313.16	40000.00	0.0004
323.16	1000.00	0.0002
323.17	5000.00	0.0002
323.17	10000.00	0.0003
323.17	15000.00	0.0003
323.17	20000.00	0.0003
323.17	25000.00	0.0003
323.17	30000.00	0.0003
323.17	35000.00	0.0003
323.17	40000.00	0.0003
333.15	1000.00	0.0002
333.16	5000.00	0.0002
333.16	10000.00	0.0002
333.16	15000.00	0.0003
333.16	20000.00	0.0003
333.16	25000.00	0.0003
333.16	30000.00	0.0003
333.16	35000.00	0.0003
333.17	40000.00	0.0003
343.15	1000.00	0.0002
343.15	5000.00	0.0002
343.16	10000.00	0.0002
343.16	15000.00	0.0002
343.16	20000.00	0.0002
343.16	25000.00	0.0003
343.15	30000.00	0.0003
343.16	35000.00	0.0003
343.15	40000.00	0.0003
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	673.34
100.00	288.15	668.91
100.00	293.15	664.28
100.00	298.15	659.73
100.00	303.15	655.07
100.00	308.15	650.44
100.00	313.15	645.7
100.00	318.15	640.93
100.00	323.15	636.14
100.00	328.15	631.22
2000.00	283.15	675.33
2000.00	288.15	670.93
2000.00	293.15	666.4
2000.00	298.15	661.91
2000.00	303.15	657.33
2000.00	308.15	652.85
2000.00	313.15	648.1
2000.00	318.15	643.46
2000.00	323.15	638.83
2000.00	328.15	634.03
5000.00	283.15	678.2
5000.00	288.15	673.95
5000.00	293.15	669.49
5000.00	298.15	665.13
5000.00	303.15	660.71
5000.00	308.15	656.28
5000.00	313.15	651.77
5000.00	318.15	647.27
5000.00	323.15	642.73
5000.00	328.15	638.2
7000.00	283.15	680.08
7000.00	288.15	675.9
7000.00	293.15	671.54
7000.00	298.15	667.22
7000.00	303.15	662.86
7000.00	308.15	658.61
7000.00	313.15	654.13
7000.00	318.15	649.71
7000.00	323.15	645.26
7000.00	328.15	640.84
10000.00	283.15	682.8
10000.00	288.15	678.66
10000.00	293.15	674.41
10000.00	298.15	670.25
10000.00	303.15	666.0
10000.00	308.15	661.77
10000.00	313.15	657.53
10000.00	318.15	653.27
10000.00	323.15	648.88
10000.00	328.15	644.64
20000.00	283.15	691.21
20000.00	288.15	687.28
20000.00	293.15	683.39
20000.00	298.15	679.53
20000.00	303.15	675.49
20000.00	308.15	671.68
20000.00	313.15	667.66
20000.00	318.15	663.74
20000.00	323.15	659.72
20000.00	328.15	655.85
30000.00	283.15	698.81
30000.00	288.15	695.19
30000.00	293.15	691.45
30000.00	298.15	687.73
30000.00	303.15	683.96
30000.00	308.15	680.42
30000.00	313.15	676.56
30000.00	318.15	672.89
30000.00	323.15	669.28
30000.00	328.15	665.6
40000.00	283.15	705.94
40000.00	288.15	702.32
40000.00	293.15	698.72
40000.00	298.15	695.4
40000.00	303.15	691.63
40000.00	308.15	688.33
40000.00	313.15	684.59
40000.00	318.15	681.17
40000.00	323.15	677.73
40000.00	328.15	674.39
50000.00	283.15	712.39
50000.00	288.15	708.77
50000.00	293.15	705.44
50000.00	298.15	702.25
50000.00	303.15	698.64
50000.00	308.15	695.51
50000.00	313.15	692.01
50000.00	318.15	688.56
50000.00	323.15	685.39
50000.00	328.15	682.22
60000.00	283.15	718.5
60000.00	288.15	715.04
60000.00	293.15	711.72
60000.00	298.15	708.63
60000.00	303.15	705.24
60000.00	308.15	702.1
60000.00	313.15	698.74
60000.00	318.15	695.68
60000.00	323.15	692.42
60000.00	328.15	689.42
65000.00	283.15	721.33
65000.00	288.15	718.14
65000.00	293.15	714.81
65000.00	298.15	711.62
65000.00	303.15	708.41
65000.00	308.15	705.28
65000.00	313.15	702.04
65000.00	318.15	699.05
65000.00	323.15	695.87
65000.00	328.15	692.79
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	659.76
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	96.00	673.7
283.15	4984.00	678.4
283.15	9983.00	682.9
283.15	14976.00	687.2
283.15	20022.00	691.2
283.15	25054.00	695.0
283.15	29951.00	698.6
283.15	35044.00	702.1
283.15	40019.00	705.4
283.15	45032.00	708.6
283.15	50012.00	711.7
283.15	54940.00	714.6
283.15	59937.00	717.5
283.15	64969.00	720.3
288.15	123.00	669.3
288.15	4981.00	674.1
288.15	10014.00	678.9
288.15	14991.00	683.2
288.15	19942.00	687.3
288.15	25033.00	691.3
288.15	29989.00	695.0
288.15	35037.00	698.6
288.15	39987.00	701.9
288.15	45029.00	705.2
288.15	50061.00	708.4
288.15	54941.00	711.3
288.15	59951.00	714.3
288.15	65035.00	717.1
293.15	98.00	664.7
293.15	4913.00	669.7
293.15	9979.00	674.6
293.15	14916.00	679.1
293.15	19985.00	683.5
293.15	24964.00	687.5
293.15	30011.00	691.3
293.15	34951.00	694.9
293.15	40003.00	698.4
293.15	45015.00	701.8
293.15	49957.00	705.0
293.15	54949.00	708.1
293.15	60008.00	711.1
293.15	65001.00	714.0
298.15	123.00	660.1
298.15	4936.00	665.3
298.15	9999.00	670.4
298.15	15031.00	675.1
298.15	20036.00	679.5
298.15	25016.00	683.7
298.15	29992.00	687.6
298.15	34973.00	691.3
298.15	40043.00	694.9
298.15	45008.00	698.3
298.15	49987.00	701.6
298.15	54938.00	704.8
298.15	59982.00	707.8
298.15	65001.00	710.8
303.15	106.00	655.4
303.15	4970.00	660.9
303.15	9996.00	666.1
303.15	15043.00	671.1
303.15	20006.00	675.6
303.15	25024.00	679.9
303.15	29956.00	683.9
303.15	34990.00	687.7
303.15	39963.00	691.4
303.15	44991.00	694.9
303.15	49940.00	698.2
303.15	54932.00	701.5
303.15	59961.00	704.6
303.15	65012.00	707.7
308.15	109.00	650.6
308.15	4967.00	656.3
308.15	10001.00	661.8
308.15	14988.00	666.8
308.15	19945.00	671.5
308.15	25037.00	676.0
308.15	29968.00	680.1
308.15	35020.00	684.0
308.15	39963.00	687.8
308.15	44985.00	691.4
308.15	49992.00	694.8
308.15	54921.00	698.1
308.15	60008.00	701.4
308.15	64999.00	704.4
313.15	117.00	645.9
313.15	4981.00	651.9
313.15	9993.00	657.5
313.15	15145.00	662.9
313.15	20027.00	667.6
313.15	25088.00	672.2
313.15	30012.00	676.4
313.15	35003.00	680.4
313.15	40042.00	684.3
313.15	45054.00	688.0
313.15	49996.00	691.5
313.15	54926.00	694.8
313.15	60053.00	698.2
313.15	65063.00	701.3
318.15	107.00	641.1
318.15	4955.00	647.4
318.15	9991.00	653.3
318.15	15039.00	658.8
318.15	20021.00	663.7
318.15	25060.00	668.4
318.15	29991.00	672.8
318.15	34997.00	676.9
318.15	40044.00	680.9
318.15	44936.00	684.6
318.15	49998.00	688.3
318.15	55010.00	691.7
318.15	59996.00	695.1
318.15	65008.00	698.3
323.15	106.00	636.3
323.15	4980.00	642.9
323.15	9966.00	649.0
323.15	15009.00	654.6
323.15	20016.00	659.8
323.15	24987.00	664.6
323.15	30019.00	669.1
323.15	34996.00	673.3
323.15	40041.00	677.4
323.15	44988.00	681.2
323.15	49949.00	684.9
323.15	55004.00	688.5
323.15	59997.00	691.8
323.15	64995.00	695.1
328.15	4974.00	638.3
328.15	9983.00	644.6
328.15	14977.00	650.4
328.15	20010.00	655.8
328.15	25021.00	660.8
328.15	29956.00	665.4
328.15	34961.00	669.7
328.15	40039.00	673.9
328.15	45005.00	677.9
328.15	50036.00	681.7
328.15	54981.00	685.2
328.15	60023.00	688.7
328.15	65018.00	692.0
333.15	4969.00	633.7
333.15	9932.00	640.2
333.15	15031.00	646.3
333.15	19959.00	651.8
333.15	25022.00	657.0
333.15	29983.00	661.7
333.15	34948.00	666.1
333.15	39982.00	670.4
333.15	45015.00	674.5
333.15	49968.00	678.3
333.15	54981.00	682.0
333.15	59935.00	685.5
333.15	65077.00	689.0
338.15	5021.00	629.0
338.15	10019.00	635.9
338.15	15009.00	642.1
338.15	20030.00	647.8
338.15	25053.00	653.1
338.15	29999.00	658.0
338.15	34951.00	662.6
338.15	39974.00	667.0
338.15	45053.00	671.2
338.15	49966.00	675.1
338.15	54970.00	678.8
338.15	59984.00	682.5
338.15	65015.00	685.9
343.15	5000.00	624.2
343.15	10002.00	631.4
343.15	15025.00	637.8
343.15	20016.00	643.7
343.15	24973.00	649.1
343.15	29947.00	654.2
343.15	34977.00	658.9
343.15	39962.00	663.4
343.15	44924.00	667.6
343.15	50034.00	671.8
343.15	54984.00	675.6
343.15	59973.00	679.3
343.15	65018.00	682.9
348.15	4999.00	619.4
348.15	10005.00	626.9
348.15	15001.00	633.6
348.15	19997.00	639.7
348.15	24983.00	645.3
348.15	30044.00	650.6
348.15	34962.00	655.3
348.15	40008.00	660.0
348.15	44956.00	664.3
348.15	50006.00	668.4
348.15	54987.00	672.4
348.15	59977.00	676.1
348.15	65005.00	679.8
353.15	4969.00	614.4
353.15	9927.00	622.1
353.15	14990.00	629.2
353.15	20018.00	635.5
353.15	25032.00	641.3
353.15	29979.00	646.6
353.15	34952.00	651.6
353.15	39962.00	656.4
353.15	44947.00	660.8
353.15	49917.00	665.0
353.15	55013.00	669.1
353.15	59927.00	672.9
353.15	65026.00	676.6
358.15	4945.00	609.3
358.15	9952.00	617.5
358.15	15000.00	624.7
358.15	20004.00	631.3
358.15	25020.00	637.3
358.15	29990.00	642.7
358.15	34993.00	647.8
358.15	40000.00	652.7
358.15	44971.00	657.2
358.15	49932.00	661.5
358.15	54965.00	665.6
358.15	59980.00	669.6
358.15	65056.00	673.4
363.15	5004.00	604.2
363.15	9965.00	612.8
363.15	15052.00	620.5
363.15	19925.00	627.1
363.15	25013.00	633.3
363.15	29929.00	638.9
363.15	35008.00	644.2
363.15	39979.00	649.1
363.15	45062.00	653.9
363.15	50011.00	658.2
363.15	54995.00	662.4
363.15	60039.00	666.4
363.15	65041.00	670.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[98.95; 394.23]	J/mol×K	[200.00; 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			6.63230e+01
Coefficient B			-4.79350e+02
Coefficient C			5.80524e+00
Coefficient D			4.10580e-04
Coefficient E			-1.37250e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	98.95	J/mol×K	200.00	Calculated Property
Cp,gas	159.89	J/mol×K	344.44	Calculated Property
Cp,gas	213.65	J/mol×K	488.89	Calculated Property
Cp,gas	257.53	J/mol×K	633.33	Calculated Property
Cp,gas	293.39	J/mol×K	777.78	Calculated Property
Cp,gas	322.89	J/mol×K	922.22	Calculated Property
Cp,gas	347.12	J/mol×K	1066.67	Calculated Property
Cp,gas	366.81	J/mol×K	1211.11	Calculated Property
Cp,gas	382.40	J/mol×K	1355.56	Calculated Property
Cp,gas	394.23	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[142.16; 205.79]	J/mol×K	[79.81; 336.43]	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			1.24870e+02
Coefficient B			3.74700e+01
Coefficient C			1.59084e+00
Coefficient D			1.04890e-02
Coefficient E			-7.40050e-06
Temperature range, min.			79.81
Temperature range, max.			336.43
Cp,liquid	142.16	J/mol×K	79.81	Calculated Property
Cp,liquid	144.68	J/mol×K	108.32	Calculated Property
Cp,liquid	148.47	J/mol×K	136.84	Calculated Property
Cp,liquid	153.36	J/mol×K	165.35	Calculated Property
Cp,liquid	159.32	J/mol×K	193.86	Calculated Property
Cp,liquid	166.38	J/mol×K	222.38	Calculated Property
Cp,liquid	174.57	J/mol×K	250.89	Calculated Property
Cp,liquid	183.89	J/mol×K	279.40	Calculated Property
Cp,liquid	194.32	J/mol×K	307.92	Calculated Property
Cp,liquid	205.79	J/mol×K	336.43	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0007666; 0.0001268]	Pa×s	[220.00; 403.52]	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			-4.44660e+00
Coefficient B			5.61390e+02
Coefficient C			-9.74960e-01
Coefficient D			-4.15250e-07
Coefficient E			2.00000e+00
Temperature range, min.			220.00
Temperature range, max.			403.52
η	0.0007666	Pa×s	220.00	Calculated Property
η	0.0005641	Pa×s	240.39	Calculated Property
η	0.0004323	Pa×s	260.78	Calculated Property
η	0.0003420	Pa×s	281.17	Calculated Property
η	0.0002777	Pa×s	301.56	Calculated Property
η	0.0002304	Pa×s	321.96	Calculated Property
η	0.0001945	Pa×s	342.35	Calculated Property
η	0.0001666	Pa×s	362.74	Calculated Property
η	0.0001446	Pa×s	383.13	Calculated Property
η	0.0001268	Pa×s	403.52	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[42.45; 12.60]	kJ/mol	[110.25; 483.84]	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			5.26104e+01
Coefficient B			1.02151e+00
Coefficient C			-6.56827e-01
Coefficient D			-2.22599e-01
Coefficient E			2.94618e-01
Critical temperature, Tc (K)			5.04400e+02
Temperature range, min.			110.25
Temperature range, max.			483.84
ΔvapH	42.45	kJ/mol	110.25	Calculated Property
ΔvapH	39.34	kJ/mol	151.76	Calculated Property
ΔvapH	36.55	kJ/mol	193.27	Calculated Property
ΔvapH	33.99	kJ/mol	234.78	Calculated Property
ΔvapH	31.58	kJ/mol	276.29	Calculated Property
ΔvapH	29.17	kJ/mol	317.80	Calculated Property
ΔvapH	26.61	kJ/mol	359.31	Calculated Property
ΔvapH	23.58	kJ/mol	400.82	Calculated Property
ΔvapH	19.53	kJ/mol	442.33	Calculated Property
ΔvapH	12.60	kJ/mol	483.84	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[241.87; 360.03]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42821e+01
Coefficient B			-2.95275e+03
Coefficient C			-3.08720e+01
Temperature range, min.			241.87
Temperature range, max.			360.03
Pvap	1.33	kPa	241.87	Calculated Property
Pvap	3.03	kPa	255.00	Calculated Property
Pvap	6.28	kPa	268.13	Calculated Property
Pvap	12.05	kPa	281.26	Calculated Property
Pvap	21.69	kPa	294.39	Calculated Property
Pvap	36.91	kPa	307.51	Calculated Property
Pvap	59.87	kPa	320.64	Calculated Property
Pvap	93.12	kPa	333.77	Calculated Property
Pvap	139.60	kPa	346.90	Calculated Property
Pvap	202.65	kPa	360.03	Calculated Property
Pvap	[3.53e-11; 3131.23]	kPa	[110.25; 504.40]	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			9.64791e+01
Coefficient B			-6.79229e+03
Coefficient C			-1.25658e+01
Coefficient D			1.27267e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 504.6 K.
Temperature range, min.			110.25
Temperature range, max.			504.40
Pvap	3.53e-11	kPa	110.25	Calculated Property
Pvap	2.47e-05	kPa	154.04	Calculated Property
Pvap	0.02	kPa	197.84	Calculated Property
Pvap	1.17	kPa	241.63	Calculated Property
Pvap	14.47	kPa	285.43	Calculated Property
Pvap	80.36	kPa	329.22	Calculated Property
Pvap	278.88	kPa	373.02	Calculated Property
Pvap	727.26	kPa	416.81	Calculated Property
Pvap	1591.28	kPa	460.61	Calculated Property
Pvap	3131.23	kPa	504.40	Calculated Property
Pvap	[1.11e-10; 3114.82]	kPa	[110.25; 504.43]	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			7.95641e+01
Coefficient B			-6.17296e+03
Coefficient C			-9.91026e+00
Coefficient D			9.40493e-06
Coefficient E			0.00000e+00
Temperature range, min.			110.25
Temperature range, max.			504.43
Pvap	1.11e-10	kPa	110.25	Calculated Property
Pvap	3.70e-05	kPa	154.05	Calculated Property
Pvap	0.03	kPa	197.85	Calculated Property
Pvap	1.20	kPa	241.64	Calculated Property
Pvap	14.46	kPa	285.44	Calculated Property
Pvap	80.38	kPa	329.24	Calculated Property
Pvap	281.37	kPa	373.04	Calculated Property
Pvap	737.75	kPa	416.83	Calculated Property
Pvap	1608.38	kPa	460.63	Calculated Property
Pvap	3114.82	kPa	504.43	Calculated Property
Pvap	[16.60; 103.89]	kPa	[288.44; 337.23]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37551e+01
Coefficient B			-2.65343e+03
Coefficient C			-4.60210e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			288.44
Temperature range, max.			337.23
Pvap	16.60	kPa	288.44	Calculated Property
Pvap	21.09	kPa	293.86	Calculated Property
Pvap	26.52	kPa	299.28	Calculated Property
Pvap	33.04	kPa	304.70	Calculated Property
Pvap	40.78	kPa	310.12	Calculated Property
Pvap	49.91	kPa	315.55	Calculated Property
Pvap	60.61	kPa	320.97	Calculated Property
Pvap	73.04	kPa	326.39	Calculated Property
Pvap	87.40	kPa	331.81	Calculated Property
Pvap	103.89	kPa	337.23	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[803.14; 267.05]	kg/m3	[110.25; 504.40]	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			5.53168e+01
Coefficient B			2.51800e-01
Coefficient C			5.04610e+02
Coefficient D			2.51140e-01
Comment			Range stopped at Tc; ChemSep gives it to 504.6 K.
Temperature range, min.			110.25
Temperature range, max.			504.40
ρl	803.14	kg/m3	110.25	Calculated Property
ρl	773.37	kg/m3	154.04	Calculated Property
ρl	741.95	kg/m3	197.84	Calculated Property
ρl	708.46	kg/m3	241.63	Calculated Property
ρl	672.32	kg/m3	285.43	Calculated Property
ρl	632.60	kg/m3	329.22	Calculated Property
ρl	587.70	kg/m3	373.02	Calculated Property
ρl	534.39	kg/m3	416.81	Calculated Property
ρl	463.85	kg/m3	460.61	Calculated Property
ρl	267.05	kg/m3	504.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[110.15; 336.15]	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			4.92139e-02
Coefficient B			-1.06000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			110.15
Temperature range, max.			336.15
γ	0.04	N/m	110.15	Calculated Property
γ	0.03	N/m	135.26	Calculated Property
γ	0.03	N/m	160.37	Calculated Property
γ	0.03	N/m	185.48	Calculated Property
γ	0.03	N/m	210.59	Calculated Property
γ	0.02	N/m	235.71	Calculated Property
γ	0.02	N/m	260.82	Calculated Property
γ	0.02	N/m	285.93	Calculated Property
γ	0.02	N/m	311.04	Calculated Property
γ	0.01	N/m	336.15	Calculated Property
γ	[0.04; 9.23e-04]	N/m	[110.25; 483.84]	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			-1.34210e-02
Coefficient B			7.97980e+00
Coefficient C			-2.86500e+00
Coefficient D			-9.25520e-04
Coefficient E			-4.05010e-06
Temperature range, min.			110.25
Temperature range, max.			483.84
γ	0.04	N/m	110.25	Calculated Property
γ	0.03	N/m	151.76	Calculated Property
γ	0.03	N/m	193.27	Calculated Property
γ	0.02	N/m	234.78	Calculated Property
γ	0.02	N/m	276.29	Calculated Property
γ	0.02	N/m	317.80	Calculated Property
γ	0.01	N/m	359.31	Calculated Property
γ	0.01	N/m	400.82	Calculated Property
γ	0.00	N/m	442.33	Calculated Property
γ	9.23e-04	N/m	483.84	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[8.06e-04; 0.10]	W/m×K	[110.25; 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			5.01780e-05
Coefficient B			1.11430e+00
Coefficient C			-6.75560e+01
Coefficient D			1.38050e+05
Temperature range, min.			110.25
Temperature range, max.			1000.00
λgas	8.06e-04	W/m×K	110.25	Calculated Property
λgas	0.01	W/m×K	209.11	Calculated Property
λgas	0.01	W/m×K	307.97	Calculated Property
λgas	0.02	W/m×K	406.83	Calculated Property
λgas	0.04	W/m×K	505.69	Calculated Property
λgas	0.05	W/m×K	604.56	Calculated Property
λgas	0.06	W/m×K	703.42	Calculated Property
λgas	0.08	W/m×K	802.28	Calculated Property
λgas	0.09	W/m×K	901.14	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.08]	W/m×K	[110.25; 402.00]	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			1.36850e-02
Coefficient B			3.29120e+01
Coefficient C			-2.24000e+00
Coefficient D			9.79640e-04
Coefficient E			-5.62920e-06
Temperature range, min.			110.25
Temperature range, max.			402.00
λliquid	0.16	W/m×K	110.25	Calculated Property
λliquid	0.15	W/m×K	142.67	Calculated Property
λliquid	0.14	W/m×K	175.08	Calculated Property
λliquid	0.13	W/m×K	207.50	Calculated Property
λliquid	0.13	W/m×K	239.92	Calculated Property
λliquid	0.12	W/m×K	272.33	Calculated Property
λliquid	0.11	W/m×K	304.75	Calculated Property
λliquid	0.10	W/m×K	337.17	Calculated Property
λliquid	0.09	W/m×K	369.58	Calculated Property
λliquid	0.08	W/m×K	402.00	Calculated Property

Similar Compounds

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

Mixtures

• Hexadecane + Pentane, 3-methyl-
• Pentane, 3-methyl- + Octadecane
• Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
• Dodecane + Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
• Decane + Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-
• Pentane, 3-methyl- + Methyl Alcohol
• Ethanol + Cyclohexane, methyl- + Pentane, 3-methyl-
• Methane, trifluoro- + Pentane, 3-methyl-
• Ethane, hexafluoro- + Pentane, 3-methyl-
• Carbon dioxide + Pentane, 3-methyl-
• 2-Pyrrolidinone, 1-methyl- + Pentane, 3-methyl-
• 1-Hexene + Pentane, 3-methyl-
• Cyclopentane + Pentane, 3-methyl- + Methyl Alcohol
• Pentane, 3-methyl- + N-Formylmorpholine
• Diisopropyl ether + Pentane, 3-methyl-
• n-Butyl ether + Pentane, 3-methyl-
• Pentane, 3-methyl- + Water
• Diisopropyl ether + Octane + Pentane, 3-methyl-
• Diisopropyl ether + Decane + Pentane, 3-methyl-
• Butane, 1-chloro- + Pentane, 3-methyl-

Find more mixtures with Pentane, 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).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 ChEDL chemicals 1.5.2, from Daubert, T. E. Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes. J. Chem. Eng. Data 1996, 41, 365-372.
• 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).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• 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
• Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
• Solubility of CO2 in branched alkanes in order to extend the PPR78 model (predictive 1978, Peng Robinson EOS with temperature-dependent kij calculated through a group contribution method) to such systems
• Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa
• Liquid liquid equilibria of lactam containing binary systems
• Experimental and VTPR-predicted volumetric properties of branched hexanes
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
• Influence of size and shape effects on the high-pressure solubility of n-alkanes: Experimental data, correlation and prediction
• Influence of temperature on the (liquid + liquid) equilibria of {3-methyl pentane + cyclopentane + methanol} ternary system at T = (293.15, 297.15, and 299.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• (Liquid + liquid) equilibrium for binary systems of N-formylmorpholine with alkanes
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Conformational analysis of branched alkanes using limiting partial molar volumes
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Compressed Liquid Viscosity of 2-Methylpentane, 3-Methylpentane, and 2,3-Dimethylbutane at Temperatures from (273 to 343) K and Pressures up to 40 MPa
• P-r-T Data and Derivative Properties of 3-Methylpentane, 2,4-Dimethylpentane, and 2,3,4-Trimethylpentane from 283.15 to 363.15 K at Pressures up to 65 MPa
• Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
• Excess Enthalpies of the Ternary Mixtures: Diisopropyl Ether + 3-Methylpentane + (Octane or Decane) at 298.15 K
• Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
• Influence of High Pressure on the Liquidus Curve Shape in Binary Hydrocarbon Mixtures: Experimental Data, Correlation, and Prediction
• Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Mutual Solubility Measurements of Hydrocarbon-Water Systems Containing Benzene, Toluene, and 3-Methylpentane
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• 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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