Chemical Properties of 1-Octene (CAS 111-66-0)

InChI

InChI=1S/C8H16/c1-3-5-7-8-6-4-2/h3H,1,4-8H2,2H3

InChI Key

KWKAKUADMBZCLK-UHFFFAOYSA-N

Formula

C8H16

SMILES

C=CCCCCCC

Molecular Weight¹

112.21

CAS

111-66-0

Other Names

• 1-C8H16
• 1-n-Octene
• NSC 8457
• Neodene 8
• Octene-1
• Octylene
• SHOP C8
• caprylene
• n-1-Octene
• oct-1-ene
• «alpha»-Octene
• «alpha»-Octylene

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• 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_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).
• 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).
• 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.
• D^*_i : Self diffusion coefficient (m²/s).
• 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.

Physical Properties

Property	Value	Unit	Source
ω	[0.3858; 0.3930]
ω	0.3860		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3858		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.3930		ChemSep v8.3 pure component data Compiled value
ω	0.3860		KDB
Tig	529.26	K	KDB
AP	305.650	K	KDB
ΔcH°liquid	-5312.90 ± 1.10	kJ/mol	NIST
μ	[0.30; 0.42]	debye
μ	0.42	debye	ChemSep v8.3 pure component data Compiled value
μ	0.30	debye	KDB
LFL	0.90	% in Air	KDB
Tflash,cc	294.26	K	KDB
ΔfG°	[104.30; 105.70]	kJ/mol
ΔfG°	105.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	104.30	kJ/mol	KDB
Δc,grossH	5312.93	kJ/mol	KDB
Δc,netH	4960.844	kJ/mol	KDB
ΔfH°gas	[-82.98; -81.94]	kJ/mol
ΔfH°gas	-81.94	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-82.98	kJ/mol	KDB
ΔfH°gas	-82.93	kJ/mol	NIST
ΔfH°gas	-82.93	kJ/mol	NIST
ΔfH°liquid	-121.80 ± 1.20	kJ/mol	NIST
ΔfusH°	15.20	kJ/mol	Joback Calculated Property
ΔvapH°	[38.00; 40.60]	kJ/mol
ΔvapH°	40.44	kJ/mol	NIST
ΔvapH°	40.60	kJ/mol	NIST
ΔvapH°	40.27 ± 0.20	kJ/mol	NIST
ΔvapH°	40.30 ± 0.20	kJ/mol	NIST
ΔvapH°	38.00	kJ/mol	NIST
IE	[9.43; 9.60]	eV
IE	9.43 ± 0.01	eV	NIST
IE	9.43 ± 0.01	eV	NIST
IE	9.43 ± 0.01	eV	NIST
IE	9.60 ± 0.01	eV	NIST
log10WS	[-4.44; -4.44]
log10WS	-4.44		Aq. Solubility Prediction
log10WS	-4.44		Estimated Solubility
logPoct/wat	3.143		Crippen Calculated Property
McVol	119.280	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[2620.01; 2680.00]	kPa
Pc	2680.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	2624.32	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2620.01	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2680.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2680.00	kPa	KDB
Pc	2680.00 ± 80.00	kPa	NIST
Ptriple	2.98e-06	kPa	ChemSep v8.3 pure component data Compiled value
ρc	235.65 ± 8.98	kg/m3	NIST
Inp	[779.00; 799.00]
Inp	786.00		NIST
Inp	788.30		NIST
Inp	780.40		NIST
Inp	784.90		NIST
Inp	783.00		NIST
Inp	789.00		NIST
Inp	788.00		NIST
Inp	780.00		NIST
Inp	785.30		NIST
Inp	786.00		NIST
Inp	788.00		NIST
Inp	789.00		NIST
Inp	788.00		NIST
Inp	789.00		NIST
Inp	789.00		NIST
Inp	789.00		NIST
Inp	788.30		NIST
Inp	789.00		NIST
Inp	781.00		NIST
Inp	781.80		NIST
Inp	789.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	790.00		NIST
Inp	792.50		NIST
Inp	792.60		NIST
Inp	792.70		NIST
Inp	792.80		NIST
Inp	792.90		NIST
Inp	793.00		NIST
Inp	790.00		NIST
Inp	789.00		NIST
Inp	789.00		NIST
Inp	788.40		NIST
Inp	788.60		NIST
Inp	788.80		NIST
Inp	789.00		NIST
Inp	786.70		NIST
Inp	789.40		NIST
Inp	788.10		NIST
Inp	787.70		NIST
Inp	787.60		NIST
Inp	787.30		NIST
Inp	787.00		NIST
Inp	786.60		NIST
Inp	790.00		NIST
Inp	781.60		NIST
Inp	782.00		NIST
Inp	781.00		NIST
Inp	782.60		NIST
Inp	784.00		NIST
Inp	783.70		NIST
Inp	782.00		NIST
Inp	782.00		NIST
Inp	784.00		NIST
Inp	784.00		NIST
Inp	781.00		NIST
Inp	782.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	782.67		NIST
Inp	782.67		NIST
Inp	782.70		NIST
Inp	783.00		NIST
Inp	783.00		NIST
Inp	782.00		NIST
Inp	789.20		NIST
Inp	781.40		NIST
Inp	781.00		NIST
Inp	782.90		NIST
Inp	782.30		NIST
Inp	783.00		NIST
Inp	786.00		NIST
Inp	790.00		NIST
Inp	782.00		NIST
Inp	783.00		NIST
Inp	Outlier 779.00		NIST
Inp	785.00		NIST
Inp	790.00		NIST
Inp	790.00		NIST
Inp	791.00		NIST
Inp	795.00		NIST
Inp	786.00		NIST
Inp	Outlier 796.00		NIST
Inp	787.72		NIST
Inp	790.00		NIST
Inp	792.90		NIST
Inp	789.00		NIST
Inp	794.00		NIST
Inp	792.00		NIST
Inp	785.00		NIST
Inp	782.40		NIST
Inp	789.30		NIST
Inp	788.40		NIST
Inp	788.30		NIST
Inp	789.30		NIST
Inp	789.10		NIST
Inp	789.60		NIST
Inp	788.40		NIST
Inp	785.00		NIST
Inp	789.70		NIST
Inp	788.30		NIST
Inp	789.30		NIST
Inp	789.10		NIST
Inp	789.30		NIST
Inp	788.40		NIST
Inp	787.00		NIST
Inp	787.00		NIST
Inp	789.04		NIST
Inp	788.99		NIST
Inp	789.05		NIST
Inp	791.72		NIST
Inp	791.76		NIST
Inp	791.77		NIST
Inp	786.00		NIST
Inp	Outlier 799.00		NIST
Inp	789.00		NIST
Inp	792.00		NIST
Inp	782.00		NIST
Inp	782.00		NIST
Inp	782.00		NIST
Inp	787.00		NIST
Inp	792.00		NIST
Inp	787.00		NIST
Inp	789.00		NIST
Inp	792.00		NIST
Inp	Outlier 796.00		NIST
Inp	790.00		NIST
Inp	791.00		NIST
Inp	793.00		NIST
Inp	792.00		NIST
Inp	794.00		NIST
Inp	786.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	790.00		NIST
Inp	794.00		NIST
Inp	Outlier 799.00		NIST
Inp	783.00		NIST
Inp	785.00		NIST
Inp	Outlier 799.00		NIST
Inp	788.20		NIST
Inp	788.04		NIST
Inp	792.00		NIST
Inp	788.00		NIST
Inp	789.00		NIST
Inp	792.00		NIST
Inp	791.00		NIST
Inp	791.00		NIST
Inp	792.00		NIST
Inp	789.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	Outlier 779.00		NIST
Inp	792.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	783.00		NIST
Inp	792.00		NIST
Inp	793.00		NIST
Inp	788.00		NIST
Inp	790.00		NIST
Inp	790.00		NIST
Inp	789.00		NIST
Inp	788.00		NIST
Inp	784.00		NIST
Inp	792.00		NIST
Inp	792.00		NIST
Inp	Outlier 797.00		NIST
Inp	783.00		NIST
Inp	790.00		NIST
Inp	784.90		NIST
Inp	783.00		NIST
Inp	788.00		NIST
Inp	787.00		NIST
Inp	790.00		NIST
Inp	788.00		NIST
Inp	788.00		NIST
Inp	795.00		NIST
Inp	790.00		NIST
Inp	790.00		NIST
Inp	786.00		NIST
Inp	785.00		NIST
Inp	785.00		NIST
Inp	786.00		NIST
Inp	782.00		NIST
Ip	[822.00; 892.00]
Ip	851.00		NIST
Ip	852.00		NIST
Ip	847.00		NIST
Ip	847.00		NIST
Ip	850.00		NIST
Ip	848.50		NIST
Ip	847.40		NIST
Ip	847.20		NIST
Ip	849.90		NIST
Ip	847.20		NIST
Ip	848.50		NIST
Ip	847.40		NIST
Ip	849.90		NIST
Ip	842.00		NIST
Ip	837.00		NIST
Ip	833.00		NIST
Ip	836.00		NIST
Ip	837.00		NIST
Ip	Outlier 892.00		NIST
Ip	850.00		NIST
Ip	822.00		NIST
Ip	830.00		NIST
Ip	830.00		NIST
Ip	831.00		NIST
Ip	830.00		NIST
Ip	851.00		NIST
Ip	848.50		NIST
Ip	836.00		NIST
S°liquid	360.45	J/mol×K	NIST
Tboil	[392.15; 398.75]	K
Tboil	394.44	K	ChemSep v8.3 pure component data Compiled value
Tboil	394.44	K	KDB
Tboil	395.70	K	NIST
Tboil	395.50 ± 0.50	K	NIST
Tboil	394.50	K	NIST
Tboil	394.40	K	NIST
Tboil	394.80 ± 1.50	K	NIST
Tboil	394.70 ± 0.50	K	NIST
Tboil	394.70 ± 0.30	K	NIST
Tboil	394.43 ± 0.20	K	NIST
Tboil	394.45 ± 0.50	K	NIST
Tboil	395.15 ± 1.00	K	NIST
Tboil	Outlier 392.15 ± 3.00	K	NIST
Tboil	396.65 ± 3.00	K	NIST
Tboil	394.15 ± 2.00	K	NIST
Tboil	395.65 ± 1.00	K	NIST
Tboil	394.41 ± 0.20	K	NIST
Tboil	394.15 ± 2.00	K	NIST
Tboil	394.15 ± 1.00	K	NIST
Tboil	393.35 ± 1.00	K	NIST
Tboil	393.15 ± 2.00	K	NIST
Tboil	394.40 ± 0.20	K	NIST
Tboil	394.00 ± 2.00	K	NIST
Tboil	394.15 ± 3.00	K	NIST
Tboil	394.43 ± 0.10	K	NIST
Tboil	394.42 ± 0.30	K	NIST
Tboil	394.40 ± 0.30	K	NIST
Tboil	395.15 ± 2.00	K	NIST
Tboil	393.65 ± 2.00	K	NIST
Tboil	394.05 ± 0.60	K	NIST
Tboil	394.40 ± 0.30	K	NIST
Tboil	393.65 ± 2.00	K	NIST
Tboil	394.40 ± 1.00	K	NIST
Tboil	394.42 ± 0.30	K	NIST
Tboil	394.42 ± 0.15	K	NIST
Tboil	394.75 ± 0.50	K	NIST
Tboil	394.42 ± 0.20	K	NIST
Tboil	394.75 ± 0.60	K	NIST
Tboil	394.42 ± 0.30	K	NIST
Tboil	394.75 ± 0.30	K	NIST
Tboil	394.75 ± 0.30	K	NIST
Tboil	Outlier 392.15 ± 3.00	K	NIST
Tboil	394.25 ± 0.50	K	NIST
Tboil	396.20 ± 1.00	K	NIST
Tboil	394.65 ± 1.00	K	NIST
Tboil	396.15 ± 2.00	K	NIST
Tboil	Outlier 398.75 ± 1.00	K	NIST
Tboil	396.35 ± 1.00	K	NIST
Tboil	393.60 ± 0.50	K	NIST
Tboil	393.40 ± 1.00	K	NIST
Tboil	394.15 ± 1.00	K	NIST
Tboil	395.15 ± 0.70	K	NIST
Tboil	395.20 ± 1.00	K	NIST
Tboil	394.65 ± 1.00	K	NIST
Tboil	395.15 ± 2.00	K	NIST
Tboil	396.15 ± 2.00	K	NIST
Tboil	395.65 ± 1.00	K	NIST
Tboil	395.65 ± 2.00	K	NIST
Tboil	395.15 ± 2.00	K	NIST
Tboil	396.65 ± 2.00	K	NIST
Tboil	396.65 ± 2.00	K	NIST
Tboil	394.90 ± 2.50	K	NIST
Tboil	395.65 ± 3.00	K	NIST
Tc	[566.55; 567.00]	K
Tc	567.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	566.60	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	566.65	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	567.00	K	ChemSep v8.3 pure component data Compiled value
Tc	567.00	K	KDB
Tc	567.00 ± 0.80	K	NIST
Tc	566.60	K	NIST
Tc	566.55 ± 0.05	K	NIST
Tfus	[167.15; 171.45]	K
Tfus	171.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	171.45	K	ChemSep v8.3 pure component data Compiled value
Tfus	171.40	K	KDB
Tfus	171.25	K	Aq. Solubility Prediction
Tfus	171.31 ± 0.20	K	NIST
Tfus	171.43 ± 0.05	K	NIST
Tfus	171.44 ± 0.03	K	NIST
Tfus	171.20 ± 1.00	K	NIST
Tfus	171.44 ± 0.03	K	NIST
Tfus	171.40 ± 0.06	K	NIST
Tfus	171.09 ± 0.10	K	NIST
Tfus	171.05 ± 0.40	K	NIST
Tfus	Outlier 167.15 ± 1.50	K	NIST
Tfus	171.04 ± 0.30	K	NIST
Ttriple	[171.45; 171.47]	K
Ttriple	171.47	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	171.45	K	ChemSep v8.3 pure component data Compiled value
Ttriple	171.46 ± 0.05	K	NIST
Ttriple	171.46 ± 0.05	K	NIST
UQi	4.72		ChemSep v8.3 pure component data Compiled value
URi	5.62		ChemSep v8.3 pure component data Compiled value
Vc	[0.464; 0.468]	m3/kmol
Vc	0.468	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.464	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.468	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.468	m3/kmol	KDB
Vc	0.468	m3/kmol	NIST
VCOSTALD	0.47	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.39		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2660000; 0.2660490]
Zc	0.2660000		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	0.2660490		KDB
Zra	[0.26; 0.27]
Zra	0.26		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	241.21	J/mol×K	298.15	NIST
Csat	[212.40; 245.90]	J/mol×K	[180.00; 310.00]
Csat	212.40	J/mol×K	180.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	212.50	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	213.20	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	214.40	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	216.20	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	218.40	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	221.00	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	223.90	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	227.10	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	230.60	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	231.80	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
Csat	234.30	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	238.10	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	241.30	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	242.00	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	245.90	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
ΔfusH	[15.31; 15.31]	kJ/mol	[171.46; 171.50]
ΔfusH	15.31	kJ/mol	171.46	NIST
ΔfusH	15.31	kJ/mol	171.46	NIST
ΔfusH	15.31	kJ/mol	171.50	NIST
ΔfusH	15.31	kJ/mol	171.50	NIST
ΔvapH	[33.77; 41.20]	kJ/mol	[275.50; 395.20]
ΔvapH	41.20	kJ/mol	275.50	NIST
ΔvapH	40.20	kJ/mol	277.00	NIST
ΔvapH	39.50 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	38.60 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	37.60 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	38.80	kJ/mol	356.00	NIST
ΔvapH	36.60 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	35.80 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	34.07	kJ/mol	394.40	NIST
ΔvapH	33.77	kJ/mol	395.20	KDB
Pvap	[8.30; 165.90]	kPa	[323.15; 413.15]
Pvap	8.30	kPa	323.15	Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
Pvap	10.12	kPa	328.15	Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Pvap	38.51	kPa	363.15	Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
Pvap	39.20	kPa	363.15	Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Pvap	53.82	kPa	373.10	Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
Pvap	165.90	kPa	413.15	Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
n0	1.40620		298.15	KDB
ρl	[710.88; 715.00]	kg/m3	[293.00; 298.15]
ρl	715.00	kg/m3	293.00	KDB
ρl	710.88	kg/m3	298.15	Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
D*i	[2.28e-07; 3.44e-07]	m2/s	[298.15; 323.15]
D*i	2.28e-07	m2/s	298.15	Viscosity and Diffusivity for the Ionic Liquid 1-Hexyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)amide with 1-Octene
D*i	3.44e-07	m2/s	323.15	Viscosity and Diffusivity for the Ionic Liquid 1-Hexyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)amide with 1-Octene
ΔfusS	[89.31; 89.31]	J/mol×K	[171.46; 171.46]
ΔfusS	89.31	J/mol×K	171.46	NIST
ΔfusS	89.31	J/mol×K	171.46	NIST
γ	[0.02; 0.02]	N/m	[283.10; 348.15]
γ	0.02	N/m	283.10	Phase Equilibrium, Volumetric, and Interfacial Properties of the Ionic Liquid, 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide and 1-Octene
γ	0.02	N/m	298.15	Phase Equilibrium, Volumetric, and Interfacial Properties of the Ionic Liquid, 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide and 1-Octene
γ	0.02	N/m	298.20	KDB
γ	0.02	N/m	323.15	Phase Equilibrium, Volumetric, and Interfacial Properties of the Ionic Liquid, 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide and 1-Octene
γ	0.02	N/m	348.15	Phase Equilibrium, Volumetric, and Interfacial Properties of the Ionic Liquid, 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide and 1-Octene
λliquid	[0.12; 0.14]	W/m×K	[259.69; 326.87]
λliquid	0.14	W/m×K	259.69	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.14	W/m×K	259.90	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.14	W/m×K	260.06	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	279.34	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	279.57	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	279.72	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	296.88	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	297.14	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	297.28	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	315.82	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	316.07	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	316.24	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	326.44	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	326.70	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	326.87	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Datasets

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
254.47	100.00	0.1381
254.41	5000.00	0.1402
254.47	10000.00	0.1426
254.35	20000.00	0.1464
254.35	30000.00	0.1500
274.46	100.00	0.1302
274.44	5000.00	0.1324
274.50	10000.00	0.1349
274.59	20000.00	0.1394
274.44	30000.00	0.1439
294.91	100.00	0.1254
294.90	5200.00	0.1277
294.85	10100.00	0.1300
294.79	20000.00	0.1341
294.76	30000.00	0.1379
314.65	100.00	0.1200
314.61	5000.00	0.1228
314.59	10000.00	0.1249
314.61	20000.00	0.1291
314.51	30000.00	0.1331
334.94	100.00	0.1140
334.82	5100.00	0.1167
334.82	10000.00	0.1191
334.69	20000.00	0.1238
334.71	30000.00	0.1282
355.05	100.00	0.1078
354.89	5100.00	0.1106
354.72	10000.00	0.1137
354.74	20000.00	0.1186
354.64	30000.00	0.1234
374.48	600.00	0.1023
375.03	5100.00	0.1047
374.83	10000.00	0.1077
374.86	20100.00	0.1135
374.80	30000.00	0.1179
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[133.27; 468.42]	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			1.06430e+02
Coefficient B			-5.93770e+02
Coefficient C			6.24624e+00
Coefficient D			6.68900e-05
Coefficient E			-2.62740e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	133.27	J/mol×K	200.00	Calculated Property
Cp,gas	200.34	J/mol×K	344.44	Calculated Property
Cp,gas	263.73	J/mol×K	488.89	Calculated Property
Cp,gas	315.05	J/mol×K	633.33	Calculated Property
Cp,gas	355.80	J/mol×K	777.78	Calculated Property
Cp,gas	388.38	J/mol×K	922.22	Calculated Property
Cp,gas	414.72	J/mol×K	1066.67	Calculated Property
Cp,gas	436.22	J/mol×K	1211.11	Calculated Property
Cp,gas	453.88	J/mol×K	1355.56	Calculated Property
Cp,gas	468.42	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[212.42; 316.66]	J/mol×K	[171.00; 454.00]	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			-2.42530e+01
Coefficient B			8.78340e+01
Coefficient C			4.44224e+00
Coefficient D			3.20020e-03
Coefficient E			-1.24670e-06
Temperature range, min.			171.00
Temperature range, max.			454.00
Cp,liquid	212.42	J/mol×K	171.00	Calculated Property
Cp,liquid	213.89	J/mol×K	202.44	Calculated Property
Cp,liquid	219.97	J/mol×K	233.89	Calculated Property
Cp,liquid	229.06	J/mol×K	265.33	Calculated Property
Cp,liquid	240.33	J/mol×K	296.78	Calculated Property
Cp,liquid	253.27	J/mol×K	328.22	Calculated Property
Cp,liquid	267.58	J/mol×K	359.67	Calculated Property
Cp,liquid	283.02	J/mol×K	391.11	Calculated Property
Cp,liquid	299.43	J/mol×K	422.56	Calculated Property
Cp,liquid	316.66	J/mol×K	454.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0065983; 0.0001530]	Pa×s	[171.45; 453.52]	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			-5.80420e+00
Coefficient B			9.45320e+02
Coefficient C			-9.38270e-01
Coefficient D			3.27670e-06
Coefficient E			2.00000e+00
Temperature range, min.			171.45
Temperature range, max.			453.52
η	0.0065983	Pa×s	171.45	Calculated Property
η	0.0024983	Pa×s	202.79	Calculated Property
η	0.0012234	Pa×s	234.13	Calculated Property
η	0.0007106	Pa×s	265.47	Calculated Property
η	0.0004655	Pa×s	296.81	Calculated Property
η	0.0003333	Pa×s	328.16	Calculated Property
η	0.0002554	Pa×s	359.50	Calculated Property
η	0.0002066	Pa×s	390.84	Calculated Property
η	0.0001746	Pa×s	422.18	Calculated Property
η	0.0001530	Pa×s	453.52	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[48.76; 3.00]	kJ/mol	[171.45; 566.90]	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			5.70620e+01
Coefficient B			3.45300e-01
Coefficient C			4.16280e-01
Coefficient D			-3.61250e-01
Coefficient E			-5.95390e-02
Critical temperature, Tc (K)			5.67000e+02
Temperature range, min.			171.45
Temperature range, max.			566.90
ΔvapH	48.76	kJ/mol	171.45	Calculated Property
ΔvapH	46.06	kJ/mol	215.39	Calculated Property
ΔvapH	43.22	kJ/mol	259.33	Calculated Property
ΔvapH	40.27	kJ/mol	303.27	Calculated Property
ΔvapH	37.21	kJ/mol	347.21	Calculated Property
ΔvapH	34.05	kJ/mol	391.14	Calculated Property
ΔvapH	30.70	kJ/mol	435.08	Calculated Property
ΔvapH	26.92	kJ/mol	479.02	Calculated Property
ΔvapH	21.88	kJ/mol	522.96	Calculated Property
ΔvapH	3.00	kJ/mol	566.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[287.65; 421.80]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42819e+01
Coefficient B			-3.35220e+03
Coefficient C			-4.81090e+01
Temperature range, min.			287.65
Temperature range, max.			421.80
Pvap	1.33	kPa	287.65	Calculated Property
Pvap	3.03	kPa	302.56	Calculated Property
Pvap	6.27	kPa	317.46	Calculated Property
Pvap	12.05	kPa	332.37	Calculated Property
Pvap	21.69	kPa	347.27	Calculated Property
Pvap	36.91	kPa	362.18	Calculated Property
Pvap	59.86	kPa	377.08	Calculated Property
Pvap	93.10	kPa	391.99	Calculated Property
Pvap	139.59	kPa	406.89	Calculated Property
Pvap	202.63	kPa	421.80	Calculated Property
Pvap	[3.30e-07; 2692.30]	kPa	[171.45; 566.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.70808e+02
Coefficient B			-1.11373e+04
Coefficient C			-2.35892e+01
Coefficient D			1.95920e-05
Coefficient E			2.00000e+00
Temperature range, min.			171.45
Temperature range, max.			566.90
Pvap	3.30e-07	kPa	171.45	Calculated Property
Pvap	1.20e-03	kPa	215.39	Calculated Property
Pvap	0.14	kPa	259.33	Calculated Property
Pvap	2.95	kPa	303.27	Calculated Property
Pvap	22.15	kPa	347.21	Calculated Property
Pvap	92.36	kPa	391.14	Calculated Property
Pvap	270.74	kPa	435.08	Calculated Property
Pvap	643.27	kPa	479.02	Calculated Property
Pvap	1356.12	kPa	522.96	Calculated Property
Pvap	2692.30	kPa	566.90	Calculated Property
Pvap	[2.43e-06; 2579.57]	kPa	[171.45; 566.60]	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			9.67823e+01
Coefficient B			-8.07486e+03
Coefficient C			-1.22214e+01
Coefficient D			8.73474e-06
Coefficient E			0.00000e+00
Temperature range, min.			171.45
Temperature range, max.			566.60
Pvap	2.43e-06	kPa	171.45	Calculated Property
Pvap	2.57e-03	kPa	215.36	Calculated Property
Pvap	0.18	kPa	259.26	Calculated Property
Pvap	3.04	kPa	303.17	Calculated Property
Pvap	21.74	kPa	347.07	Calculated Property
Pvap	91.75	kPa	390.98	Calculated Property
Pvap	275.95	kPa	434.88	Calculated Property
Pvap	663.70	kPa	478.79	Calculated Property
Pvap	1375.08	kPa	522.69	Calculated Property
Pvap	2579.57	kPa	566.60	Calculated Property
Pvap	[6.37; 104.01]	kPa	[318.04; 395.37]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39480e+01
Coefficient B			-3.11652e+03
Coefficient C			-6.03860e+01
Reference			Forziati, Camin, et al., 1950, 2
Temperature range, min.			318.04
Temperature range, max.			395.37
Pvap	6.37	kPa	318.04	Calculated Property
Pvap	9.42	kPa	326.63	Calculated Property
Pvap	13.58	kPa	335.22	Calculated Property
Pvap	19.15	kPa	343.82	Calculated Property
Pvap	26.46	kPa	352.41	Calculated Property
Pvap	35.90	kPa	361.00	Calculated Property
Pvap	47.89	kPa	369.59	Calculated Property
Pvap	62.89	kPa	378.19	Calculated Property
Pvap	81.42	kPa	386.78	Calculated Property
Pvap	104.01	kPa	395.37	Calculated Property
Pvap	[6.37; 104.01]	kPa	[318.04; 395.37]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39480e+01
Coefficient B			-3.11652e+03
Coefficient C			-6.03860e+01
Reference			Forziati, Camin, et al., 1950
Temperature range, min.			318.04
Temperature range, max.			395.37
Pvap	6.37	kPa	318.04	Calculated Property
Pvap	9.42	kPa	326.63	Calculated Property
Pvap	13.58	kPa	335.22	Calculated Property
Pvap	19.15	kPa	343.82	Calculated Property
Pvap	26.46	kPa	352.41	Calculated Property
Pvap	35.90	kPa	361.00	Calculated Property
Pvap	47.89	kPa	369.59	Calculated Property
Pvap	62.89	kPa	378.19	Calculated Property
Pvap	81.42	kPa	386.78	Calculated Property
Pvap	104.01	kPa	395.37	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[804.53; 253.13]	kg/m3	[171.45; 566.90]	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			5.01411e+01
Coefficient B			2.34630e-01
Coefficient C			5.67000e+02
Coefficient D			2.48460e-01
Temperature range, min.			171.45
Temperature range, max.			566.90
ρl	804.53	kg/m3	171.45	Calculated Property
ρl	774.36	kg/m3	215.39	Calculated Property
ρl	742.51	kg/m3	259.33	Calculated Property
ρl	708.57	kg/m3	303.27	Calculated Property
ρl	671.95	kg/m3	347.21	Calculated Property
ρl	631.71	kg/m3	391.14	Calculated Property
ρl	586.23	kg/m3	435.08	Calculated Property
ρl	532.24	kg/m3	479.02	Calculated Property
ρl	460.79	kg/m3	522.96	Calculated Property
ρl	253.13	kg/m3	566.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[171.15; 394.15]	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			4.98478e-02
Coefficient B			-9.58000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			171.15
Temperature range, max.			394.15
γ	0.03	N/m	171.15	Calculated Property
γ	0.03	N/m	195.93	Calculated Property
γ	0.03	N/m	220.71	Calculated Property
γ	0.03	N/m	245.48	Calculated Property
γ	0.02	N/m	270.26	Calculated Property
γ	0.02	N/m	295.04	Calculated Property
γ	0.02	N/m	319.82	Calculated Property
γ	0.02	N/m	344.59	Calculated Property
γ	0.01	N/m	369.37	Calculated Property
γ	0.01	N/m	394.15	Calculated Property
γ	[0.04; 7.93e-06]	N/m	[171.45; 556.62]	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			-1.44830e-01
Coefficient B			-2.78070e+00
Coefficient C			-1.55040e+00
Coefficient D			-9.12940e-04
Coefficient E			4.24160e-07
Comment			Range stopped where the equation turns negative; ChemSep gives it to 566.9 K.
Temperature range, min.			171.45
Temperature range, max.			556.62
γ	0.04	N/m	171.45	Calculated Property
γ	0.03	N/m	214.25	Calculated Property
γ	0.03	N/m	257.04	Calculated Property
γ	0.02	N/m	299.84	Calculated Property
γ	0.02	N/m	342.64	Calculated Property
γ	0.01	N/m	385.43	Calculated Property
γ	0.01	N/m	428.23	Calculated Property
γ	0.01	N/m	471.03	Calculated Property
γ	0.00	N/m	513.82	Calculated Property
γ	7.93e-06	N/m	556.62	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.10]	W/m×K	[171.45; 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			1.41090e-05
Coefficient B			1.35400e+00
Coefficient C			6.10510e+02
Coefficient D			-3.09150e+04
Temperature range, min.			171.45
Temperature range, max.			1000.00
λgas	0.00	W/m×K	171.45	Calculated Property
λgas	0.01	W/m×K	263.51	Calculated Property
λgas	0.02	W/m×K	355.57	Calculated Property
λgas	0.02	W/m×K	447.63	Calculated Property
λgas	0.03	W/m×K	539.69	Calculated Property
λgas	0.05	W/m×K	631.76	Calculated Property
λgas	0.06	W/m×K	723.82	Calculated Property
λgas	0.07	W/m×K	815.88	Calculated Property
λgas	0.09	W/m×K	907.94	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.07]	W/m×K	[171.45; 513.15]	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			3.52260e-02
Coefficient B			4.07540e+01
Coefficient C			-2.26680e+00
Coefficient D			9.22970e-04
Coefficient E			-6.03010e-06
Temperature range, min.			171.45
Temperature range, max.			513.15
λliquid	0.16	W/m×K	171.45	Calculated Property
λliquid	0.15	W/m×K	209.42	Calculated Property
λliquid	0.14	W/m×K	247.38	Calculated Property
λliquid	0.13	W/m×K	285.35	Calculated Property
λliquid	0.12	W/m×K	323.32	Calculated Property
λliquid	0.11	W/m×K	361.28	Calculated Property
λliquid	0.10	W/m×K	399.25	Calculated Property
λliquid	0.09	W/m×K	437.22	Calculated Property
λliquid	0.08	W/m×K	475.18	Calculated Property
λliquid	0.07	W/m×K	513.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Octene.

Mixtures

• 1-Propanol + 1-Octene
• 1-Octene + 1-Butanol
• 1-Octene + 1-Hexanol
• 1-Octene + 1-Octanol
• 1-Octene + 1-Decanol
• 1-Octene + N-Formylmorpholine
• 1-Octene + 2-Pyrrolidinone, 1-methyl-
• 1-Octene + 1,2-Ethanediol
• 1-Octene + Ethanol, 2,2'-oxybis-
• 1-Octene + Triethylene glycol
• 1-Hexene + 1-Octene
• 1-Octene + Octane
• 1-Octene + N,N-Dimethylacetamide
• Carbon monoxide + 1-Octene
• Carbon dioxide + 1-Octene
• Hydrogen + 1-Octene
• Carbon monoxide + Carbon dioxide + 1-Octene
• Hydrogen + Carbon dioxide + 1-Octene
• 1-Octene + Thiophene, 2-methyl-
• 1-Octene + Propanamide, N,N-bis(2-ethylhexyl)-2-methyl-

Find more mixtures with 1-Octene.

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
• 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
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
• Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
• 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)
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• 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)
• 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• 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
• 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]
• 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
• 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
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• 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
• 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
• Interactions of volatile organic compounds with 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 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
• 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
• 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
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• 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
• 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
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• 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
• 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
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• 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
• 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
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• 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
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• 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
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Measurements of the Thermal Conductivity of n-Octane, Isooctane, 1-Octene, and 1-Octanol in the Temperature Range from 253 to 393 K at Pressures up to 30 MPa
• 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
• 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
• Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• 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
• Viscosity and Diffusivity for the Ionic Liquid 1-Hexyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)amide with 1-Octene
• 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 by GLC in Alkanediamines as Stationary Phases
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Chemical Equilibrium of the Liquid-Phase Dehydration of 1-Octanol to 1-(Octyloxy)octane
• Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
• Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 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
• 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
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Solubilities of CO and H2 in Neat and CO2-Expanded Hydroformylation Reaction Mixtures Containing 1-Octene and Nonanal up to 353.15 K and 9 MPa
• Phase Equilibrium, Volumetric, and Interfacial Properties of the Ionic Liquid, 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide and 1-Octene
• 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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