Chemical Properties of 1-Hexene (CAS 592-41-6)

InChI

InChI=1S/C6H12/c1-3-5-6-4-2/h3H,1,4-6H2,2H3

InChI Key

LIKMAJRDDDTEIG-UHFFFAOYSA-N

Formula

C6H12

SMILES

C=CCCCC

Molecular Weight¹

84.16

CAS

592-41-6

Other Names

• 1-C6H12
• 1-n-Hexene
• Butylethylene
• Dialene 6
• Hexene
• Hexene-1
• Hexylene
• NSC 74121
• Neodene 6 XHP
• UN 2370
• hex-1-ene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• BasG : Gas basicity (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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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).
• 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.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• 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	[0.2810; 0.2850]
ω	0.2839		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2848		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2810		ChemSep v8.3 pure component data Compiled value
ω	0.2850		KDB
PAff	805.20	kJ/mol	NIST
Tig	544.82	K	KDB
AP	295.950	K	KDB
BasG	776.30	kJ/mol	NIST
μ	[0.40; 0.45]	debye
μ	0.45	debye	ChemSep v8.3 pure component data Compiled value
μ	0.40	debye	KDB
LFL	1.20	% in Air	KDB
Tflash,cc	255.37	K	KDB
Tflash,oc	247.04	K	KDB
ΔfG°	[87.00; 87.50]	kJ/mol
ΔfG°	87.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	87.50	kJ/mol	KDB
Rg	3.6470		KDB
Δc,grossH	4003.75	kJ/mol	KDB
Δc,netH	3739.659	kJ/mol	KDB
ΔfH°gas	[-44.80; -41.40]	kJ/mol
ΔfH°gas	-41.67	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-41.70	kJ/mol	KDB
ΔfH°gas	-42.10 ± 1.20	kJ/mol	NIST
ΔfH°gas	Outlier -44.80 ± 1.40	kJ/mol	NIST
ΔfH°gas	-41.70	kJ/mol	NIST
ΔfH°gas	-41.40 ± 0.90	kJ/mol	NIST
ΔfH°gas	Outlier -44.80 ± 1.00	kJ/mol	NIST
ΔfH°gas	-41.50 ± 1.20	kJ/mol	NIST
ΔfH°gas	-42.09	kJ/mol	NIST
ΔfH°gas	-43.00 ± 1.50	kJ/mol	NIST
ΔfH°gas	-41.50 ± 1.00	kJ/mol	NIST
ΔfH°gas	-42.10 ± 2.10	kJ/mol	NIST
ΔfH°liquid	[-75.40; -72.00]	kJ/mol
ΔfH°liquid	-72.70 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-75.40 ± 1.40	kJ/mol	NIST
ΔfH°liquid	-72.30 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-72.00 ± 0.80	kJ/mol	NIST
ΔfH°liquid	-75.40 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-72.10 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-73.60 ± 1.50	kJ/mol	NIST
ΔfH°liquid	-72.10 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-72.70 ± 2.10	kJ/mol	NIST
ΔfusH°	10.02	kJ/mol	Joback Calculated Property
ΔvapH°	[30.60; 30.60]	kJ/mol
ΔvapH°	30.60	kJ/mol	NIST
ΔvapH°	30.60	kJ/mol	NIST
ΔvapH°	30.60	kJ/mol	NIST
IE	[9.31; 9.65]	eV
IE	9.44 ± 0.04	eV	NIST
IE	9.46 ± 0.05	eV	NIST
IE	9.37 ± 0.02	eV	NIST
IE	9.44	eV	NIST
IE	9.44	eV	NIST
IE	9.48 ± 0.00	eV	NIST
IE	9.31	eV	NIST
IE	9.33	eV	NIST
IE	9.46 ± 0.02	eV	NIST
IE	9.45 ± 0.02	eV	NIST
IE	Outlier 9.65 ± 0.01	eV	NIST
log10WS	[-3.23; -3.23]
log10WS	-3.23		Aq. Solubility Prediction
log10WS	-3.23		Estimated Solubility
logPoct/wat	2.363		Crippen Calculated Property
McVol	91.100	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3143.00; 3210.00]	kPa
Pc	3210.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	3206.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3171.59	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3143.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3210.00	kPa	KDB
Pc	3210.00 ± 30.00	kPa	NIST
Ptriple	5.16e-07	kPa	ChemSep v8.3 pure component data Compiled value
ρc	237.33 ± 2.52	kg/m3	NIST
Inp	[580.00; 601.00]
Inp	589.00		NIST
Inp	581.50		NIST
Inp	585.90		NIST
Inp	584.00		NIST
Inp	582.00		NIST
Inp	588.96		NIST
Inp	587.00		NIST
Inp	581.00		NIST
Inp	588.00		NIST
Inp	592.00		NIST
Inp	590.00		NIST
Inp	588.00		NIST
Inp	589.00		NIST
Inp	589.00		NIST
Inp	583.00		NIST
Inp	589.40		NIST
Inp	590.00		NIST
Inp	582.50		NIST
Inp	583.00		NIST
Inp	588.90		NIST
Inp	Outlier 598.00		NIST
Inp	589.00		NIST
Inp	589.00		NIST
Inp	590.00		NIST
Inp	588.00		NIST
Inp	588.00		NIST
Inp	588.00		NIST
Inp	589.00		NIST
Inp	589.00		NIST
Inp	589.00		NIST
Inp	594.00		NIST
Inp	594.10		NIST
Inp	594.30		NIST
Inp	594.40		NIST
Inp	594.60		NIST
Inp	594.80		NIST
Inp	593.00		NIST
Inp	589.00		NIST
Inp	587.00		NIST
Inp	589.10		NIST
Inp	589.40		NIST
Inp	589.70		NIST
Inp	590.00		NIST
Inp	590.40		NIST
Inp	590.00		NIST
Inp	583.50		NIST
Inp	584.50		NIST
Inp	585.20		NIST
Inp	586.20		NIST
Inp	587.10		NIST
Inp	588.20		NIST
Inp	582.00		NIST
Inp	582.00		NIST
Inp	Outlier 596.00		NIST
Inp	582.10		NIST
Inp	582.50		NIST
Inp	582.36		NIST
Inp	583.00		NIST
Inp	582.00		NIST
Inp	584.00		NIST
Inp	584.50		NIST
Inp	582.00		NIST
Inp	582.00		NIST
Inp	583.00		NIST
Inp	583.00		NIST
Inp	582.00		NIST
Inp	583.00		NIST
Inp	589.00		NIST
Inp	589.00		NIST
Inp	581.38		NIST
Inp	586.90		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	583.00		NIST
Inp	589.60		NIST
Inp	582.30		NIST
Inp	582.00		NIST
Inp	589.00		NIST
Inp	580.00		NIST
Inp	Outlier 596.00		NIST
Inp	584.00		NIST
Inp	583.10		NIST
Inp	583.00		NIST
Inp	588.00		NIST
Inp	Outlier 596.00		NIST
Inp	582.00		NIST
Inp	583.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	593.00		NIST
Inp	583.00		NIST
Inp	583.00		NIST
Inp	587.00		NIST
Inp	586.00		NIST
Inp	585.00		NIST
Inp	591.20		NIST
Inp	590.00		NIST
Inp	589.00		NIST
Inp	588.20		NIST
Inp	587.90		NIST
Inp	587.90		NIST
Inp	584.20		NIST
Inp	588.40		NIST
Inp	588.20		NIST
Inp	587.90		NIST
Inp	587.90		NIST
Inp	584.67		NIST
Inp	584.79		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	Outlier 596.00		NIST
Inp	590.00		NIST
Inp	584.00		NIST
Inp	Outlier 596.84		NIST
Inp	581.50		NIST
Inp	592.00		NIST
Inp	582.00		NIST
Inp	Outlier 600.00		NIST
Inp	589.00		NIST
Inp	589.00		NIST
Inp	583.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	592.00		NIST
Inp	593.00		NIST
Inp	585.00		NIST
Inp	585.00		NIST
Inp	584.70		NIST
Inp	585.32		NIST
Inp	589.00		NIST
Inp	587.00		NIST
Inp	584.00		NIST
Inp	590.00		NIST
Inp	591.00		NIST
Inp	588.00		NIST
Inp	585.00		NIST
Inp	590.00		NIST
Inp	592.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	589.00		NIST
Inp	584.00		NIST
Inp	591.00		NIST
Inp	583.00		NIST
Inp	Outlier 601.00		NIST
Inp	588.00		NIST
Inp	589.00		NIST
Inp	588.00		NIST
Inp	590.00		NIST
Inp	587.00		NIST
Inp	584.00		NIST
Inp	584.00		NIST
Inp	587.00		NIST
Inp	585.00		NIST
Inp	592.00		NIST
Inp	582.00		NIST
Inp	592.00		NIST
Inp	582.00		NIST
Inp	586.00		NIST
Inp	589.00		NIST
Inp	592.00		NIST
Inp	585.32		NIST
Inp	591.00		NIST
Inp	584.00		NIST
Inp	590.00		NIST
Ip	[610.00; 674.00]
Ip	648.00		NIST
Ip	649.00		NIST
Ip	648.50		NIST
Ip	648.70		NIST
Ip	648.70		NIST
Ip	648.50		NIST
Ip	632.00		NIST
Ip	622.00		NIST
Ip	674.00		NIST
Ip	610.00		NIST
Ip	674.00		NIST
S°liquid	295.18	J/mol×K	NIST
Tboil	[280.00; 341.45]	K
Tboil	336.48	K	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Tboil	336.63	K	ChemSep v8.3 pure component data Compiled value
Tboil	336.63	K	KDB
Tboil	336.50	K	NIST
Tboil	336.66 ± 0.30	K	NIST
Tboil	336.70 ± 0.20	K	NIST
Tboil	336.80 ± 1.00	K	NIST
Tboil	337.30 ± 0.40	K	NIST
Tboil	337.30 ± 0.20	K	NIST
Tboil	Outlier 280.00 ± 3.00	K	NIST
Tboil	336.64 ± 0.50	K	NIST
Tboil	336.95 ± 1.00	K	NIST
Tboil	338.65 ± 2.00	K	NIST
Tboil	335.23 ± 0.60	K	NIST
Tboil	336.70 ± 2.00	K	NIST
Tboil	336.65 ± 1.00	K	NIST
Tboil	338.40 ± 1.50	K	NIST
Tboil	336.65 ± 0.50	K	NIST
Tboil	337.15 ± 3.00	K	NIST
Tboil	336.64 ± 0.50	K	NIST
Tboil	336.40 ± 0.70	K	NIST
Tboil	336.60 ± 0.30	K	NIST
Tboil	336.70 ± 0.60	K	NIST
Tboil	336.65 ± 0.30	K	NIST
Tboil	336.60 ± 0.30	K	NIST
Tboil	336.60 ± 0.30	K	NIST
Tboil	336.67 ± 0.20	K	NIST
Tboil	336.65 ± 0.50	K	NIST
Tboil	336.70 ± 0.60	K	NIST
Tboil	337.10 ± 1.50	K	NIST
Tboil	336.75 ± 0.50	K	NIST
Tboil	336.70 ± 0.50	K	NIST
Tboil	336.60 ± 0.40	K	NIST
Tboil	339.90 ± 1.20	K	NIST
Tboil	337.00 ± 0.60	K	NIST
Tboil	336.65 ± 0.30	K	NIST
Tboil	341.45 ± 0.50	K	NIST
Tboil	336.70 ± 0.60	K	NIST
Tboil	335.65 ± 3.00	K	NIST
Tboil	337.90 ± 1.50	K	NIST
Tboil	335.15 ± 0.50	K	NIST
Tboil	336.50 ± 0.30	K	NIST
Tboil	335.15 ± 1.50	K	NIST
Tboil	336.50 ± 0.30	K	NIST
Tboil	339.00 ± 3.00	K	NIST
Tboil	340.15 ± 2.00	K	NIST
Tboil	340.00 ± 2.00	K	NIST
Tc	[503.98; 504.03]	K
Tc	504.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	504.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	Outlier 504.03	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	504.00	K	ChemSep v8.3 pure component data Compiled value
Tc	504.00	K	KDB
Tc	504.00 ± 0.30	K	NIST
Tc	503.98 ± 0.30	K	NIST
Tfus	[128.15; 135.15]	K
Tfus	133.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	133.39	K	ChemSep v8.3 pure component data Compiled value
Tfus	133.39	K	KDB
Tfus	133.18	K	Aq. Solubility Prediction
Tfus	133.15 ± 1.00	K	NIST
Tfus	133.25 ± 0.30	K	NIST
Tfus	133.28 ± 0.30	K	NIST
Tfus	133.11 ± 0.30	K	NIST
Tfus	132.15 ± 1.50	K	NIST
Tfus	Outlier 128.15 ± 1.50	K	NIST
Tfus	134.00 ± 6.00	K	NIST
Tfus	135.15 ± 2.00	K	NIST
Tfus	133.70 ± 2.00	K	NIST
Ttriple	[133.38; 133.40]	K
Ttriple	133.40	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	133.39	K	ChemSep v8.3 pure component data Compiled value
Ttriple	133.39 ± 0.01	K	NIST
Ttriple	133.38 ± 0.05	K	NIST
Ttriple	133.39 ± 0.02	K	NIST
Ttriple	133.39 ± 0.01	K	NIST
UQi	3.64		ChemSep v8.3 pure component data Compiled value
URi	4.27		ChemSep v8.3 pure component data Compiled value
Vc	[0.350; 0.355]	m3/kmol
Vc	0.355	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.350	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.355	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.355	m3/kmol	KDB
Vc	0.355	m3/kmol	NIST
VCOSTALD	0.35	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2660000; 0.2720120]
Zc	0.2720000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Zc	0.2660000		ChemSep v8.3 pure component data Compiled value
Zc	0.2720120		KDB
Zra	[0.27; 0.27]
Zra	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[182.77; 183.30]	J/mol×K	[298.15; 298.56]
Cp,liquid	183.30	J/mol×K	298.15	NIST
Cp,liquid	182.77	J/mol×K	298.56	NIST
Csat	[154.30; 187.40]	J/mol×K	[140.00; 310.00]
Csat	154.30	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
Csat	154.30	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
Csat	154.60	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	155.20	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
Csat	156.10	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	157.20	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	158.60	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	160.20	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
Csat	162.10	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	164.20	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	166.50	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	169.00	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	171.60	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	174.50	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	175.40	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	177.50	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	180.70	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
Csat	183.30	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	184.00	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
Csat	187.40	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
η	[0.0002360; 0.0002800]	Pa×s	[293.15; 313.15]
η	0.0002800	Pa×s	293.15	Density, Viscosity, and Isobaric Heat Capacity of the Mixture (1-Butanol + 1-Hexene)
η	0.0002570	Pa×s	303.15	Density, Viscosity, and Isobaric Heat Capacity of the Mixture (1-Butanol + 1-Hexene)
η	0.0002360	Pa×s	313.15	Density, Viscosity, and Isobaric Heat Capacity of the Mixture (1-Butanol + 1-Hexene)
ΔfusH	[9.35; 9.35]	kJ/mol	[133.39; 133.40]
ΔfusH	9.35	kJ/mol	133.39	NIST
ΔfusH	9.35	kJ/mol	133.39	NIST
ΔfusH	9.35	kJ/mol	133.40	NIST
ΔfusH	9.35	kJ/mol	133.40	NIST
ΔvapH	[28.28; 31.60]	kJ/mol	[308.00; 337.90]
ΔvapH	31.60	kJ/mol	308.00	NIST
ΔvapH	31.00	kJ/mol	313.00	NIST
ΔvapH	30.40	kJ/mol	317.00	NIST
ΔvapH	30.60	kJ/mol	318.50	NIST
ΔvapH	28.28	kJ/mol	337.90	KDB
Pvap	[4.46; 218.50]	kPa	[263.15; 363.15]
Pvap	4.46	kPa	263.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	4.50	kPa	263.45	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	7.72	kPa	273.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	7.69	kPa	273.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	7.70	kPa	273.32	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	12.71	kPa	283.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	12.64	kPa	283.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	12.80	kPa	283.24	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	20.08	kPa	293.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	19.98	kPa	293.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	20.10	kPa	293.22	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	24.93	kPa	298.07	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	24.77	kPa	298.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	27.41	kPa	300.32	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	30.08	kPa	302.55	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	30.54	kPa	303.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	30.46	kPa	303.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	30.60	kPa	303.22	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	32.46	kPa	304.54	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	34.84	kPa	306.31	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	37.48	kPa	308.20	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	39.96	kPa	309.84	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	42.53	kPa	311.51	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	44.96	kPa	312.98	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	44.98	kPa	313.15	Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4- trimethylpentane and 1-hexene at 313.15 K
Pvap	44.96	kPa	313.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	44.98	kPa	313.15	Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
Pvap	44.98	kPa	313.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	45.00	kPa	313.15	Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
Pvap	45.00	kPa	313.20	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	47.42	kPa	314.38	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	49.92	kPa	315.79	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	52.53	kPa	317.17	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	54.98	kPa	318.43	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	57.39	kPa	319.62	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	59.94	kPa	320.84	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	62.51	kPa	322.02	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	64.28	kPa	323.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	64.60	kPa	323.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	64.97	kPa	323.16	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	64.40	kPa	323.19	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	67.45	kPa	324.21	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	69.88	kPa	325.25	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	72.44	kPa	326.29	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	75.04	kPa	327.32	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	77.45	kPa	328.25	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	79.98	kPa	329.21	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	82.42	kPa	330.11	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	84.93	kPa	331.01	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	87.33	kPa	331.86	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	89.92	kPa	332.74	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	89.55	kPa	333.15	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	90.44	kPa	333.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	89.70	kPa	333.23	Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
Pvap	92.54	kPa	333.62	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	94.82	kPa	334.38	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	97.45	kPa	335.24	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	101.30	kPa	336.48	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	123.79	kPa	343.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	165.99	kPa	353.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
Pvap	218.50	kPa	363.15	Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
n0	[1.38380; 1.38790]		[293.15; 298.15]
n0	1.38790		293.15	Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
n0	1.38380		293.15	Vapor Liquid Equilibrium Data for 1-Methyl-2-Pyrrolidone + (1-Butanol or 1-Hexene or Water) Binary Mixtures
n0	1.38490		298.15	Phase equilibria on four binary systems containing 3-methylthiophene
n0	1.38510		298.15	Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
n0	1.38530		298.15	Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
n0	1.38520		298.15	Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
n0	1.38510		298.15	Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol
n0	1.38502		298.15	KDB
ρl	[655.00; 673.23]	kg/m3	[293.00; 313.15]
ρl	673.00	kg/m3	293.00	KDB
ρl	673.23	kg/m3	293.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	670.87	kg/m3	295.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	668.99	kg/m3	297.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	668.73	kg/m3	298.15	Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
ρl	668.73	kg/m3	298.15	Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
ρl	668.03	kg/m3	298.15	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	669.34	kg/m3	298.15	Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
ρl	668.73	kg/m3	298.15	Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
ρl	668.76	kg/m3	298.15	Excess Molar Enthalpies of Dipropyl Ether + Dibutyl Ether + (1-Hexene or Tetrahydrofuran) at 298.15 K
ρl	665.00	kg/m3	301.35	Isothermal vapour-liquid equilibrium data for binary systems of (CHF3 or C2F6) with (1-hexene or 3-methylpentane)
ρl	655.00	kg/m3	313.15	Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
ΔfusS	[70.07; 70.07]	J/mol×K	[133.39; 133.39]
ΔfusS	70.07	J/mol×K	133.39	NIST
ΔfusS	70.07	J/mol×K	133.39	NIST
γ	0.02	N/m	298.20	KDB
λliquid	[0.11; 0.13]	W/m×K	[259.93; 329.89]
λliquid	0.13	W/m×K	259.93	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	260.19	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	260.47	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	275.98	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	276.28	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	276.60	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	295.84	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	296.26	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	296.53	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	301.27	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	301.73	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	301.96	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	314.67	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	315.04	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	315.38	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	329.14	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	329.53	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	329.89	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
273.15	100.00	691.9
273.15	1000.00	692.7
273.15	2000.00	693.6
273.15	5000.00	696.4
273.15	10000.00	700.6
273.15	15000.00	704.6
273.15	20000.00	708.5
273.15	30000.00	715.6
273.15	40000.00	722.2
273.15	50000.00	728.2
273.15	60000.00	733.9
273.15	70000.00	739.4
293.15	100.00	673.3
293.15	1000.00	674.3
293.15	2000.00	675.4
293.15	5000.00	678.6
293.15	10000.00	683.5
293.15	15000.00	688.1
293.15	20000.00	692.4
293.15	30000.00	700.4
293.15	40000.00	707.6
293.15	50000.00	714.3
293.15	60000.00	720.5
293.15	70000.00	726.4
313.15	100.00	654.2
313.15	1000.00	655.3
313.15	2000.00	656.6
313.15	5000.00	660.3
313.15	10000.00	666.0
313.15	15000.00	671.2
313.15	20000.00	676.1
313.15	30000.00	685.1
313.15	40000.00	693.1
313.15	50000.00	700.4
313.15	60000.00	707.4
313.15	70000.00	713.5
333.15	100.00	634.7
333.15	1000.00	636.0
333.15	2000.00	637.5
333.15	5000.00	641.9
333.15	10000.00	648.5
333.15	15000.00	654.5
333.15	20000.00	660.1
333.15	30000.00	670.1
333.15	40000.00	679.0
333.15	50000.00	687.0
333.15	60000.00	694.4
333.15	70000.00	701.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.59	100.00	682.2
283.58	500.00	682.3
283.57	1000.00	683.2
283.57	3000.00	685.2
283.57	5000.00	687.2
283.57	10000.00	691.9
283.57	15000.00	696.4
283.57	20000.00	700.6
283.57	25000.00	704.7
283.57	30000.00	708.5
283.57	35000.00	712.4
283.58	40000.00	714.7
283.57	45000.00	719.4
283.58	50000.00	722.4
283.58	55000.00	725.5
283.58	60000.00	728.6
283.58	70000.00	734.4
283.58	80000.00	739.9
283.59	90000.00	745.2
283.59	100000.00	750.1
293.51	100.00	673.1
293.51	500.00	673.5
293.50	1000.00	674.1
293.51	3000.00	676.3
293.51	5000.00	678.4
293.51	10000.00	683.5
293.52	15000.00	688.3
293.51	20000.00	692.8
293.51	25000.00	697.0
293.51	30000.00	701.1
293.51	35000.00	704.9
293.52	40000.00	708.6
293.52	45000.00	712.5
293.52	50000.00	715.6
293.51	55000.00	718.9
293.51	60000.00	722.1
293.51	70000.00	728.2
293.51	80000.00	733.8
293.51	90000.00	739.3
293.51	100000.00	744.4
303.41	100.00	663.5
303.40	500.00	664.1
303.40	1000.00	664.6
303.41	3000.00	667.0
303.41	5000.00	669.3
303.41	10000.00	674.8
303.41	15000.00	679.9
303.41	20000.00	684.7
303.41	25000.00	689.2
303.42	30000.00	693.5
303.42	35000.00	698.2
303.42	40000.00	701.5
303.42	45000.00	705.8
303.42	50000.00	708.8
303.42	55000.00	712.8
303.42	60000.00	715.5
303.42	70000.00	721.8
303.42	80000.00	727.7
303.42	90000.00	733.2
303.42	100000.00	738.5
313.34	100.00	654.1
313.35	500.00	654.2
313.35	1000.00	655.3
313.35	3000.00	657.9
313.35	5000.00	660.3
313.35	10000.00	666.1
313.35	15000.00	671.6
313.34	20000.00	676.6
313.35	25000.00	681.4
313.35	30000.00	685.9
313.35	35000.00	690.2
313.35	40000.00	694.3
313.35	45000.00	698.3
313.35	50000.00	701.9
313.35	55000.00	705.7
313.35	60000.00	709.0
313.36	70000.00	715.9
313.35	80000.00	721.9
313.35	90000.00	727.6
313.35	100000.00	733.2
323.18	100.00	644.5
323.19	500.00	644.9
323.19	1000.00	645.8
323.19	3000.00	648.6
323.19	5000.00	651.3
323.19	10000.00	657.6
323.20	15000.00	663.4
323.20	20000.00	668.8
323.21	25000.00	673.8
323.20	30000.00	678.6
323.20	35000.00	683.4
323.20	40000.00	687.3
323.21	45000.00	691.8
323.19	50000.00	695.2
323.19	55000.00	699.3
323.18	60000.00	702.5
323.20	70000.00	709.4
323.20	80000.00	715.7
323.20	90000.00	721.6
323.20	100000.00	727.2
333.08	500.00	635.3
333.08	1000.00	636.0
333.08	3000.00	639.1
333.08	5000.00	642.0
333.08	10000.00	648.8
333.09	15000.00	655.0
333.09	20000.00	660.8
333.09	25000.00	666.1
333.09	30000.00	671.1
333.09	35000.00	676.4
333.09	40000.00	680.2
333.09	45000.00	685.1
333.09	50000.00	688.5
333.09	55000.00	693.0
333.09	60000.00	696.1
333.09	70000.00	703.3
333.09	80000.00	709.8
333.09	90000.00	715.9
333.09	100000.00	721.7
342.96	500.00	625.6
342.96	1000.00	626.4
342.97	3000.00	629.8
342.97	5000.00	633.0
342.97	10000.00	640.3
342.97	15000.00	647.0
342.97	20000.00	653.2
342.97	25000.00	658.8
342.97	30000.00	664.1
342.97	35000.00	669.6
342.97	40000.00	673.8
342.97	45000.00	678.8
342.97	50000.00	682.3
342.97	55000.00	687.0
342.97	60000.00	690.4
342.97	70000.00	697.6
342.97	80000.00	704.3
342.97	90000.00	710.7
342.97	100000.00	716.6
352.85	500.00	615.7
352.85	1000.00	617.0
352.85	3000.00	620.7
352.85	5000.00	624.2
352.86	10000.00	632.2
352.85	15000.00	639.4
352.86	20000.00	645.7
352.86	25000.00	651.7
352.86	30000.00	657.4
352.86	35000.00	662.8
352.86	40000.00	667.4
352.86	45000.00	672.4
352.86	50000.00	676.6
352.86	55000.00	680.9
352.86	60000.00	684.8
352.86	70000.00	692.4
352.86	80000.00	699.4
352.86	90000.00	705.9
352.86	100000.00	712.0
362.70	500.00	604.1
362.70	1000.00	605.5
362.71	3000.00	609.5
362.71	5000.00	613.3
362.71	10000.00	622.0
362.71	15000.00	629.7
362.71	20000.00	636.7
362.71	25000.00	643.0
362.71	30000.00	648.9
362.71	35000.00	654.7
362.71	40000.00	659.6
362.71	45000.00	664.8
362.71	50000.00	669.0
362.71	55000.00	673.7
362.71	60000.00	677.6
362.71	70000.00	685.4
362.71	80000.00	692.6
362.71	90000.00	699.3
362.70	100000.00	705.7
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
98.00	298.15	669.71
98.00	303.15	664.87
98.00	312.92	655.77
98.00	325.17	644.12
24510.00	298.15	696.93
24510.00	303.15	690.93
24510.00	326.00	675.1
24510.00	364.73	645.55
24510.00	398.43	618.11
24510.00	423.18	598.39
24510.00	452.77	575.45
24510.00	471.92	560.56
49030.00	298.15	714.95
49030.00	303.15	711.55
49030.00	326.02	694.93
49030.00	364.69	670.17
49030.00	398.87	645.8
49030.00	423.10	630.04
49030.00	453.14	608.12
49030.00	471.73	598.79
98060.00	298.15	744.22
98060.00	303.15	741.4
98060.00	325.99	729.28
98060.00	364.75	706.69
98060.00	398.78	687.13
98060.00	422.90	672.81
98060.00	453.19	656.91
98060.00	471.78	646.27
147100.00	298.15	763.36
147100.00	303.15	761.37
147100.00	326.05	750.05
147100.00	364.83	731.74
147100.00	398.25	715.97
147100.00	422.74	703.54
147100.00	453.28	687.84
147100.00	472.02	680.82
196130.00	298.15	778.91
196130.00	303.15	776.19
196130.00	326.12	767.98
196130.00	364.63	751.74
196130.00	398.37	736.05
196130.00	422.71	726.21
196130.00	453.14	712.63
196130.00	471.55	704.21
245160.00	298.15	793.17
245160.00	303.15	791.19
245160.00	326.15	783.2
245160.00	364.25	767.68
245160.00	398.35	753.74
245160.00	422.37	743.17
245160.00	453.52	732.58
245160.00	471.64	725.42
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[98.97; 348.25]	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			7.90630e+01
Coefficient B			-5.88630e+02
Coefficient C			5.91424e+00
Coefficient D			1.08370e-04
Coefficient E			-3.95490e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	98.97	J/mol×K	200.00	Calculated Property
Cp,gas	148.33	J/mol×K	344.44	Calculated Property
Cp,gas	195.08	J/mol×K	488.89	Calculated Property
Cp,gas	233.16	J/mol×K	633.33	Calculated Property
Cp,gas	263.59	J/mol×K	777.78	Calculated Property
Cp,gas	288.05	J/mol×K	922.22	Calculated Property
Cp,gas	307.90	J/mol×K	1066.67	Calculated Property
Cp,gas	324.11	J/mol×K	1211.11	Calculated Property
Cp,gas	337.39	J/mol×K	1355.56	Calculated Property
Cp,gas	348.25	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[154.15; 226.91]	J/mol×K	[133.39; 404.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.20740e+02
Coefficient B			1.97350e+02
Coefficient C			5.59345e-01
Coefficient D			1.20380e-02
Coefficient E			-7.63520e-06
Temperature range, min.			133.39
Temperature range, max.			404.00
Cp,liquid	154.15	J/mol×K	133.39	Calculated Property
Cp,liquid	154.88	J/mol×K	163.46	Calculated Property
Cp,liquid	158.18	J/mol×K	193.53	Calculated Property
Cp,liquid	163.34	J/mol×K	223.59	Calculated Property
Cp,liquid	170.12	J/mol×K	253.66	Calculated Property
Cp,liquid	178.47	J/mol×K	283.73	Calculated Property
Cp,liquid	188.36	J/mol×K	313.80	Calculated Property
Cp,liquid	199.78	J/mol×K	343.86	Calculated Property
Cp,liquid	212.66	J/mol×K	373.93	Calculated Property
Cp,liquid	226.91	J/mol×K	404.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0071942; 0.0001253]	Pa×s	[133.39; 403.20]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.00270e+01
Coefficient B			7.74410e+02
Coefficient C			-1.45620e-01
Coefficient D			-2.99300e-08
Coefficient E			2.00000e+00
Temperature range, min.			133.39
Temperature range, max.			403.20
η	0.0071942	Pa×s	133.39	Calculated Property
η	0.0024064	Pa×s	163.37	Calculated Property
η	0.0011256	Pa×s	193.35	Calculated Property
η	0.0006436	Pa×s	223.33	Calculated Property
η	0.0004190	Pa×s	253.31	Calculated Property
η	0.0002981	Pa×s	283.28	Calculated Property
η	0.0002261	Pa×s	313.26	Calculated Property
η	0.0001796	Pa×s	343.24	Calculated Property
η	0.0001480	Pa×s	373.22	Calculated Property
η	0.0001253	Pa×s	403.20	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[39.47; 12.05]	kJ/mol	[133.39; 484.49]	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			4.36540e+01
Coefficient B			3.60650e-02
Coefficient C			1.71760e+00
Coefficient D			-2.68050e+00
Coefficient E			1.33490e+00
Critical temperature, Tc (K)			5.04000e+02
Temperature range, min.			133.39
Temperature range, max.			484.49
ΔvapH	39.47	kJ/mol	133.39	Calculated Property
ΔvapH	37.49	kJ/mol	172.40	Calculated Property
ΔvapH	35.44	kJ/mol	211.41	Calculated Property
ΔvapH	33.36	kJ/mol	250.42	Calculated Property
ΔvapH	31.26	kJ/mol	289.43	Calculated Property
ΔvapH	29.04	kJ/mol	328.45	Calculated Property
ΔvapH	26.55	kJ/mol	367.46	Calculated Property
ΔvapH	23.46	kJ/mol	406.47	Calculated Property
ΔvapH	19.18	kJ/mol	445.48	Calculated Property
ΔvapH	12.05	kJ/mol	484.49	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[242.74; 360.58]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42313e+01
Coefficient B			-2.91733e+03
Coefficient C			-3.35220e+01
Temperature range, min.			242.74
Temperature range, max.			360.58
Pvap	1.33	kPa	242.74	Calculated Property
Pvap	3.03	kPa	255.83	Calculated Property
Pvap	6.29	kPa	268.93	Calculated Property
Pvap	12.08	kPa	282.02	Calculated Property
Pvap	21.74	kPa	295.11	Calculated Property
Pvap	36.99	kPa	308.21	Calculated Property
Pvap	59.97	kPa	321.30	Calculated Property
Pvap	93.23	kPa	334.39	Calculated Property
Pvap	139.69	kPa	347.49	Calculated Property
Pvap	202.63	kPa	360.58	Calculated Property
Pvap	[5.98e-07; 3209.68]	kPa	[133.39; 504.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			5.42819e+01
Coefficient B			-5.30203e+03
Coefficient C			-5.91435e+00
Coefficient D			4.38711e-06
Coefficient E			2.00000e+00
Temperature range, min.			133.39
Temperature range, max.			504.00
Pvap	5.98e-07	kPa	133.39	Calculated Property
Pvap	1.52e-03	kPa	174.57	Calculated Property
Pvap	0.15	kPa	215.75	Calculated Property
Pvap	3.06	kPa	256.93	Calculated Property
Pvap	24.27	kPa	298.11	Calculated Property
Pvap	109.71	kPa	339.28	Calculated Property
Pvap	344.40	kPa	380.46	Calculated Property
Pvap	845.48	kPa	421.64	Calculated Property
Pvap	1750.02	kPa	462.82	Calculated Property
Pvap	3209.68	kPa	504.00	Calculated Property
Pvap	[3.00e-07; 3165.89]	kPa	[133.39; 504.03]	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			7.43339e+01
Coefficient B			-6.02031e+03
Coefficient C			-9.06686e+00
Coefficient D			8.22835e-06
Coefficient E			0.00000e+00
Temperature range, min.			133.39
Temperature range, max.			504.03
Pvap	3.00e-07	kPa	133.39	Calculated Property
Pvap	1.22e-03	kPa	174.57	Calculated Property
Pvap	0.15	kPa	215.75	Calculated Property
Pvap	3.11	kPa	256.94	Calculated Property
Pvap	24.84	kPa	298.12	Calculated Property
Pvap	110.65	kPa	339.30	Calculated Property
Pvap	341.07	kPa	380.48	Calculated Property
Pvap	826.71	kPa	421.67	Calculated Property
Pvap	1707.23	kPa	462.85	Calculated Property
Pvap	3165.89	kPa	504.03	Calculated Property
Pvap	[16.64; 104.00]	kPa	[289.04; 337.46]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37939e+01
Coefficient B			-2.65481e+03
Coefficient C			-4.73010e+01
Reference			Forziati, Camin, et al., 1950
Temperature range, min.			289.04
Temperature range, max.			337.46
Pvap	16.64	kPa	289.04	Calculated Property
Pvap	21.13	kPa	294.42	Calculated Property
Pvap	26.57	kPa	299.80	Calculated Property
Pvap	33.09	kPa	305.18	Calculated Property
Pvap	40.83	kPa	310.56	Calculated Property
Pvap	49.97	kPa	315.94	Calculated Property
Pvap	60.67	kPa	321.32	Calculated Property
Pvap	73.12	kPa	326.70	Calculated Property
Pvap	87.49	kPa	332.08	Calculated Property
Pvap	104.00	kPa	337.46	Calculated Property
Pvap	[16.64; 104.00]	kPa	[289.04; 337.46]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37939e+01
Coefficient B			-2.65481e+03
Coefficient C			-4.73010e+01
Reference			Forziati, Camin, et al., 1950, 2
Temperature range, min.			289.04
Temperature range, max.			337.46
Pvap	16.64	kPa	289.04	Calculated Property
Pvap	21.13	kPa	294.42	Calculated Property
Pvap	26.57	kPa	299.80	Calculated Property
Pvap	33.09	kPa	305.18	Calculated Property
Pvap	40.83	kPa	310.56	Calculated Property
Pvap	49.97	kPa	315.94	Calculated Property
Pvap	60.67	kPa	321.32	Calculated Property
Pvap	73.12	kPa	326.70	Calculated Property
Pvap	87.49	kPa	332.08	Calculated Property
Pvap	104.00	kPa	337.46	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[802.13; 254.47]	kg/m3	[133.39; 503.53]	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			3.58418e+01
Coefficient B			2.00730e-01
Coefficient C			5.04000e+02
Coefficient D			2.16590e-01
Temperature range, min.			133.39
Temperature range, max.			503.53
ρl	802.13	kg/m3	133.39	Calculated Property
ρl	772.38	kg/m3	174.52	Calculated Property
ρl	740.84	kg/m3	215.64	Calculated Property
ρl	707.08	kg/m3	256.77	Calculated Property
ρl	670.46	kg/m3	297.90	Calculated Property
ρl	629.99	kg/m3	339.02	Calculated Property
ρl	583.93	kg/m3	380.15	Calculated Property
ρl	528.80	kg/m3	421.28	Calculated Property
ρl	455.05	kg/m3	462.40	Calculated Property
ρl	254.47	kg/m3	503.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[133.15; 336.65]	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			4.85225e-02
Coefficient B			-1.02700e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			133.15
Temperature range, max.			336.65
γ	0.03	N/m	133.15	Calculated Property
γ	0.03	N/m	155.76	Calculated Property
γ	0.03	N/m	178.37	Calculated Property
γ	0.03	N/m	200.98	Calculated Property
γ	0.03	N/m	223.59	Calculated Property
γ	0.02	N/m	246.21	Calculated Property
γ	0.02	N/m	268.82	Calculated Property
γ	0.02	N/m	291.43	Calculated Property
γ	0.02	N/m	314.04	Calculated Property
γ	0.01	N/m	336.65	Calculated Property
γ	[0.04; 7.99e-04]	N/m	[133.39; 484.49]	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			-1.22970e-02
Coefficient B			1.18870e+01
Coefficient C			-2.89450e+00
Coefficient D			-7.74430e-04
Coefficient E			-4.64470e-06
Temperature range, min.			133.39
Temperature range, max.			484.49
γ	0.04	N/m	133.39	Calculated Property
γ	0.03	N/m	172.40	Calculated Property
γ	0.03	N/m	211.41	Calculated Property
γ	0.02	N/m	250.42	Calculated Property
γ	0.02	N/m	289.43	Calculated Property
γ	0.01	N/m	328.45	Calculated Property
γ	0.01	N/m	367.46	Calculated Property
γ	0.01	N/m	406.47	Calculated Property
γ	0.00	N/m	445.48	Calculated Property
γ	7.99e-04	N/m	484.49	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.11]	W/m×K	[133.39; 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			6.42570e-05
Coefficient B			1.13550e+00
Coefficient C			4.45140e+02
Coefficient D			6.48300e+04
Temperature range, min.			133.39
Temperature range, max.			1000.00
λgas	0.00	W/m×K	133.39	Calculated Property
λgas	0.01	W/m×K	229.68	Calculated Property
λgas	0.02	W/m×K	325.97	Calculated Property
λgas	0.03	W/m×K	422.26	Calculated Property
λgas	0.04	W/m×K	518.55	Calculated Property
λgas	0.05	W/m×K	614.84	Calculated Property
λgas	0.06	W/m×K	711.13	Calculated Property
λgas	0.08	W/m×K	807.42	Calculated Property
λgas	0.09	W/m×K	903.71	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.18; 0.09]	W/m×K	[133.15; 383.15]	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			4.90940e-02
Coefficient B			1.83340e+01
Coefficient C			-2.21750e+00
Coefficient D			1.56070e-03
Coefficient E			-1.06950e-05
Temperature range, min.			133.15
Temperature range, max.			383.15
λliquid	0.18	W/m×K	133.15	Calculated Property
λliquid	0.17	W/m×K	160.93	Calculated Property
λliquid	0.16	W/m×K	188.71	Calculated Property
λliquid	0.15	W/m×K	216.48	Calculated Property
λliquid	0.14	W/m×K	244.26	Calculated Property
λliquid	0.13	W/m×K	272.04	Calculated Property
λliquid	0.12	W/m×K	299.82	Calculated Property
λliquid	0.11	W/m×K	327.59	Calculated Property
λliquid	0.10	W/m×K	355.37	Calculated Property
λliquid	0.09	W/m×K	383.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Hexene.

Mixtures

• 1-Hexene + Acetone
• 1-Hexene + Ethanol
• n-Hexane + 1-Hexene + Ethanol
• 1-Hexene + Ethyl Acetate
• Benzene + 1-Hexene
• Benzene + 1-Hexene + 2-Pyrrolidinone, 1-methyl-
• Benzene + 1-Hexene + Cyclohexane
• 1-Hexene + 1-Butanol
• 1-Hexene + Cyclohexane
• 1-Hexene + Acetic acid
• n-Hexane + 1-Hexene
• 1-Hexene + 2-Propanol
• 1-Hexene + Methyl Alcohol
• 1-Hexene + 2-Pyrrolidinone, 1-methyl-
• 1-Hexene + Tetrahydrofuran
• 1-Hexene + Water
• 1-Hexene + 2-Pyrrolidinone, 1-methyl- + Water
• 1-Hexene + Benzene, 1,3-dimethyl-
• 1-Hexene + p-Xylene
• 1-Hexene + 1,2-Ethanediol + TETRAMETHYLAMMONIUM CHLORIDE

Find more mixtures with 1-Hexene.

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 6 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons. J. Chem. Eng. Data 1996, 41, 645-656.
• 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.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• 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
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Study on the separation of 1-hexene and trans-3-hexene using ionic liquids
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Thermodynamics of fuels with a biosynthetic component (III): Vapor liquid equilibrium data for the ternary mixture ethyl 1, 1-dimethylethyl ether, n-heptane and 1-hexene at T = 313.15K
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
• Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Phase equilibria on four binary systems containing 3-methylthiophene
• Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
• Temperature dependence of the excess molar volume of 1-hexanol + 1-alkene systems in terms of an association and equation of state model
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
• Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
• Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4- trimethylpentane and 1-hexene at 313.15 K
• Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
• 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
• Separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [EMIM]-based ionic liquids
• 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
• Vapor-liquid equilibria and excess enthalpies of the binary systems 1- pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Ternary LLE measurements for the separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [DCA]-based ionic liquids
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• 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
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
• The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
• Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Excess molar enthalpies of ternary mixtures (1-hexene + tetrahydrofuran + 2,2-dimethylbutane or 2,3-dimethylbutane) at the temperature 298.15 K
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• 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
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• 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 of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• 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
• Experimental study on vapor-liquid equilibria of ternary systems of hydrocarbons/ionic liquid using headspace gas chromatography
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• 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
• Isothermal (vapor + liquid) equilibria and excess enthalpy data of {1-hexene + methyl butyl ether (MBE)} and {1-hexene + methyl tert-butyl ether (MTBE)} binary systems at several temperatures
• 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 coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Heat capacities and densities of the binary mixtures containing ethanol, cyclohexane or 1-hexene at high pressures
• 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 coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• 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 of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
• 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
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• 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
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• Use of water in aiding olefin/paraffin (liquid + liquid) extraction via complexation with a silver bis(trifluoromethylsulfonyl)imide salt
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• 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
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• 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
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Bis(trifluoromethylsulfonyl)imide, or dicyanamide-based ionic liquids in the liquid liquid extraction of hex-1-ene from hexane and cyclohexene from cyclohexane
• Liquid-liquid separation of hex-1-ene from hexane and cyclohexene from cyclohexane with ionic liquids
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Liquid-liquid separation of hexane/hex-1-ene and cyclohexane/cyclohexene by dicyanamide-based ionic liquids
• 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)
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Measurements of the density and viscosity of 1-hexene + 1-octene mixtures at high temperatures and high pressures
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• Liquid Density of n-Pentene, n-Hexene, and n-Heptene at Temperatures from 283.15 to 363.15 K and Pressures up to 100 MPa
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
• Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
• Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
• Excess Molar Enthalpies of Dipropyl Ether + Dibutyl Ether + (1-Hexene or Tetrahydrofuran) at 298.15 K
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• 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
• Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
• Density, Viscosity, and Isobaric Heat Capacity of the Mixture (1-Butanol + 1-Hexene)
• Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol
• 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
• Experimental Study and Correlation Models of the Density and Viscosity of 1-Hexene and 1-Heptene at Temperatures from (298 to 473) K and Pressures up to 245 MPa
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Vapor Liquid Equilibrium Data for 1-Methyl-2-Pyrrolidone + (1-Butanol or 1-Hexene or Water) Binary Mixtures
• Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
• Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K
• Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
• Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K
• Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and Heptane or 1-Hexene at T ) 313.15 K
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• 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
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• 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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